CN104864623A - Thermodynamic combined supply system - Google Patents

Thermodynamic combined supply system Download PDF

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Publication number
CN104864623A
CN104864623A CN201510043920.6A CN201510043920A CN104864623A CN 104864623 A CN104864623 A CN 104864623A CN 201510043920 A CN201510043920 A CN 201510043920A CN 104864623 A CN104864623 A CN 104864623A
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absorber
communicated
solution
generator
heat exchanger
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CN201510043920.6A
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CN104864623B (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
    • F01K17/02—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B27/00—Machines, plants or systems, using particular sources of energy
    • F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems
    • Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/14—Combined heat and power generation [CHP]

Abstract

The invention provides a thermodynamic combined supply system, and belongs to the technical field of thermodynamic combined supply and heat pumps. A power machine provides second steam for a second evaporator, and provides exhaust steam for an evaporator, a second generator and a generator; the generator, the second generator, an absorber, a second absorber, a third absorber, a solution pump, a second solution pump, a solution heat exchanger, a second solution heat exchanger and a solution throttle valve form a solution circulation loop with a backheating cooling end; the second generator provides refrigerant steam for the third absorber; the generator provides refrigerant steam for a condenser; the condenser correspondingly provides a coolant for the evaporator and the second evaporator through a coolant pump and a second coolant pump; the evaporator and the second evaporator correspondingly provide coolant steam for the absorber and the second absorber; the condenser and the third absorber discharge heat to a cooling medium; the absorber and the second absorber supply heat to the heated medium, so that the thermodynamic combined supply system is formed.

Description

The dynamic co-feeding system of heat
Technical field:
The invention belongs to dynamic (electricity) alliance of heat and technical field of heat pumps.
Background technology:
The dynamic alliance of heat or cogeneration, follow thermal energy step and utilize principle, have higher heat utilization rate.Corresponding technical scheme generally comprises: (1) is improved engine outlet steam discharge parameter and carried out heat supply; (2) utilize engine intermediate extraction or segmentation to draw gas and carry out heat supply; (3) engine intermediate extraction is adopted to be that the high temperature heat source of first-class absorption type heat pump carrys out recovery section exhaust steam heat and carries out heat supply.But, making full use of all not to cold environment in the dynamic jointly-supplying technology measure of these heat.
For the situation that heated medium range of temperature is wider, adopt multiterminal heat supply second-kind absorption-type heat pump principle, carry out segmentation to engine to draw gas, meet the heat demand under different situations and the rationalization realizing heat energy utilization, and make full use of engine and draw gas or the temperature difference between steam discharge and cold environment, to realize effective utilization of the temperature difference.
Consider that/multiple concrete the operating mode such as thermic load that between steam discharge and cold environment, the height of temperature difference size, cold ambient temperature, steam discharge contain is how many taken out by heat user thermal parameter and thermic load, engine, need to provide multiple concrete technical scheme.
Summary of the invention:
Main purpose of the present invention to provide heat dynamic co-feeding system, and concrete summary of the invention subitem is described below:
1. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter and generator successively after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser also has cooling medium pipeline and ft connection, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger and the second solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, engine also has exhaust passage to be communicated with absorber, and engine also has the second steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Condenser also has cooling medium pipeline and ft connection, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, that heat described in the 1st is moved in co-feeding system, engine is had exhaust passage be communicated with successively evaporimeter and generator after generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, engine is had the second steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the second condensate liquid pipeline and ft connection to be adjusted to engine again to have the second steam channel to be communicated with evaporimeter have the second condensate liquid pipeline and ft connection again, the second evaporimeter after the 3rd steam channel is communicated with the second evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, that heat described in the 2nd is moved in co-feeding system, cancel the exhaust passage that engine is communicated with absorber, being had by engine the second steam channel to be communicated with the second absorber to be adjusted to engine has the second steam channel to be communicated with absorber, engine is set up the 3rd steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser also has cooling medium pipeline and ft connection, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger and the second solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Condenser also has cooling medium pipeline and ft connection, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, that heat described in the 5th is moved in co-feeding system, engine is had the second steam channel be communicated with successively evaporimeter and generator after generator have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, that heat described in the 6th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter, the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine also has exhaust passage to be communicated with absorber, and engine also has the second steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, that heat described in the 9th is moved in co-feeding system, exhaust passage is had to be communicated with evaporimeter successively in engine, second generator and generator after generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine is had the second steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the second condensate liquid pipeline and ft connection to be adjusted to engine again to have the second steam channel to be communicated with evaporimeter have the second condensate liquid pipeline and ft connection again, the second evaporimeter after the 3rd steam channel is communicated with the second evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
12. main heat move co-feeding system, that heat described in the 10th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the second steam channel to be communicated with the second absorber to be adjusted to engine has the second steam channel to be communicated with absorber, engine is set up the 3rd steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
14. main heat moves co-feeding system, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, that heat described in the 13rd is moved in co-feeding system, engine is had the second steam channel be communicated with successively evaporimeter and generator after generator have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, that heat described in the 14th is moved in co-feeding system, cancelling engine has the second steam channel to be communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with evaporimeter, the second generator and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
18. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with the second generator and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, that heat described in the 17th is moved in co-feeding system, the second steam channel is had by engine to be communicated with evaporimeter successively, second generator and generator after generator have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with the second generator and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, that heat described in the 18th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with the second generator after the second generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with evaporimeter and generator successively after generator have the 3rd condensate liquid pipeline and ft connection again, engine also have the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter have the 4th condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
22. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with the second generator after the second generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with generator after generator have the 3rd condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with absorber, and engine also has the 4th steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, that heat described in the 21st is moved in co-feeding system, engine is had the 3rd steam channel be communicated with successively evaporimeter and generator after generator have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine have the 3rd steam channel be communicated with generator after generator have the 3rd condensate liquid pipeline and ft connection again, engine is had the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine again to have the 4th steam channel to be communicated with evaporimeter have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter after the 5th steaming passage is communicated with the second evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, that heat described in the 22nd is moved in co-feeding system, cancel the 3rd steam channel that engine is communicated with absorber, being had by engine the 4th steam channel to be communicated with the second absorber to be adjusted to engine has the 4th steam channel to be communicated with absorber, engine is set up the 5th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 25. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter, the 3rd evaporimeter and generator successively after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, steam chest is divided to have concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with the 3rd absorber, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, second condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, engine also has exhaust passage to be communicated with the 3rd absorber, engine also has exhaust passage to be communicated with absorber, and engine also has the second steam channel to be communicated with the second absorber; Steam chest is divided to have concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and the 3rd absorber, divide steam chest to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, and the second condenser also has cryogen liquid pipeline through the second cryogen liquid pump and ft connection; Condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, that heat described in the 25th is moved in co-feeding system, exhaust passage is had to be communicated with evaporimeter successively in engine, 3rd evaporimeter and generator after generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with the 3rd evaporimeter and generator successively after generator have condensate liquid pipeline and ft connection again, engine is had the second steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the second condensate liquid pipeline and ft connection to be adjusted to engine again to have the second steam channel to be communicated with evaporimeter have the second condensate liquid pipeline and ft connection again, the second evaporimeter after the 3rd steam channel is communicated with the second evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, that heat described in the 26th is moved in co-feeding system, cancel the exhaust passage that engine is communicated with absorber, being had by engine the second steam channel to be communicated with the second absorber to be adjusted to engine has the second steam channel to be communicated with absorber, engine is set up the 3rd steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 29. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with evaporimeter and the 3rd evaporimeter successively after the 3rd evaporimeter have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, steam chest is divided to have concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with the 3rd absorber, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, second condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the 3rd absorber, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber; Steam chest is divided to have concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and the 3rd absorber, divide steam chest to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, and the second condenser also has cryogen liquid pipeline through the second cryogen liquid pump and ft connection; Condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, that heat described in the 29th is moved in co-feeding system, engine is had the second steam channel be communicated with successively evaporimeter and the 3rd evaporimeter after the 3rd evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with the 3rd evaporimeter after the 3rd evaporimeter have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, that heat described in the 30th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 33. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with evaporimeter, the 3rd evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, steam chest is divided to have concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with the 3rd absorber, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, second condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 34. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the 3rd absorber, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber; Steam chest is divided to have concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and the 3rd absorber, divide steam chest to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, and the second condenser also has cryogen liquid pipeline through the second cryogen liquid pump and ft connection; Condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 35. heat, that heat described in the 33rd is moved in co-feeding system, the second steam channel is had by engine to be communicated with evaporimeter successively, 3rd evaporimeter and generator after generator have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with the 3rd evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 36. heat, that heat described in the 34th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 37. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with evaporimeter and the 3rd evaporimeter successively after the 3rd evaporimeter have the 3rd condensate liquid pipeline and ft connection again, engine also have the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter have the 4th condensate liquid pipeline and ft connection again, steam chest is divided to have concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with the 3rd absorber, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, second condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 38. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with the 3rd absorber, engine also has the 3rd steam channel to be communicated with absorber, and engine also has the 4th steam channel to be communicated with the second absorber; Steam chest is divided to have concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and the 3rd absorber, divide steam chest to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with generator through the 3rd solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second condenser, and the second condenser also has cryogen liquid pipeline through the second cryogen liquid pump and ft connection; Condenser and the second condenser also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, that heat described in the 37th is moved in co-feeding system, engine is had the 3rd steam channel be communicated with successively evaporimeter and the 3rd evaporimeter after the 3rd evaporimeter have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine have the 3rd steam channel be communicated with the 3rd evaporimeter after the 3rd evaporimeter have the 3rd condensate liquid pipeline and ft connection again, engine is had the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine again to have the 4th steam channel to be communicated with evaporimeter have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter after the 5th steam channel is communicated with the second evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 40. heat, that heat described in the 38th is moved in co-feeding system, cancel the 3rd steam channel that engine is communicated with absorber, being had by engine the 4th steam channel to be communicated with the second absorber to be adjusted to engine has the 4th steam channel to be communicated with absorber, engine is set up the 5th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter, the 3rd evaporimeter and generator successively after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively again, cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with the second evaporimeter, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 42. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter and generator successively after generator have condensate liquid pipeline and ft connection again, engine also has exhaust passage to be communicated with absorber, and engine also has the second steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline again through the second cryogen liquid pump and ft connection; Second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, and evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber; Condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 43. heat, that heat described in the 41st is moved in co-feeding system, exhaust passage is had to be communicated with evaporimeter successively in engine, 3rd evaporimeter and generator after generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with the 3rd evaporimeter and generator successively after generator have condensate liquid pipeline and ft connection again, engine is had the second steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the second condensate liquid pipeline and ft connection to be adjusted to engine again to have the second steam channel to be communicated with evaporimeter have the second condensate liquid pipeline and ft connection again, the second evaporimeter after the 3rd steam channel is communicated with the second evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 44. heat, that heat described in the 42nd is moved in co-feeding system, cancel the exhaust passage that engine is communicated with absorber, being had by engine the second steam channel to be communicated with the second absorber to be adjusted to engine has the second steam channel to be communicated with absorber, engine is set up the 3rd steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 45. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with evaporimeter and the 3rd evaporimeter successively after the 3rd evaporimeter have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively again, cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with the second evaporimeter, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 46. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, the finisher that engine also has the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline again through the second cryogen liquid pump and ft connection; Second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, and evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber; Condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 47. heat, that heat described in the 45th is moved in co-feeding system, engine is had the second steam channel be communicated with successively evaporimeter and the 3rd evaporimeter after the 3rd evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with the 3rd evaporimeter after the 3rd evaporimeter have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, that heat described in the 46th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with evaporimeter, the 3rd evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively again, cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with the second evaporimeter, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 50. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline again through the second cryogen liquid pump and ft connection; Second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, and evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber; Condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 51. heat, that heat described in the 49th is moved in co-feeding system, the second steam channel is had by engine to be communicated with evaporimeter successively, 3rd evaporimeter and generator after generator have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with the 3rd evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 52. heat, that heat described in the 50th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 53. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with evaporimeter and the 3rd evaporimeter successively after the 3rd evaporimeter have the 3rd condensate liquid pipeline and ft connection again, engine also have the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter have the 4th condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively again, cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with the second evaporimeter, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, and the 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 54. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, the finisher that engine also has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with absorber, and engine also has the 4th steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline again through the second cryogen liquid pump and ft connection; Second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, and evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber; Condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 55. heat, that heat described in the 53rd is moved in co-feeding system, engine is had the 3rd steam channel be communicated with successively evaporimeter and the 3rd evaporimeter after the 3rd evaporimeter have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine have the 3rd steam channel be communicated with the 3rd evaporimeter after the 3rd evaporimeter have the 3rd condensate liquid pipeline and ft connection again, engine is had the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine again to have the 4th steam channel to be communicated with evaporimeter have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter after the 5th steam channel is communicated with the second evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 56. heat, that heat described in the 54th is moved in co-feeding system, cancel the 3rd steam channel that engine is communicated with absorber, being had by engine the 4th steam channel to be communicated with the second absorber to be adjusted to engine has the 4th steam channel to be communicated with absorber, engine is set up the 5th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 57. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger and the 3rd cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter and generator successively after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively again, cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with the second evaporimeter, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through the 3rd cryogen liquid pump, and evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 58. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator after generator have condensate liquid pipeline and ft connection again, engine also has exhaust passage to be communicated with the 3rd absorber, engine also has exhaust passage to be communicated with absorber, and engine also has the second steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline again through the second cryogen liquid pump and ft connection; Second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 59. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger and the 3rd cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively again, cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with the second evaporimeter, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through the 3rd cryogen liquid pump, and evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 60. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the 3rd absorber with absorber respectively, and engine also has the 3rd steam channel to be communicated with the second absorber; Generator also has concentrated solution pipeline to be communicated with the second absorber with the second solution heat exchanger through solution pump, solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline again through the second cryogen liquid pump and ft connection; Second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection; Condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 61. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter, the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
62. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine also has exhaust passage to be communicated with absorber, and engine also has the second steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 63. heat, that heat described in the 61st is moved in co-feeding system, exhaust passage is had to be communicated with evaporimeter successively in engine, second generator and generator after generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine is had the second steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the second condensate liquid pipeline and ft connection to be adjusted to engine again to have the second steam channel to be communicated with evaporimeter have the second condensate liquid pipeline and ft connection again, the second evaporimeter after the 3rd steam channel is communicated with the second evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 64. heat, that heat described in the 62nd is moved in co-feeding system, cancel the exhaust passage that engine is communicated with absorber, being had by engine the second steam channel to be communicated with the second absorber to be adjusted to engine has the second steam channel to be communicated with absorber, engine is set up the 3rd steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 65. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with evaporimeter and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
66. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 67. heat, that heat described in the 65th is moved in co-feeding system, engine is had the second steam channel be communicated with successively evaporimeter and generator after generator have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 68. heat, that heat described in the 66th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 69. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with evaporimeter, the second generator and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
70. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with the second generator and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with absorber, and engine also has the 3rd steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 71. heat, that heat described in the 69th is moved in co-feeding system, the second steam channel is had by engine to be communicated with evaporimeter successively, second generator and generator after generator have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with the second generator and generator successively after generator have the second condensate liquid pipeline and ft connection again, engine is had the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again to have the 3rd steam channel to be communicated with evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter after the 4th steam channel is communicated with the second evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 72. heat, that heat described in the 70th is moved in co-feeding system, cancel the second steam channel that engine is communicated with absorber, being had by engine the 3rd steam channel to be communicated with the second absorber to be adjusted to engine has the 3rd steam channel to be communicated with absorber, engine is set up the 4th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 73. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with the second generator after the second generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with evaporimeter and generator successively after generator have the 3rd condensate liquid pipeline and ft connection again, engine also have the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter have the 4th condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
74. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine also has exhaust passage and ft connection, engine also have the second steam channel be communicated with the second generator after the second generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with generator after generator have the 3rd condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with absorber, and engine also has the 4th steam channel to be communicated with the second absorber, second generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the 3rd absorber through solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the 3rd absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 75. heat, that heat described in the 73rd is moved in co-feeding system, engine is had the 3rd steam channel be communicated with successively evaporimeter and generator after generator have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine have the 3rd steam channel be communicated with generator after generator have the 3rd condensate liquid pipeline and ft connection to adjust again, engine is had the 4th steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine again to have the 4th steam channel to be communicated with evaporimeter have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter after the 5th steam channel is communicated with the second evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 76. heat, that heat described in the 74th is moved in co-feeding system, cancel the 3rd steam channel that engine is communicated with absorber, being had by engine the 4th steam channel to be communicated with the second absorber to be adjusted to engine has the 4th steam channel to be communicated with absorber, engine is set up the 5th steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 77. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, solution choke valve, the 3rd generator, the 4th absorber and the 3rd solution pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with evaporimeter, the 3rd generator, the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the 4th absorber with the 3rd solution heat exchanger through the second solution pump, 4th absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd generator through solution choke valve, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with the 4th absorber, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser, the 3rd absorber and the 4th absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 78. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, solution choke valve, the 3rd generator, the 4th absorber and the 3rd solution pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the 3rd generator, the second generator and generator successively after generator have condensate liquid pipeline and ft connection again, engine also has exhaust passage to be communicated with absorber, and engine also has the second steam channel to be communicated with the second absorber, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second absorber with the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the 4th absorber with the 3rd solution heat exchanger through the second solution pump, 4th absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd generator through solution choke valve, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with the 4th absorber, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and ft connection, condenser, the 3rd absorber and the 4th absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second absorber also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 79. heat, that heat shown in the 77th is moved in co-feeding system, exhaust passage is had to be communicated with evaporimeter successively in engine, 3rd generator, second generator and generator after generator have condensate liquid pipeline and ft connection to be adjusted to engine again has exhaust passage to be communicated with the 3rd generator successively, after second generator and generator, generator has condensate liquid pipeline and ft connection again, engine is had the second steam channel be communicated with the second evaporimeter after the second evaporimeter finisher of having the second condensate liquid pipeline and ft connection to be adjusted to engine again to have the second steam channel to be communicated with evaporimeter have the second condensate liquid pipeline and ft connection again, the second evaporimeter after the 3rd steam channel is communicated with the second evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 80. heat, that heat shown in the 78th is moved in co-feeding system, cancel the exhaust passage that engine is communicated with absorber, being had by engine the second steam channel to be communicated with the second absorber to be adjusted to engine has the second steam channel to be communicated with absorber, engine is set up the 3rd steam channel and is communicated with the second absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 81. heat, that heat described in the 1st is moved in co-feeding system, increase by the 3rd absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 3rd absorber with the 3rd solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, the 3rd evaporimeter after the 3rd steam channel is communicated with the 3rd evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 82. heat, that heat described in the 2nd is moved in co-feeding system, increase the 3rd absorber and the 3rd solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 3rd absorber with the 3rd solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, engine is set up the 3rd steam channel and is communicated with the 3rd absorber, 3rd absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 83. heat, that heat described in the 3rd or the 5th is moved in co-feeding system, increase by the 3rd absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 3rd absorber with the 3rd solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, the 3rd evaporimeter after the 4th steam channel is communicated with the 3rd evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 84. heat, that heat described in the 4th or the 6th is moved in co-feeding system, increase the 3rd absorber and the 3rd solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 3rd absorber with the 3rd solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 3rd absorber, 3rd absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 85. heat, that heat described in the 7th is moved in co-feeding system, increase by the 3rd absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 3rd absorber with the 3rd solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, the 3rd evaporimeter after the 5th steam channel is communicated with the 3rd evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 86. heat, that heat described in the 8th is moved in co-feeding system, increase the 3rd absorber and the 3rd solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 3rd absorber with the 3rd solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, engine is set up the 5th steam channel and is communicated with the 3rd absorber, 3rd absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 87. heat, that heat described in the 9th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 3rd steam channel is communicated with the 3rd evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 88. heat, that heat described in the 10th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 3rd steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 89. heat, the 11st, 13, arbitrary heat described in 17 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 4th steam channel is communicated with the 3rd evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 90. heat, the 12nd, 14, heat described in 18 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 91. heat, the 15th, 19, arbitrary heat described in 21 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 5th steam channel is communicated with the 3rd evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 92. heat, the 16th, 20, arbitrary heat described in 22 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 5th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 93. heat, that heat described in the 23rd is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 6th steam channel is communicated with the 3rd evaporimeter set up by engine the 6th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 94. heat, that heat described in the 24th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 6th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 95. heat, that heat described in the 25th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 4th evaporimeter after the 3rd steam channel is communicated with the 4th evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter through the 4th cryogen liquid pump, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 96. heat, that heat described in the 26th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 3rd steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 97. heat, the 27th, 29, arbitrary heat described in 33 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, steam chest will be divided to have concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to a point steam chest and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 4th evaporimeter after the 4th steam channel is communicated with the 4th evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter through the 4th cryogen liquid pump, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 98. heat, the 28th, 30, arbitrary heat described in 34 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, steam chest will be divided to have concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to a point steam chest and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 99. heat, the 31st, 35, arbitrary heat described in 37 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, steam chest will be divided to have concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to a point steam chest and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 4th evaporimeter after the 5th steam channel is communicated with the 4th evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter through the 4th cryogen liquid pump, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 100. heat, the 32nd, 36, arbitrary heat described in 38 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, steam chest will be divided to have concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to a point steam chest and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 5th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 101. heat, that heat described in the 39th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, steam chest will be divided to have concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to a point steam chest and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 4th evaporimeter after the 6th steam channel is communicated with the 4th evaporimeter set up by engine the 6th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter through the 4th cryogen liquid pump, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 102. heat, that heat described in the 40th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, steam chest will be divided to have concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to a point steam chest and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 6th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 103. heat, that heat described in the 41st is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, generator is had refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively to be again adjusted to generator have refrigerant steam channel be communicated with the second generator after the second generator have again cryogen liquid pipeline respectively with cryogen liquid pump, second cryogen liquid pump is communicated with the 4th cryogen liquid pump, 4th cryogen liquid pump also has cryogen liquid pipeline to be communicated with the 4th evaporimeter, the 4th evaporimeter after the 3rd steam channel is communicated with the 4th evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 104. heat, that heat described in the 42nd is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 3rd steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 105. heat, the 43rd, 45, arbitrary heat described in 49 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, generator is had refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively to be again adjusted to generator have refrigerant steam channel be communicated with the second generator after the second generator have again cryogen liquid pipeline respectively with cryogen liquid pump, second cryogen liquid pump is communicated with the 4th cryogen liquid pump, 4th cryogen liquid pump also has cryogen liquid pipeline to be communicated with the 4th evaporimeter, the 4th evaporimeter after the 4th steam channel is communicated with the 4th evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 106. heat, the 44th, 46, arbitrary heat described in 50 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 107. heat, the 47th, 51, arbitrary heat described in 53 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, generator is had refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively to be again adjusted to generator have refrigerant steam channel be communicated with the second generator after the second generator have again cryogen liquid pipeline respectively with cryogen liquid pump, second cryogen liquid pump is communicated with the 4th cryogen liquid pump, 4th cryogen liquid pump also has cryogen liquid pipeline to be communicated with the 4th evaporimeter, the 4th evaporimeter after the 5th steam channel is communicated with the 4th evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 108. heat, the 48th, 52, arbitrary heat described in 54 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 5th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 109. heat, that heat described in the 55th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, generator is had refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively to be again adjusted to generator have refrigerant steam channel be communicated with the second generator after the second generator have again cryogen liquid pipeline respectively with cryogen liquid pump, second cryogen liquid pump is communicated with the 4th cryogen liquid pump, 4th cryogen liquid pump also has cryogen liquid pipeline to be communicated with the 4th evaporimeter, the 4th evaporimeter after the 6th steam channel is communicated with the 4th evaporimeter set up by engine the 6th condensate liquid pipeline and ft connection again, 4th evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 110. heat, that heat described in the 56th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 6th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 111. heat, that heat described in the 57th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 4th cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, generator is had refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively to be again adjusted to generator have refrigerant steam channel be communicated with the second generator after the second generator have again cryogen liquid pipeline respectively with cryogen liquid pump, second cryogen liquid pump is communicated with the 4th cryogen liquid pump, 4th cryogen liquid pump also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter, the 3rd evaporimeter after the 3rd steam channel is communicated with the 3rd evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 112. heat, that heat described in the 58th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 3rd steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 113. heat, that heat described in the 59th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 4th cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, generator is had refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump with cryogen liquid pump respectively to be again adjusted to generator have refrigerant steam channel be communicated with the second generator after the second generator have again cryogen liquid pipeline respectively with cryogen liquid pump, second cryogen liquid pump is communicated with the 4th cryogen liquid pump, 4th cryogen liquid pump also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter, the 3rd evaporimeter after the 4th steam channel is communicated with the 3rd evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 114. heat, that heat described in the 60th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 115. heat, that heat described in the 61st is moved in co-feeding system, increase by the 4th absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 3rd solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, the 3rd evaporimeter after the 3rd steam channel is communicated with the 3rd evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 116. heat, that heat described in the 62nd is moved in co-feeding system, increase the 4th absorber and the 3rd solution heat exchanger, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 3rd solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, engine is set up the 3rd steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 117. heat, that heat described in the 65th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 4th steam channel is communicated with the 3rd evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 118. heat, that heat described in the 66th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 119. heat, the 63rd, arbitrary heat described in 69 is moved in co-feeding system, increase by the 4th absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 3rd solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, the 3rd evaporimeter after the 4th steam channel is communicated with the 3rd evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 120. heat, the 64th, 70 described arbitrary heat are moved in co-feeding system, increase the 4th absorber and the 3rd solution heat exchanger, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 3rd solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 121. heat, that heat described in the 71st is moved in co-feeding system, increase by the 4th absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 3rd solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, the 3rd evaporimeter after the 5th steam channel is communicated with the 3rd evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 122. heat, that heat described in the 72nd is moved in co-feeding system, increase the 4th absorber and the 3rd solution heat exchanger, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 3rd solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger again, engine is set up the 5th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 123. heat, the 67th, arbitrary heat described in 73 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 5th steam channel is communicated with the 3rd evaporimeter set up by engine the 5th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 124. heat, the 68th, 74 described arbitrary heat are moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 5th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 125. heat, that heat described in the 75th is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 6th steam channel is communicated with the 3rd evaporimeter set up by engine the 6th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 126. heat, that heat described in the 76th is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, second generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to the second generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 4th absorber with the 4th solution heat exchanger, 4th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 6th steam channel and is communicated with the 4th absorber, 4th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 127. heat, that heat described in the 77th is moved in co-feeding system, increase by the 5th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 5th absorber with the 4th solution heat exchanger, 5th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 3rd steam channel is communicated with the 3rd evaporimeter set up by engine the 3rd condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 128. heat, that heat described in the 78th is moved in co-feeding system, increase the 5th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 5th absorber with the 4th solution heat exchanger, 5th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 3rd steam channel and is communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 129. heat, that heat described in the 79th is moved in co-feeding system, increase by the 5th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 5th absorber with the 4th solution heat exchanger, 5th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, the 3rd evaporimeter after the 4th steam channel is communicated with the 3rd evaporimeter set up by engine the 4th condensate liquid pipeline and ft connection again, condenser is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter through the 3rd cryogen liquid pump, 3rd evaporimeter also has refrigerant steam channel to be communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 130. heat, that heat described in the 80th is moved in co-feeding system, increase the 5th absorber and the 4th solution heat exchanger, generator there is concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with the second absorber and are adjusted to generator and have concentrated solution pipeline through solution pump, solution heat exchanger, second solution heat exchanger is communicated with the 5th absorber with the 4th solution heat exchanger, 5th absorber has weak solution pipeline to be communicated with the second absorber through the 4th solution heat exchanger again, engine is set up the 4th steam channel and is communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 131. heat, be that arbitrary heat described in 1-40,61-80 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber and the second absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased second absorber, newly-increased condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 132. heat, be that arbitrary heat described in 41-60 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, 3rd absorber, absorber and the second absorber there are heated medium pipeline and ft connection to be adjusted to the 3rd absorber respectively and have that circulating thermal medium pipeline is communicated with absorber successively, the second absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter have circulating thermal medium pipeline be communicated with the 3rd absorber and form closed-loop path with circulating pump after circulating pump again, newly-increased absorber, newly-increased second absorber, newly-increased condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 133. heat, be in the arbitrary dynamic co-feeding system of the heat described in 81-86 item, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 3rd absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 3rd absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased second absorber, newly-increased condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 134. heat, be that arbitrary heat described in 87-102 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 4th absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 4th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased second absorber, newly-increased condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 135. heat, be that arbitrary heat described in 103-114 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, by the 3rd absorber, absorber, second absorber and the 4th absorber have heated medium pipeline and ft connection to be adjusted to the 3rd absorber respectively has circulating thermal medium pipeline to be communicated with absorber successively, second absorber, 4th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter has circulating thermal medium pipeline be communicated with the 3rd absorber and form closed-loop path with circulating pump after circulating pump again, newly-increased absorber, newly-increased second absorber, newly-increased condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 136. heat, be that arbitrary heat described in 115-126 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 4th absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 4th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased second absorber, newly-increased condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 137. heat, be that arbitrary heat described in 127-130 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased second solution heat exchanger through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased second solution heat exchanger, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 5th absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 5th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased second absorber, newly-increased condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 138. heat, that arbitrary heat described in 131-137 item is moved in co-feeding system, increase newly-increased 3rd generator, newly-increased 3rd absorber, newly-increased 3rd solution pump and newly-increased 3rd solution heat exchanger, had by newly-increased absorber weak solution pipeline to be communicated with newly-increased second absorber through newly-increased solution pump and newly-increased solution heat exchanger to be adjusted to newly-increased absorber and to have weak solution pipeline warp to increase solution pump newly to be communicated with newly-increased 3rd absorber with newly-increased solution heat exchanger, newly-increased 3rd absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased 3rd solution heat exchanger through newly-increased 3rd solution pump again, had by newly-increased second generator concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger to be adjusted to newly-increased second generator and to have concentrated solution pipeline warp to increase the 3rd solution heat exchanger newly to be communicated with newly-increased 3rd generator, newly-increased 3rd generator has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger again, newly-increased 3rd generator also has refrigerant steam channel to be communicated with newly-increased 3rd absorber, had by newly-increased second generator circulating thermal medium pipeline to be communicated with newly-increased evaporimeter through newly-increased heat exchanger to be adjusted to newly-increased second generator and to have circulating thermal medium pipeline warp to increase the 3rd generator newly to be communicated with newly-increased evaporimeter with newly-increased heat exchanger, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 139. heat, be that arbitrary heat described in 1-40,61-80 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator through solution choke valve, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased generator through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest with newly-increased second absorber through newly-increased second solution choke valve, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, a newly-increased point steam chest also has refrigerant steam channel to be communicated with newly-increased second condenser, newly-increased second condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased second throttle, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber and the second absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased condenser, newly-increased second condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 140. heat, be that arbitrary heat described in 41-60 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator through solution choke valve, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased generator through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest with newly-increased second absorber through newly-increased second solution choke valve, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, a newly-increased point steam chest also has refrigerant steam channel to be communicated with newly-increased second condenser, newly-increased second condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased second throttle, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, 3rd absorber, absorber and the second absorber there are heated medium pipeline and ft connection to be adjusted to the 3rd absorber respectively and have that circulating thermal medium pipeline is communicated with absorber successively, the second absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter have circulating thermal medium pipeline be communicated with the 3rd absorber and form closed-loop path with circulating pump after circulating pump again, newly-increased absorber, newly-increased condenser, newly-increased second condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 141. heat, be that arbitrary heat described in 81-86 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator through solution choke valve, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased generator through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest with newly-increased second absorber through newly-increased second solution choke valve, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, a newly-increased point steam chest also has refrigerant steam channel to be communicated with newly-increased second condenser, newly-increased second condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased second throttle, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 3rd absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 3rd absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased condenser, newly-increased second condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 142. heat, be that arbitrary heat described in 87-102 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator through solution choke valve, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased generator through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest with newly-increased second absorber through newly-increased second solution choke valve, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, a newly-increased point steam chest also has refrigerant steam channel to be communicated with newly-increased second condenser, newly-increased second condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased second throttle, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 4th absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 4th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased condenser, newly-increased second condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 143. heat, be that arbitrary heat described in 103-114 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator through solution choke valve, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased generator through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest with newly-increased second absorber through newly-increased second solution choke valve, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, a newly-increased point steam chest also has refrigerant steam channel to be communicated with newly-increased second condenser, newly-increased second condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased second throttle, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, by the 3rd absorber, absorber, second absorber and the 4th absorber have heated medium pipeline and ft connection to be adjusted to the 3rd absorber respectively has circulating thermal medium pipeline to be communicated with absorber successively, second absorber, 4th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter has circulating thermal medium pipeline be communicated with the 3rd absorber and form closed-loop path with circulating pump after circulating pump again, newly-increased absorber, newly-increased condenser, newly-increased second condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 144. heat, be that arbitrary heat described in 115-126 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator through solution choke valve, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased generator through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest with newly-increased second absorber through newly-increased second solution choke valve, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, a newly-increased point steam chest also has refrigerant steam channel to be communicated with newly-increased second condenser, newly-increased second condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased second throttle, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 4th absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 4th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased condenser, newly-increased second condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 145. heat, be that arbitrary heat described in 127-130 item is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber also has weak solution pipeline to be communicated with newly-increased second generator through solution choke valve, newly-increased second generator also has concentrated solution pipeline to be communicated with newly-increased generator through newly-increased second solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with a newly-increased point steam chest with newly-increased second absorber through newly-increased second solution choke valve, a newly-increased point steam chest also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with newly-increased second absorber, newly-increased second generator also has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased choke valve, a newly-increased point steam chest also has refrigerant steam channel to be communicated with newly-increased second condenser, newly-increased second condenser also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter through newly-increased second throttle, newly-increased evaporimeter also has refrigerant steam channel to be communicated with newly-increased absorber, absorber, the second absorber and the 5th absorber are had heated medium pipeline and ft connection to be adjusted to absorber respectively to have circulating thermal medium pipeline to be communicated with the second absorber, the 5th absorber, newly-increased generator, newly-increased second generator, newly-increased heat exchanger, newly-increased evaporimeter and circulating pump after circulating pump successively to have circulating thermal medium pipeline be communicated with absorber and form closed-loop path again, newly-increased absorber, newly-increased condenser, newly-increased second condenser and newly-increased heat exchanger also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
Accompanying drawing illustrates:
Fig. 1 moves co-feeding system the 1st kind of principled thermal system figure according to heat provided by the present invention.
Fig. 2 moves co-feeding system the 2nd kind of principled thermal system figure according to heat provided by the present invention.
Fig. 3 moves co-feeding system the 3rd kind of principled thermal system figure according to heat provided by the present invention.
Fig. 4 moves co-feeding system the 4th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 5 moves co-feeding system the 5th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 6 moves co-feeding system the 6th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 7 moves co-feeding system the 7th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 8 moves co-feeding system the 8th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 9 moves co-feeding system the 9th kind of principled thermal system figure according to heat provided by the present invention.
Figure 10 moves co-feeding system the 10th kind of principled thermal system figure according to heat provided by the present invention.
Figure 11 moves co-feeding system the 11st kind of principled thermal system figure according to heat provided by the present invention.
Figure 12 moves co-feeding system the 12nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 13 moves co-feeding system the 13rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 14 moves co-feeding system the 14th kind of principled thermal system figure according to heat provided by the present invention.
Figure 15 moves co-feeding system the 15th kind of principled thermal system figure according to heat provided by the present invention.
Figure 16 moves co-feeding system the 16th kind of principled thermal system figure according to heat provided by the present invention.
Figure 17 moves co-feeding system the 17th kind of principled thermal system figure according to heat provided by the present invention.
Figure 18 moves co-feeding system the 18th kind of principled thermal system figure according to heat provided by the present invention.
Figure 19 moves co-feeding system the 19th kind of principled thermal system figure according to heat provided by the present invention.
Figure 20 moves co-feeding system the 20th kind of principled thermal system figure according to heat provided by the present invention.
Figure 21 moves co-feeding system the 21st kind of principled thermal system figure according to heat provided by the present invention.
Figure 22 moves co-feeding system the 22nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 23 moves co-feeding system the 23rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 24 moves co-feeding system the 24th kind of principled thermal system figure according to heat provided by the present invention.
Figure 25 moves co-feeding system the 25th kind of principled thermal system figure according to heat provided by the present invention.
Figure 26 moves co-feeding system the 26th kind of principled thermal system figure according to heat provided by the present invention.
Figure 27 moves co-feeding system the 27th kind of principled thermal system figure according to heat provided by the present invention.
Figure 28 moves co-feeding system the 28th kind of principled thermal system figure according to heat provided by the present invention.
Figure 29 moves co-feeding system the 29th kind of principled thermal system figure according to heat provided by the present invention.
Figure 30 moves co-feeding system the 30th kind of principled thermal system figure according to heat provided by the present invention.
Figure 31 moves co-feeding system the 31st kind of principled thermal system figure according to heat provided by the present invention.
Figure 32 moves co-feeding system the 32nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 33 moves co-feeding system the 33rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 34 moves co-feeding system the 34th kind of principled thermal system figure according to heat provided by the present invention.
Figure 35 moves co-feeding system the 35th kind of principled thermal system figure according to heat provided by the present invention.
Figure 36 moves co-feeding system the 36th kind of principled thermal system figure according to heat provided by the present invention.
Figure 37 moves co-feeding system the 37th kind of principled thermal system figure according to heat provided by the present invention.
Figure 38 moves co-feeding system the 38th kind of principled thermal system figure according to heat provided by the present invention.
Figure 39 moves co-feeding system the 39th kind of principled thermal system figure according to heat provided by the present invention.
Figure 40 moves co-feeding system the 40th kind of principled thermal system figure according to heat provided by the present invention.
Figure 41 moves co-feeding system the 41st kind of principled thermal system figure according to heat provided by the present invention.
Figure 42 moves co-feeding system the 42nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 43 moves co-feeding system the 43rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 44 moves co-feeding system the 44th kind of principled thermal system figure according to heat provided by the present invention.
Figure 45 moves co-feeding system the 45th kind of principled thermal system figure according to heat provided by the present invention.
Figure 46 moves co-feeding system the 46th kind of principled thermal system figure according to heat provided by the present invention.
Figure 47 moves co-feeding system the 47th kind of principled thermal system figure according to heat provided by the present invention.
Figure 48 moves co-feeding system the 48th kind of principled thermal system figure according to heat provided by the present invention.
Figure 49 moves co-feeding system the 49th kind of principled thermal system figure according to heat provided by the present invention.
Figure 50 moves co-feeding system the 50th kind of principled thermal system figure according to heat provided by the present invention.
Figure 51 moves co-feeding system the 51st kind of principled thermal system figure according to heat provided by the present invention.
Figure 52 moves co-feeding system the 52nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 53 moves co-feeding system the 53rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 54 moves co-feeding system the 54th kind of principled thermal system figure according to heat provided by the present invention.
Figure 55 moves co-feeding system the 55th kind of principled thermal system figure according to heat provided by the present invention.
Figure 56 moves co-feeding system the 56th kind of principled thermal system figure according to heat provided by the present invention.
Figure 57 moves co-feeding system the 57th kind of principled thermal system figure according to heat provided by the present invention.
Figure 58 moves co-feeding system the 58th kind of principled thermal system figure according to heat provided by the present invention.
Figure 59 moves co-feeding system the 59th kind of principled thermal system figure according to heat provided by the present invention.
Figure 60 moves co-feeding system the 60th kind of principled thermal system figure according to heat provided by the present invention.
Figure 61 moves co-feeding system the 61st kind of principled thermal system figure according to heat provided by the present invention.
Figure 62 moves co-feeding system the 62nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 63 moves co-feeding system the 63rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 64 moves co-feeding system the 64th kind of principled thermal system figure according to heat provided by the present invention.
Figure 65 moves co-feeding system the 65th kind of principled thermal system figure according to heat provided by the present invention.
Figure 66 moves co-feeding system the 66th kind of principled thermal system figure according to heat provided by the present invention.
Figure 67 moves co-feeding system the 67th kind of principled thermal system figure according to heat provided by the present invention.
Figure 68 moves co-feeding system the 68th kind of principled thermal system figure according to heat provided by the present invention.
Figure 69 moves co-feeding system the 69th kind of principled thermal system figure according to heat provided by the present invention.
Figure 70 moves co-feeding system the 70th kind of principled thermal system figure according to heat provided by the present invention.
Figure 71 moves co-feeding system the 71st kind of principled thermal system figure according to heat provided by the present invention.
Figure 72 moves co-feeding system the 72nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 73 moves co-feeding system the 73rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 74 moves co-feeding system the 74th kind of principled thermal system figure according to heat provided by the present invention.
Figure 75 moves co-feeding system the 75th kind of principled thermal system figure according to heat provided by the present invention.
Figure 76 moves co-feeding system the 76th kind of principled thermal system figure according to heat provided by the present invention.
Figure 77 moves co-feeding system the 77th kind of principled thermal system figure according to heat provided by the present invention.
Figure 78 moves co-feeding system the 78th kind of principled thermal system figure according to heat provided by the present invention.
Figure 79 moves co-feeding system the 79th kind of principled thermal system figure according to heat provided by the present invention.
Figure 80 moves co-feeding system the 80th kind of principled thermal system figure according to heat provided by the present invention.
Figure 81 moves co-feeding system the 81st kind of principled thermal system figure according to heat provided by the present invention.
Figure 82 moves co-feeding system the 82nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 83 moves co-feeding system the 83rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 84 moves co-feeding system the 84th kind of principled thermal system figure according to heat provided by the present invention.
Figure 85 moves co-feeding system the 85th kind of principled thermal system figure according to heat provided by the present invention.
Figure 86 moves co-feeding system the 86th kind of principled thermal system figure according to heat provided by the present invention.
Figure 87 moves co-feeding system the 87th kind of principled thermal system figure according to heat provided by the present invention.
Figure 88 moves co-feeding system the 88th kind of principled thermal system figure according to heat provided by the present invention.
In figure, 1-engine, 2-working machine, 3-generator, 4-condenser, 5-absorber, 6-evaporimeter, 7-second absorber, 8-second evaporimeter, 9-solution pump, 10-cryogen liquid pump, 11-second cryogen liquid pump, 12-solution heat exchanger, 13-second solution heat exchanger, 14-second generator, 15-the 3rd absorber, 16-second solution pump, 17-the 3rd solution heat exchanger, 18-second condenser, 19-the 3rd evaporimeter, 20-the 3rd cryogen liquid pump, 21-solution choke valve, 22-divides steam chest, 23-the 3rd generator, 24-the 4th absorber, 25-the 3rd solution pump, 26-the 4th solution heat exchanger, 27-the 4th evaporimeter, 28-the 4th cryogen liquid pump, A-increases generator newly, B-increases the second generator newly, C-increases absorber newly, D-increases the second absorber newly, E-increases condenser newly, F-increases evaporimeter newly, G-increases choke valve newly, H-increases solution pump newly, I-increases the second solution pump newly, J-increases solution heat exchanger newly, K-increases the second solution heat exchanger newly, L-increases heat exchanger newly, M-increases circulating pump newly, N-increases the 3rd generator newly, 0-increases the 3rd absorber newly, P-increases the 3rd solution pump newly, Q-increases the 3rd solution heat exchanger newly, R-increases the second condenser newly, S-increases second throttle newly, the new solubilization liquid choke valve of T-, U-increases the second solution choke valve newly, the newly-increased point steam chest of V-.
Here also following explanation to be provided:
(1) live steam---refer to for hot merit conversion, pressure and temperature all higher than the engine working media drawn gas.
(2) steam discharge---refer to engine export medium, as the low-pressure steam in steam turbine outlet moist steam.
(3) second steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of steam discharge.
(4) the 3rd steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the second steam.
(4) the 4th steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the 3rd steam.
(5) the 5th steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the 4th steam.
(6) the 6th steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the 5th steam.
(7) condensate liquid---the liquid formed after steam discharge exothermic condensation.
(8) second condensate liquids---the liquid after the second steam exothermic condensation.
(9) the 3rd condensate liquids---the liquid after the 3rd steam exothermic condensation.
(10) the 4th condensate liquids---the liquid after the 4th steam exothermic condensation.
(11) the 5th condensate liquids---the liquid after the 5th steam exothermic condensation.
(12) the 6th condensate liquids---the liquid after the 6th steam exothermic condensation.
(13) relevant with engine, but do not relate to operation principle of the present invention, the parts (as dynamical system backheat heat exchanger components etc.) irrelevant with content of the present invention and flow process (recovery etc. as condensate liquid), not in express ranges of the present invention.
(14) cryogen liquid and condensate liquid---the refrigerant vapour exothermic condensation that generator solution discharges forms cryogen liquid, and the working steam exothermic condensation of engine forms condensate liquid; Refrigerant vapour and working steam claim cryogen liquid when being same material.
(15) engine outlet steam discharge utilization---move co-feeding system for concrete heat, the utilization of exhaust steam heat load is divided into three kinds of situations: 1. exhaust steam heat load is all utilized; 2. exhaust steam heat load part is utilized; 3. exhaust steam heat load is not utilized.For this reason, " engine 1 or in addition exhaust passage and ft connection " such statement is adopted to summarize steam discharge utilization power.
(16) effect of choke valve and solution choke valve---for fluid step-down, can be replaced by gravity pressure reduction or pipe resistance.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, do not repeat in inessential situation; Apparent flow process is not stated.The present invention is described in detail below in conjunction with accompanying drawing and example.
Heat shown in Fig. 1 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have exhaust passage be communicated with evaporimeter 6 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the second condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, live steam enters engine 1, engine 1 provides the second steam to the second evaporimeter 8, second steam heat release is flowed out through the second condensate liquid pipeline after becoming condensate liquid, engine 1 provides steam discharge to evaporimeter 6 and generator 3, steam discharge progressively heat release flows out through condensate line road after becoming condensate liquid, and residue steam discharge is externally discharged; The concentrated solution of generator 3 enters the second absorber 7 through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13, concentrated solution in the second absorber 7, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 7 enters absorber 5 through the second solution heat exchanger 13, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 5 enters generator 3, heat absorption release refrigerant vapour providing to condenser 4 through solution heat exchanger 12; The refrigerant vapour heat release of condenser 4 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 4 is divided into two-way---and the first via enters evaporimeter 6 through cryogen liquid pump 10 pressurization, absorbs heat into refrigerant vapour and provide to absorber 5, second tunnel second cryogen liquid pump 11 pressurization enters the second evaporimeter 8, absorbs heat into refrigerant vapour and provide to the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 2 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger and the second solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has exhaust passage to be communicated with absorber 5, and engine 1 also has the second steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with condenser 4, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 1, difference is: engine 1 provides the second steam directly to the second absorber 7, and engine 1 provides steam discharge directly to absorber 5, and the cryogen liquid of condenser 4 is externally discharged through cryogen liquid pump 10.
Heat shown in Fig. 3 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 1, engine 1 is had exhaust passage be communicated with evaporimeter 6 and generator 3 successively after generator 3 have again condensate liquid pipeline and ft connection be adjusted to engine 1 have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, engine 1 is had the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the second condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the second steam channel to be communicated with evaporimeter 6 have the second condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 3rd steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 1, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is flowed out through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6, and the heat release in evaporimeter 6 of the second steam is flowed out through the second condensate liquid pipeline after becoming condensate liquid.
Heat shown in Fig. 4 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 2, cancel the exhaust passage that engine 1 is communicated with absorber 5, being had by engine 1 second steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the second steam channel to be communicated with absorber 5, engine 1 is set up the 3rd steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 5 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 1, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is flowed out through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6 and generator 3, second steam progressively heat release flows out through the second condensate liquid pipeline after becoming condensate liquid, and the whole steam discharges after completing work done are externally discharged.
Heat shown in Fig. 6 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger and the second solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with condenser 4, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 2, difference is: engine 1 provides the 3rd steam to the second absorber 7, and engine 1 provides the second steam to generator 3 and absorber 5, and the whole steam discharges after completing work done are externally discharged.
Heat shown in Fig. 7 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 5, engine 1 is had the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 5, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 4th steam is flowed out through the 4th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 3rd steam to evaporimeter 6, the heat release in evaporimeter 6 of second steam is flowed out through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to generator 3, and the heat release in generator 3 of the second steam is flowed out through the second condensate liquid pipeline after becoming condensate liquid.
Heat shown in Fig. 8 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 6, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 9 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with evaporimeter 6, second generator 14 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the second condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, engine 1 provides the second steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 1 provides steam discharge to evaporimeter 6, second generator 14 and generator 3, and steam discharge heat release is discharged through condensate liquid pipeline after becoming condensate liquid; The concentrated solution of generator 3 enters the second absorber 7 through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13, concentrated solution in the second absorber 7, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 7 enters absorber 5 through the second solution heat exchanger 13, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 5 enters generator 3 through solution heat exchanger 12, heat absorption release refrigerant vapour the 3rd absorber 15 provide; The weak solution of the 3rd absorber 15 enters the second generator 14, heat absorption release refrigerant vapour providing to condenser 4 through the second solution pump 16 and the 3rd solution heat exchanger 17, the concentrated solution of the second generator 14 enters the 3rd absorber 15 through the 3rd solution heat exchanger 17, absorb refrigerant vapour and heat release in cooling medium; The refrigerant vapour heat release of condenser 4 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 4 is divided into two-way---and the first via enters evaporimeter 6 through cryogen liquid pump 10 pressurization, absorbs heat into refrigerant vapour and provide to absorber 5, second tunnel second cryogen liquid pump 11 pressurization enters the second evaporimeter 8, absorbs heat into refrigerant vapour and provide to the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 10 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with the second generator 14 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has exhaust passage to be communicated with absorber 5, and engine 1 also has the second steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 9, difference is: engine 1 provides near steam directly to the second absorber 7, and engine 1 provides steam discharge directly to absorber 5.
Heat shown in Figure 11 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 9, exhaust passage is had to be communicated with evaporimeter 6 successively in engine 1, after second generator 14 and generator 3 generator 3 have again condensate liquid pipeline and ft connection be adjusted to engine 1 have exhaust passage be communicated with successively the second generator 14 and generator 3 afterwards generator 3 have condensate liquid pipeline and ft connection again, engine 1 is had the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the second condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the second steam channel to be communicated with evaporimeter 6 have the second condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 3rd steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 9, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is flowed out through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6, and the heat release in evaporimeter 6 of the second steam is flowed out through the second condensate liquid pipeline after becoming condensate liquid.
Heat shown in Figure 12 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 10, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 second steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the second steam channel to be communicated with absorber 5, engine 1 is set up the 3rd steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 13 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with the second generator 14 after the second generator 14 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 11, difference is: engine 1 provides the second steam to evaporimeter 6 and generator 3, second vapor stream becomes through the second condensate liquid pipeline discharge after condensate liquid with generator 3 heat release through evaporimeter 6, and engine 1 only provides steam discharge to the second generator 14.
Heat shown in Figure 14 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with the second generator 14 after the second generator 14 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 12, difference is: engine 1 provides the second steam to generator 3, and engine 1 only provides steam discharge to the second generator 14.
Heat shown in Figure 15 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 13, engine 1 is had the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 13, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 3rd steam to evaporimeter 6, and the heat release in evaporimeter 6 of the 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid.
Heat shown in Figure 16 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 14, cancelling engine 1 has the second steam channel to be communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 17 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with evaporimeter 6, second generator 14 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Fig. 9, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6, second generator 14 and generator 3, second vapor stream through evaporimeter 6, second generator 14 and generator 3 progressively heat release discharge through the second condensate liquid pipeline after becoming condensate liquid, whole steam discharges of engine 1 are externally discharged.
Heat shown in Figure 18 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with the second generator 14 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 10, difference is: engine 1 provides the 3rd steam to the second absorber 7, engine 1 provides the second steam to absorber 5, engine 1 provides the second steam to the second generator 14 and generator 3, and whole steam discharges of engine 1 are externally discharged.
Heat shown in Figure 19 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 17, the second steam channel is had to be communicated with evaporimeter 6 successively in engine 1, after second generator 14 and generator 3 generator 3 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with successively the second generator 14 and generator 3 afterwards generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 17, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 3rd steam to evaporimeter 6, and the heat release in evaporimeter 6 of the 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid.
Heat shown in Figure 20 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 18, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 21 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with the second generator 14 after the second generator 14 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have the 3rd condensate liquid pipeline and ft connection again, engine 1 also have the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 4th condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 19, difference is: engine 1 provides the 3rd steam to evaporimeter 6 and generator 3,3rd vapor stream becomes through the 3rd condensate liquid pipeline discharge after condensate liquid with generator 3, progressively heat release through evaporimeter 6, and engine 1 only provides the second steam to the second generator 14.
Heat shown in Figure 22 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with the second generator 14 after the second generator 14 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with generator 3 after generator 3 have the 3rd condensate liquid pipeline and ft connection again, engine 1 also has the 3rd steam channel to be communicated with absorber 5, and engine 1 also has the 4th steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 with the 3rd solution heat exchanger 17 through the second solution pump 16, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 20, difference is: engine 1 provides the 3rd steam to generator 3, and engine 1 only provides the second steam to the second generator 14.
Heat shown in Figure 23 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 21, engine 1 is had the 3rd steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine 1 have the 3rd steam channel be communicated with generator 3 after generator 3 have the 3rd condensate liquid pipeline and ft connection again, engine 1 is had the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 4th steam channel to be communicated with evaporimeter 6 have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 5th steaming passage is communicated with the second evaporimeter 8 set up by engine 1 the 5th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 21, difference is: engine 1 provides the 5th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 5th steam is discharged through the 5th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 4th steam to evaporimeter 6, the heat release in evaporimeter 6 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides the 3rd steam to generator 3.
Heat shown in Figure 24 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 22, cancel the 3rd steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 4th steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 4th steam channel to be communicated with absorber 5, engine 1 is set up the 5th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 25 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage to be communicated with generator 3 after evaporimeter 6, the 3rd evaporimeter 19 and generator 3 successively and has condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the second condensate liquid pipeline and ft connection again, steam chest 22 is divided to have concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline through solution heat exchanger 12, solution choke valve 21 is communicated with a point steam chest 22 with the 3rd absorber 15, steam chest 22 is divided to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, second condenser 18 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, live steam enters engine 1 step-down work done, engine 1 provides the second steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 1 provides steam discharge to evaporimeter 6, the 3rd evaporimeter 19 and generator 3, steam discharge flow through evaporimeter 6, the 3rd evaporimeter 19 and generator 3 progressively heat release discharge through condensate line road after becoming condensate liquid, divide the concentrated solution of steam chest 22 through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 enter the second absorber 7, concentrated solution in the second absorber 7, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 7 enters absorber 5 through the second solution heat exchanger 13, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 5 flows through the 3rd absorber 15 after solution heat exchanger 12 heat exchange cooling and solution choke valve 21 reducing pressure by regulating flow, heat absorbing part vaporization enters point steam chest 22, steam chest 22 is divided to discharge and provide refrigerant vapour to condenser 4, the refrigerant vapour heat release of condenser 4 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 4 is divided into two-way---and the first via enters evaporimeter 6 through cryogen liquid pump 10 pressurization, absorbs heat into refrigerant vapour and provide to absorber 5, and the second tunnel second cryogen liquid pump 11 pressurization enters the second evaporimeter 8, absorbs heat into refrigerant vapour and provide to the second absorber 7, the concentrated solution of generator 3 enters the 3rd absorber 15 through the second solution pump 16 and the 3rd solution heat exchanger 17, absorb refrigerant vapour and heat release in solution, the weak solution of the 3rd absorber 15 enters generator 3 through the 3rd solution heat exchanger 17, absorbing heat discharges refrigerant vapour and provide to the second condenser 18, the refrigerant vapour heat release of the second condenser 18 becomes cryogen liquid in cooling medium, the cryogen liquid of the second condenser 18 enters the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20 pressurization, absorbs heat into refrigerant vapour and provide to the 3rd absorber 15, forms the dynamic co-feeding system of heat.
Heat shown in Figure 26 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has exhaust passage to be communicated with the 3rd absorber 15, engine 1 also has exhaust passage to be communicated with absorber 5, and engine 1 also has the second steam channel to be communicated with the second absorber 7; Steam chest 22 is divided to have concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with a point steam chest 22 through solution heat exchanger 12, solution choke valve 21 and the 3rd absorber 15, divide steam chest 22 to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, and the second condenser 18 also has cryogen liquid pipeline through the second cryogen liquid pump 11 and ft connection; Condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 25, difference is: engine 1 provides the second steam directly to the second absorber 7, engine 1 provides steam discharge directly to absorber 5 and the 3rd absorber 15, the cryogen liquid of condenser 4 is externally discharged through cryogen liquid pump 10, and the cryogen liquid of the second condenser 18 is externally discharged through the second cryogen liquid pump 11.
Heat shown in Figure 27 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 25, exhaust passage is had to be communicated with evaporimeter 6 successively in engine 1, after 3rd evaporimeter 19 and generator 3 generator 3 have again condensate liquid pipeline and ft connection be adjusted to engine 1 have exhaust passage be communicated with successively the 3rd evaporimeter 19 and generator 3 afterwards generator 3 have condensate liquid pipeline and ft connection again, engine 1 is had the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the second condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the second steam channel to be communicated with evaporimeter 6 have the second condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 3rd steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 25, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6, the heat release in evaporimeter 6 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides steam discharge to the 3rd evaporimeter 19 and generator 3.
Heat shown in Figure 28 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 26, cancel the exhaust passage that engine 1 is communicated with absorber 5, being had by engine 1 second steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the second steam channel to be communicated with absorber 5, engine 1 is set up the 3rd steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 29 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, steam chest 22 is divided to have concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline through solution heat exchanger 12, solution choke valve 21 is communicated with a point steam chest 22 with the 3rd absorber 15, steam chest 22 is divided to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, second condenser 18 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 27, difference is: engine 1 provides the second steam to evaporimeter 6 and the 3rd evaporimeter 19, second vapor stream becomes through the second condensate liquid pipeline discharge after condensate liquid with the 3rd evaporimeter 19, heat release through evaporimeter 6, and engine 1 only provides steam discharge to generator 3.
Heat shown in Figure 30 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with the 3rd absorber 15, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7; Steam chest 22 is divided to have concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with a point steam chest 22 through solution heat exchanger 12, solution choke valve 21 and the 3rd absorber 15, divide steam chest 22 to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, and the second condenser 18 also has cryogen liquid pipeline through the second cryogen liquid pump 11 and ft connection; Condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 28, difference is: engine 1 provides the second steam to the 3rd absorber 15, and engine 1 only provides steam discharge to generator 3.
Heat shown in Figure 31 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 29, engine 1 is had the second steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with the 3rd evaporimeter 19 after the 3rd evaporimeter 19 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with his heat shown in 29, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 3rd steam to evaporimeter 6, the heat release in evaporimeter 6 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides the second steam to the 3rd evaporimeter 19.
Heat shown in Figure 32 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 30, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 33 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also has the second steam channel to be communicated with generator 3 after evaporimeter 6, the 3rd evaporimeter 19 and generator 3 successively and has the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, steam chest 22 is divided to have concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline through solution heat exchanger 12, solution choke valve 21 is communicated with a point steam chest 22 with the 3rd absorber 15, steam chest 22 is divided to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, second condenser 18 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 25, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6, the 3rd evaporimeter 19 and generator 1, second vapor stream through evaporimeter 6, the 3rd evaporimeter 19 and generator 1 progressively heat release become after condensate liquid and discharge through the second condensate liquid pipeline, the steam discharge of engine 1 is all externally discharged.
Heat shown in Figure 34 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with the 3rd absorber 15, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7; Steam chest 22 is divided to have concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with a point steam chest 22 through solution heat exchanger 12, solution choke valve 21 and the 3rd absorber 15, divide steam chest 22 to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, and the second condenser 18 also has cryogen liquid pipeline through the second cryogen liquid pump 11 and ft connection; Condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 26, difference is: engine 1 provides the 3rd steam to the second absorber 7, engine 1 provides the second steam respectively to absorber 5 and the 3rd absorber 15, engine 1 provides the second steam to generator 3, the cryogen liquid of condenser 4 is externally discharged through cryogen liquid pump 10, and the cryogen liquid of the second condenser 18 is externally discharged through the second cryogen liquid pump 11.
Heat shown in Figure 35 is moved co-feeding system and is achieved in that
(1) in structure, Figure 33 heat move in co-feeding system, the second steam channel is had to be communicated with evaporimeter 6 successively in engine 1, after 3rd evaporimeter 19 and generator 3 generator 3 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with successively the 3rd evaporimeter 19 and generator 3 afterwards generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 33, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 3rd steam to evaporimeter 6, the heat release in evaporimeter 6 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides the second steam to the 3rd evaporimeter 19 and generator 3.
Heat shown in Figure 36 is moved co-feeding system and is achieved in that
Figure 34 heat move in co-feeding system, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 37 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have the 3rd condensate liquid pipeline and ft connection again, engine 1 also have the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 4th condensate liquid pipeline and ft connection again, steam chest 22 is divided to have concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline through solution heat exchanger 12, solution choke valve 21 is communicated with a point steam chest 22 with the 3rd absorber 15, steam chest 22 is divided to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, second condenser 18 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 35, difference is: engine 1 provides the 3rd steam to evaporimeter 6 and the 3rd evaporimeter 19,3rd vapor stream becomes through the 3rd condensate liquid pipeline discharge after condensate liquid with the 3rd evaporimeter 19, progressively heat release through evaporimeter 6, and engine 1 only provides the second steam to generator 3.
Heat shown in Figure 38 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the 3rd steam channel to be communicated with the 3rd absorber 15, engine 1 also has the 3rd steam channel to be communicated with absorber 5, and engine 1 also has the 4th steam channel to be communicated with the second absorber 7; Steam chest 22 is divided to have concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with a point steam chest 22 through solution heat exchanger 12, solution choke valve 21 and the 3rd absorber 15, divide steam chest 22 to also have refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Generator 3 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the 3rd solution heat exchanger 17, generator 3 also has refrigerant steam channel to be communicated with the second condenser 18, and the second condenser 18 also has cryogen liquid pipeline through the second cryogen liquid pump 11 and ft connection; Condenser 4 and the second condenser 18 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 36, difference is: engine 1 provides the 3rd steam to the 3rd absorber 15, and engine 1 only provides the second steam to generator 3.
Heat shown in Figure 39 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 37, engine 1 is had the 3rd steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine 1 have the 3rd steam channel be communicated with the 3rd evaporimeter 19 after the 3rd evaporimeter 19 have the 3rd condensate liquid pipeline and ft connection again, engine 1 is had the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 4th steam channel to be communicated with evaporimeter 6 have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 5th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 5th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 37, difference is: engine 1 provides the 5th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 5th steam is discharged through the 5th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 4th steam to evaporimeter 6, the heat release in evaporimeter 6 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides the 3rd steam to the 3rd evaporimeter 19.
Heat shown in Figure 40 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 38, cancel the 3rd steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 4th steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 4th steam channel to be communicated with absorber 5, engine 1 is set up the 5th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 41 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage to be communicated with generator 3 after evaporimeter 6, the 3rd evaporimeter 19 and generator 3 successively and has condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the second condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 11 with cryogen liquid pump 10 respectively again, cryogen liquid pump 10 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, second cryogen liquid pump 11 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, live steam enters engine 1 step-down work done, engine 1 provides the second steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 1 provides steam discharge to evaporimeter 6, the 3rd evaporimeter 19 and generator 3, steam discharge flow through evaporimeter 6, the 3rd evaporimeter 19 and generator 3 progressively heat release discharge through condensate line road after becoming condensate liquid, the concentrated solution of generator 3 is through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 enter the second absorber 7, concentrated solution in the second absorber 7, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 7 enters absorber 5 through the second solution heat exchanger 13, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 5 enters generator 3 through solution heat exchanger 12, heat absorption release refrigerant vapour also provides to the second generator 14, refrigerant vapour flows through the second generator 14, heating enters the solution release in it and provides refrigerant vapour to condenser 4, the refrigerant vapour heat release flowing through the second generator 14 is divided into two-way after becoming cryogen liquid---and the first via enters evaporimeter 6 through cryogen liquid pump 10 pressurization, absorb heat into refrigerant vapour and provide to absorber 5, second tunnel second cryogen liquid pump 11 pressurization enters the second evaporimeter 8, absorb heat into refrigerant vapour and provide to the second absorber 7, the concentrated solution of the second generator 14 enters the 3rd absorber 15 through the second solution pump 16 and the 3rd solution heat exchanger 17, absorbs refrigerant vapour and heat release heated medium, and the weak solution of the 3rd absorber 15 enters the second generator 14 through the 3rd solution heat exchanger 17, the refrigerant vapour heat release of condenser 4 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 4 enters the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20 pressurization, absorbs heat into refrigerant vapour and provide to the 3rd absorber 15, forms the dynamic co-feeding system of heat.
Heat shown in Figure 42 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with evaporimeter 6 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has exhaust passage to be communicated with absorber 5, and engine 1 also has the second steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline again through the second cryogen liquid pump 11 and ft connection; Second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, and evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 15; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 41, difference is: engine 1 provides the second steam directly to the second absorber 7, and engine 1 provides steam discharge directly to absorber 5; Steam discharge flows through evaporimeter 6 and generator 3, externally discharge through the second cryogen liquid pump 11 after the refrigerant vapour heat release flowing through the second generator 14 becomes cryogen liquid, the cryogen liquid of condenser 4 enters evaporimeter 6 through cryogen liquid pump 10 pressurization, absorbs heat into refrigerant vapour and provide to the 3rd absorber 15.
Heat shown in Figure 43 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 41, exhaust passage is had to be communicated with evaporimeter 6 successively in engine 1, after 3rd evaporimeter 19 and generator 3 generator 3 have again condensate liquid pipeline and ft connection be adjusted to engine 1 have exhaust passage be communicated with successively the 3rd evaporimeter 19 and generator 3 afterwards generator 3 have condensate liquid pipeline and ft connection again, engine 1 is had the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the second condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the second steam channel to be communicated with evaporimeter 6 have the second condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 3rd steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 41, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6, the heat release in evaporimeter 6 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides steam discharge to the 3rd evaporimeter 19 and generator 3.
Heat shown in Figure 44 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 42, cancel the exhaust passage that engine 1 is communicated with absorber 5, being had by engine 1 second steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the second steam channel to be communicated with absorber 5, engine 1 is set up the 3rd steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 45 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 11 with cryogen liquid pump 10 respectively again, cryogen liquid pump 10 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, second cryogen liquid pump 11 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 43, difference is: engine 1 provides the second steam to evaporimeter 6 and the 3rd evaporimeter 19, second vapor stream becomes through the second condensate liquid pipeline discharge after condensate liquid with the 3rd evaporimeter 19, progressively heat release through evaporimeter 6, and engine 1 only provides steam discharge to generator 3.
Heat shown in Figure 46 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 1 also has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline again through the second cryogen liquid pump 11 and ft connection; Second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, and evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 15; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 44, difference is: engine 1 provides the second steam to evaporimeter 6, and the heat release in evaporimeter 6 of the second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides steam discharge to generator 3.
Heat shown in Figure 47 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 45, engine 1 is had the second steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with the 3rd evaporimeter 19 after the 3rd evaporimeter 19 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 45, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 3rd steam to evaporimeter 6, the heat release in evaporimeter 6 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides the second steam to the 3rd evaporimeter 19.
Heat shown in Figure 48 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 46, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 49 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also has the second steam channel to be communicated with generator 3 after evaporimeter 6, the 3rd evaporimeter 19 and generator 3 successively and has the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 11 with cryogen liquid pump 10 respectively again, cryogen liquid pump 10 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, second cryogen liquid pump 11 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 41, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 1 provides the second steam to evaporimeter 6, the 3rd evaporimeter 19 and generator 3, second vapor stream through evaporimeter 6, the 3rd evaporimeter 19 and generator 3 progressively heat release become after condensate liquid and discharge through the second condensate liquid pipeline, engine 1 discharges steam discharge.
Heat shown in Figure 50 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline again through the second cryogen liquid pump 11 and ft connection; Second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, and evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 15; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 42, difference is: engine 1 provides the 3rd steam to the second absorber 7, engine 1 provides the second steam to absorber 5, engine 1 provides the second steam to evaporimeter 6 and generator 3, and the steam discharge of engine 1 is externally discharged.
Heat shown in Figure 51 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 49, the second steam channel is had to be communicated with evaporimeter 6 successively in engine 1, after 3rd evaporimeter 19 and generator 3 generator 3 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with successively the 3rd evaporimeter 19 and generator 3 afterwards generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 49, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 3rd steam to evaporimeter 6, the heat release in evaporimeter 6 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides the second steam to the 3rd evaporimeter 19 and generator 3.
Heat shown in Figure 52 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 50, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 53 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have the 3rd condensate liquid pipeline and ft connection again, engine 1 also have the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 4th condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 11 with cryogen liquid pump 10 respectively again, cryogen liquid pump 10 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, second cryogen liquid pump 11 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, and the 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 51, difference is: engine 1 provides the 3rd steam to evaporimeter 6 and the 3rd evaporimeter 19,3rd vapor stream becomes through the 3rd condensate liquid pipeline discharge after condensate liquid with the 3rd evaporimeter 19, progressively heat release through evaporimeter 6, and engine 1 only provides the second steam to generator 3.
Heat shown in Figure 54 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, the finisher 6 that engine 1 also has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, engine 1 also has the 3rd steam channel to be communicated with absorber 5, and engine 1 also has the 4th steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline again through the second cryogen liquid pump 11 and ft connection; Second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, and evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 15; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 52, difference is: engine 1 provides the 3rd steam to evaporimeter 6, and engine 1 only provides the second steam to generator 3.
Heat shown in Figure 55 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 53, engine 1 is had the 3rd steam channel be communicated with evaporimeter 6 and the 3rd evaporimeter 19 successively after the 3rd evaporimeter 19 have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine 1 have the 3rd steam channel be communicated with the 3rd evaporimeter 19 after the 3rd evaporimeter 19 have the 3rd condensate liquid pipeline and ft connection again, engine 1 is had the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 4th steam channel to be communicated with evaporimeter 6 have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 5th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 5th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 53, difference is: engine 1 provides the 5th steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of 5th steam is discharged through the 5th condensate liquid pipeline after becoming condensate liquid, engine 1 provides the 4th steam to evaporimeter 6, the heat release in evaporimeter 6 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, and engine 1 only provides the 3rd steam to the 3rd evaporimeter 19.
Heat shown in Figure 56 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 54, cancel the 3rd steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 4th steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 4th steam channel to be communicated with absorber 5, engine 1 is set up the 5th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 57 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger and the 3rd cryogen liquid pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with evaporimeter 6 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the second condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 11 with cryogen liquid pump 10 respectively again, cryogen liquid pump 10 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, second cryogen liquid pump 11 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through the 3rd cryogen liquid pump 20, and evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2), in flow process, live steam enters engine 1 step-down work done, and engine 1 provides the second steam to the second evaporimeter 8, and engine 1 provides steam discharge to evaporimeter 6 and generator 3, the concentrated solution of generator 3 is through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 enter the second absorber 7, concentrated solution in the second absorber 7, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 7 enters absorber 5 through the second solution heat exchanger 13, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 5 enters generator 3 through solution heat exchanger 12, heat absorption release refrigerant vapour also provides to the second generator 14, refrigerant vapour flows through the second generator 14, heating enters the solution release in it and provides refrigerant vapour to condenser 4, the refrigerant vapour heat release flowing through the second generator 14 is divided into two-way after becoming cryogen liquid---and the first via enters evaporimeter 6 through cryogen liquid pump 10 pressurization, second tunnel second cryogen liquid pump 11 pressurization enters the second evaporimeter 8, absorb heat into refrigerant vapour and provide to the second absorber 7, the concentrated solution of the second generator 14 enters the 3rd absorber 15 through the second solution pump 16 and the 3rd solution heat exchanger 17, absorbs refrigerant vapour and heat release heated medium, and the weak solution of the 3rd absorber 15 enters the second generator 14 through the 3rd solution heat exchanger 17, the refrigerant vapour heat release of condenser 4 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 4 enters evaporimeter 6 through the 3rd cryogen liquid pump 20 pressurization, the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour and provides respectively to absorber 5 and the 3rd absorber 15, forms the dynamic co-feeding system of heat.
Heat shown in Figure 58 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with generator 3 after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has exhaust passage to be communicated with the 3rd absorber 15, engine 1 also has exhaust passage to be communicated with absorber 5, and engine 1 also has the second steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline again through the second cryogen liquid pump 11 and ft connection; Second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 57, difference is: engine 1 provides the second steam directly to the second absorber 7, engine 1 provides steam discharge directly to absorber 5 and the 3rd absorber 15, the cryogen liquid of condenser 4 is externally discharged through cryogen liquid pump 10, externally discharges after the refrigerant vapour heat release flowing through the second generator 14 becomes cryogen liquid through the second cryogen liquid pump 11.
Heat shown in Figure 59 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger and the 3rd cryogen liquid pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 11 with cryogen liquid pump 10 respectively again, cryogen liquid pump 10 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, second cryogen liquid pump 11 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through the 3rd cryogen liquid pump 20, and evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 15, condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 57, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, and engine 1 provides the second steam to evaporimeter 6 and generator 3, and the steam discharge of engine 1 is externally discharged.
Heat shown in Figure 60 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with the 3rd absorber 15 with absorber 5 respectively, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7; Generator 3 also has concentrated solution pipeline to be communicated with the second absorber 7 with the second solution heat exchanger 13 through solution pump 9, solution heat exchanger 12, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline again through the second cryogen liquid pump 11 and ft connection; Second generator 14 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17 through the second solution pump 16,3rd absorber 15 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection; Condenser 4 also has cooling medium pipeline and ft connection, and absorber 5, second absorber 7 and the 3rd absorber 15 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 58, difference is: engine 1 provides the 3rd steam to the second absorber 7, engine 1 provides the second steam to absorber 5 and the 3rd absorber 15, engine 1 provides the second steam to generator 3, and the steam discharge of engine 1 is externally discharged.
Heat shown in Figure 61 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have exhaust passage be communicated with evaporimeter 6, second generator 14 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the second condensate liquid pipeline and ft connection again, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through solution choke valve 21, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, engine 1 provides the second steam to the second evaporimeter 8, the heat release in the second evaporimeter 8 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 1 provides steam discharge to evaporimeter 6, second generator 14 and generator 3, steam discharge flows through evaporimeter 6, second generator 14 successively and becomes with generator 3 heat release through the discharge of condensate line road after condensate liquid, and engine 1 also has exhaust externally to discharge, the concentrated solution of the second generator 14 is through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 enter the second absorber 7, concentrated solution in the second absorber 7, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 7 enters absorber 5 through the second solution heat exchanger 13, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 5 enters the 3rd absorber 15 through solution heat exchanger 12, absorb refrigerant vapour heat release in cooling medium, the weak solution of the 3rd absorber 15 enters generator 3 through the second solution pump 16 pressurization, heat absorption release refrigerant vapour also provides to condenser 4, the concentrated solution of generator 3 enters the second generator 14 through solution choke valve 21 reducing pressure by regulating flow, heat absorption release refrigerant vapour also provides to the 3rd absorber 15, the refrigerant vapour heat release of condenser 4 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 4 is divided into two-way---and the first via enters evaporimeter 6 through cryogen liquid pump 10 pressurization, absorbs heat into refrigerant vapour and provide to absorber 5, second tunnel second cryogen liquid pump 11 pressurization enters the second evaporimeter 8, absorbs heat into refrigerant vapour and provide to the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 62 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have exhaust passage be communicated with the second generator 14 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has exhaust passage to be communicated with absorber 5, and engine 1 also has the second steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through solution choke valve 21, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 61, difference is: engine 1 provides the second steam directly to the second absorber 7, and engine 1 provides steam discharge directly to absorber 5, and the cryogen liquid of condenser 4 is externally discharged through cryogen liquid pump 10.
Heat shown in Figure 63 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 61, exhaust passage is had to be communicated with evaporimeter 6 successively in engine 1, after second generator 14 and generator 3 generator 3 have again condensate liquid pipeline and ft connection be adjusted to engine 1 have exhaust passage be communicated with successively the second generator 14 and generator 3 afterwards generator 3 have condensate liquid pipeline and ft connection again, engine 1 is had the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the second condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the second steam channel to be communicated with evaporimeter 6 have the second condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 3rd steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving alliance with the heat shown in Figure 61, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, and engine 1 provides the second steam to evaporimeter 6, and engine 1 only provides steam discharge to the second generator 14 and generator 3.
Heat shown in Figure 64 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 62, cancel the exhaust passage that engine 1 is communicated with absorber 5, being had by engine 1 second steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the second steam channel to be communicated with absorber 5, engine 1 is set up the 3rd steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 65 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have exhaust passage be communicated with the second generator 14 after the second generator 14 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 with the 3rd solution heat exchanger 17 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 63, difference is: engine 1 provides the second steam to evaporimeter 6 and generator 3, and engine 1 provides steam discharge to the second generator 14.
Heat shown in Figure 66 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have exhaust passage be communicated with the second generator 14 after the second generator 14 have condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 with the 3rd solution heat exchanger 17 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 64, difference is: engine 1 provides the second steam to generator 3, and engine 1 only provides steam discharge to the second generator 14.
Heat shown in Figure 67 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 65, engine 1 is had the second steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with generator 3 after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving co-feeding system with the heat shown in Figure 65, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, and engine 1 provides the 3rd steam to evaporimeter 6, and engine 1 only provides the second steam to generator 3.
Heat shown in Figure 68 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 66, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 69 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with evaporimeter 6, second generator 14 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 3rd condensate liquid pipeline and ft connection again, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through solution choke valve 21, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 61, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, and engine 1 provides the second steam to evaporimeter 6, second generator 14 and generator 3, and the steam discharge of engine 1 is all externally discharged.
Heat shown in Figure 70 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with the second generator 14 and generator 3 successively after generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 also has the second steam channel to be communicated with absorber 5, and engine 1 also has the 3rd steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through solution choke valve 21, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 69, difference is: engine 1 provides the 3rd steam directly to the second absorber 7, and engine 1 provides the second steam directly to absorber 5, and the cryogen liquid of condenser 4 is externally discharged through cryogen liquid pump 10.
Heat shown in Figure 71 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 69, the second steam channel is had to be communicated with evaporimeter 6 successively in engine 1, after second generator 14 and generator 3 generator 3 have again the second condensate liquid pipeline and ft connection be adjusted to engine 1 have the second steam channel be communicated with successively the second generator 14 and generator 3 afterwards generator 3 have the second condensate liquid pipeline and ft connection again, engine 1 is had the 3rd steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 3rd steam channel to be communicated with evaporimeter 6 have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 4th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 4th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving alliance with the heat shown in Figure 69, difference is: engine 1 provides the 4th steam to the second evaporimeter 8, and engine 1 provides the 3rd steam to evaporimeter 6, and engine 1 only provides the second steam to the second generator 14 and generator 3.
Heat shown in Figure 72 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 70, cancel the second steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 3rd steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 3rd steam channel to be communicated with absorber 5, engine 1 is set up the 4th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 73 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with the second generator 14 after the second generator 14 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have the 3rd condensate liquid pipeline and ft connection again, engine 1 also have the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the 4th condensate liquid pipeline and ft connection again, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 with the 3rd solution heat exchanger 17 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 71, difference is: engine 1 provides the 3rd steam to evaporimeter 6 and generator 3, and engine 1 only provides the second steam to the second generator 14.
Heat shown in Figure 74 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage and ft connection, engine 1 also have the second steam channel be communicated with the second generator 14 after the second generator 14 have the second condensate liquid pipeline and ft connection again, engine 1 also have the 3rd steam channel be communicated with generator 3 after generator 3 have the 3rd condensate liquid pipeline and ft connection again, engine 1 also has the 3rd steam channel to be communicated with absorber 5, and engine 1 also has the 4th steam channel to be communicated with the second absorber 7, second generator 14 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with the 3rd absorber 15 through solution heat exchanger 12, 3rd absorber 15 also has weak solution pipeline to be communicated with generator 3 with the 3rd solution heat exchanger 17 through the second solution pump 16, generator 3 also has concentrated solution pipeline to be communicated with the second generator 14 through the 3rd solution heat exchanger 17, second generator 14 also has refrigerant steam channel to be communicated with the 3rd absorber 15, generator 3 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4 and the 3rd absorber 15 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 72, difference is: engine 1 provides the 3rd steam to generator 3, and engine 1 only provides the second steam to the second generator 14.
Heat shown in Figure 75 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 73, engine 1 is had the 3rd steam channel be communicated with evaporimeter 6 and generator 3 successively after generator 3 have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine 1 have the 3rd steam channel be communicated with generator 3 after generator 3 have the 3rd condensate liquid pipeline and ft connection to adjust again, engine 1 is had the 4th steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the 4th steam channel to be communicated with evaporimeter 6 have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 5th steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 5th condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving alliance with the heat shown in Figure 73, difference is: engine 1 provides the 5th steam to the second evaporimeter 68, and engine 1 provides the 4th steam to evaporimeter 6, and engine 1 provides the 3rd steam to generator 3.
Heat shown in Figure 76 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 74, cancel the 3rd steam channel that engine 1 is communicated with absorber 5, being had by engine 1 the 4th steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the 4th steam channel to be communicated with absorber 5, engine 1 is set up the 5th steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 77 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, solution choke valve, the 3rd generator, the 4th absorber and the 3rd solution pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also has exhaust passage to be communicated with generator 3 after evaporimeter 6, the 3rd generator 23, second generator 14 and generator 3 successively and has condensate liquid pipeline and ft connection again, engine 1 also have the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 have the second condensate liquid pipeline and ft connection again, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the 4th absorber 24 with the 3rd solution heat exchanger 17 through the second solution pump 16, 4th absorber 24 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution pump 25, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd generator 23 through solution choke valve 21, 3rd generator 23 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, 3rd generator 23 also has refrigerant steam channel to be communicated with the 4th absorber 24, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 10, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 5, condenser 4 also has cryogen liquid pipeline to be communicated with the second evaporimeter 8 through the second cryogen liquid pump 11, second evaporimeter 8 also has refrigerant steam channel to be communicated with the second absorber 7, condenser 4, the 3rd absorber 15 and the 4th absorber 24 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, live steam enters engine 1, engine 1 provides the second steam to the second evaporimeter 8, second steam heat release is flowed out through the second condensate liquid pipeline after becoming condensate liquid, engine 1 provides steam discharge to evaporimeter 6, the 3rd generator 23, second generator 14 and generator 3, and steam discharge progressively heat release flows out through condensate line road after becoming condensate liquid, the concentrated solution of generator 3 enters the second absorber 7 through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13, concentrated solution in the second absorber 7, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 7 enters absorber 5 through the second solution heat exchanger 13, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 5 enters generator 3, heat absorption release refrigerant vapour providing to the 3rd absorber 15 through solution heat exchanger 12, the weak solution of the 3rd absorber 15 enters the 4th absorber 24 through the second solution pump 16 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in cooling medium, the weak solution of the 4th absorber 24 enters the second generator 14 through the 3rd solution pump 25, heat absorption release refrigerant vapour also provides to condenser 4, the concentrated solution of the second generator 14 enters the 3rd generator 23 through solution choke valve 21, heat absorption release refrigerant vapour also provides to the 4th absorber 24, the concentrated solution of the 3rd generator 23 enters the 3rd absorber 15 through the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in cooling medium, the refrigerant vapour heat release of condenser 4 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 4 is divided into two-way---and the first via enters evaporimeter 6 through cryogen liquid pump 10 pressurization, absorbs heat into refrigerant vapour and provide to absorber 5, second tunnel second cryogen liquid pump 11 pressurization enters the second evaporimeter 8, absorbs heat into refrigerant vapour and provide to the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 78 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, solution choke valve, the 3rd generator, the 4th absorber and the 3rd solution pump, engine 1 connects working machine 2, engine 1 has live steam passage and ft connection, engine 1 also have exhaust passage be communicated with the 3rd generator 23, second generator 14 and generator 3 successively after generator 3 have condensate liquid pipeline and ft connection again, engine 1 also has exhaust passage to be communicated with absorber 5, and engine 1 also has the second steam channel to be communicated with the second absorber 7, generator 3 also has concentrated solution pipeline through solution pump 9, solution heat exchanger 12 is communicated with the second absorber 7 with the second solution heat exchanger 13, second absorber 7 also has weak solution pipeline to be communicated with absorber 5 through the second solution heat exchanger 13, absorber 5 also has weak solution pipeline to be communicated with generator 3 through solution heat exchanger 12, generator 3 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has weak solution pipeline to be communicated with the 4th absorber 24 with the 3rd solution heat exchanger 17 through the second solution pump 16, 4th absorber 24 also has weak solution pipeline to be communicated with the second generator 14 through the 3rd solution pump 25, second generator 14 also has concentrated solution pipeline to be communicated with the 3rd generator 23 through solution choke valve 21, 3rd generator 23 also has concentrated solution pipeline to be communicated with the 3rd absorber 15 through the 3rd solution heat exchanger 17, 3rd generator 23 also has refrigerant steam channel to be communicated with the 4th absorber 24, second generator 14 also has refrigerant steam channel to be communicated with condenser 4, condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 10 and ft connection, condenser 4, the 3rd absorber 15 and the 4th absorber 24 also have cooling medium pipeline and ft connection respectively, and absorber 5 and the second absorber 7 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with moving alliance with the heat shown in Figure 77, difference is: engine 1 provides the second steam directly to the second absorber 7, and engine 1 provides steam discharge directly to absorber 5.
Heat shown in Figure 79 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 77, exhaust passage is had to be communicated with evaporimeter 6 successively in engine 1, 3rd generator 23, second generator 14 has condensate liquid pipeline and ft connection to be adjusted to engine 1 with generator 3 after generator 3 again has exhaust passage to be communicated with the 3rd generator 23 successively, second generator 14 and generator 3 afterwards generator 3 have condensate liquid pipeline and ft connection again, engine 1 is had the second steam channel be communicated with the second evaporimeter 8 after the second evaporimeter 8 finisher 6 of having the second condensate liquid pipeline and ft connection to be adjusted to engine 1 again to have the second steam channel to be communicated with evaporimeter 6 have the second condensate liquid pipeline and ft connection again, the second evaporimeter 8 after the 3rd steam channel is communicated with the second evaporimeter 8 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again.
(2) in flow process, compared with moving alliance with the heat shown in Figure 77, difference is: engine 1 provides the 3rd steam to the second evaporimeter 8, and engine 1 provides the second steam to evaporimeter 6, and engine 1 only provides steam discharge to the 3rd generator 23, second generator 14 and generator 3.
Heat shown in Figure 80 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 78, cancel the exhaust passage that engine 1 is communicated with absorber 5, being had by engine 1 second steam channel to be communicated with the second absorber 7 to be adjusted to engine 1 has the second steam channel to be communicated with absorber 5, engine 1 is set up the 3rd steam channel and is communicated with the second absorber 7, forms the dynamic co-feeding system of heat.
Heat shown in Figure 81 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 5, increase by the 3rd absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator 3 there is concentrated solution pipeline through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 are communicated with the second absorber 7 and are adjusted to generator 3 and have concentrated solution pipeline through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 is communicated with the 3rd absorber 15 with the 3rd solution heat exchanger 17, 3rd absorber 15 has weak solution pipeline to be communicated with the second absorber 7 through the 3rd solution heat exchanger 17 again, the 3rd evaporimeter 19 after the 4th steam channel is communicated with the 3rd evaporimeter 19 set up by engine 1 the 4th condensate liquid pipeline and ft connection again, condenser 4 is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 15, 3rd absorber 15 also has heated medium pipeline and ft connection.
(2) in flow process, engine 1 provides the 4th steam to the 3rd evaporimeter 19, and the heat release in the 3rd evaporimeter 19 of the 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid; The concentrated solution of generator 3 enters the 3rd absorber 15 through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 and the 3rd solution heat exchanger 17, concentrated solution in the 3rd absorber 15, absorb refrigerant vapour and heat release in heated medium, the weak solution of the 3rd absorber 15 enters the second absorber 7 through the 3rd solution heat exchanger 17; The cryogen liquid of condenser 4 is divided into three tunnels, and the 3rd tunnel the 3rd cryogen liquid pump 20 pressurization enters the 3rd evaporimeter 19, absorbs into refrigerant vapour and provide to the 3rd absorber 15, forms the dynamic co-feeding system of heat.
Heat shown in Figure 82 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 9, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator 3 there is concentrated solution pipeline through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 are communicated with the second absorber 7 and are adjusted to generator 3 and have concentrated solution pipeline through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 is communicated with the 4th absorber 24 with the 4th solution heat exchanger 26, 4th absorber 24 has weak solution pipeline to be communicated with the second absorber 7 through the 4th solution heat exchanger 26 again, the 3rd evaporimeter 19 after the 3rd steam channel is communicated with the 3rd evaporimeter 19 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again, condenser 4 is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has heated medium pipeline and ft connection.
(2) in flow process, engine 1 provides the 3rd steam to the 3rd evaporimeter 19, and the heat release in the 3rd evaporimeter 19 of the 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid; The concentrated solution of generator 3 enters the 4th absorber 24 through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 and the 4th solution heat exchanger 26, concentrated solution in the 4th absorber 24, absorb refrigerant vapour and heat release in heated medium, the weak solution of the 4th absorber 24 enters the second absorber 7 through the 4th solution heat exchanger 26; The cryogen liquid of condenser 4 is divided into three tunnels, and the 3rd tunnel the 3rd cryogen liquid pump 20 pressurization enters the 3rd evaporimeter 19, absorbs into refrigerant vapour and provide to the 4th absorber 24, forms the dynamic co-feeding system of heat.
Heat shown in Figure 83 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 27, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, steam chest 22 will be divided to have concentrated solution pipeline through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 are communicated with the second absorber 7 and are adjusted to point steam chest 22 and have concentrated solution pipeline through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 is communicated with the 4th absorber 24 with the 4th solution heat exchanger 26, 4th absorber 24 has weak solution pipeline to be communicated with the second absorber 7 through the 4th solution heat exchanger 26 again, the 4th evaporimeter 27 after the 4th steam channel is communicated with the 4th evaporimeter 27 set up by engine 1 the 4th condensate liquid pipeline and ft connection again, condenser 4 is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter 27 through the 4th cryogen liquid pump 28, 4th evaporimeter 27 also has refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has heated medium pipeline and ft connection.
(2) in flow process, engine 1 provides the 4th steam to the 4th evaporimeter 27, and the heat release in the 4th evaporimeter 27 of the 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid; The concentrated solution of steam chest 22 is divided to enter the 4th absorber 24 through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 and the 4th solution heat exchanger 26, concentrated solution in the 4th absorber 24, absorb refrigerant vapour and heat release in heated medium, the weak solution of the 4th absorber 24 enters the second absorber 7 through the 4th solution heat exchanger 26; The cryogen liquid of condenser 4 is divided into three tunnels, and the 3rd tunnel the 4th cryogen liquid pump 28 pressurization enters the 4th evaporimeter 27, absorbs into refrigerant vapour and provide to the 4th absorber 24, forms the dynamic co-feeding system of heat.
Heat shown in Figure 84 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 41, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator 3 there is concentrated solution pipeline through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 are communicated with the second absorber 7 and are adjusted to generator 3 and have concentrated solution pipeline through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 is communicated with the 4th absorber 24 with the 4th solution heat exchanger 26, 4th absorber 24 has weak solution pipeline to be communicated with the second absorber 7 through the 4th solution heat exchanger 26 again, generator 3 is had refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 11 with cryogen liquid pump 10 respectively to be again adjusted to generator 3 have refrigerant steam channel be communicated with the second generator 14 after the second generator 14 have again cryogen liquid pipeline respectively with cryogen liquid pump 10, second cryogen liquid pump 11 is communicated with the 4th cryogen liquid pump 28, 4th cryogen liquid pump 28 also has cryogen liquid pipeline to be communicated with the 4th evaporimeter 27, the 4th evaporimeter 27 after the 3rd steam channel is communicated with the 4th evaporimeter 27 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again, 4th evaporimeter 27 also has refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has heated medium pipeline and ft connection.
(2) in flow process, engine 1 provides the 3rd steam to the 4th evaporimeter 27, and the heat release in the 4th evaporimeter 27 of the 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid; The concentrated solution of generator 3 enters the 4th absorber 24 through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 and the 4th solution heat exchanger 26, concentrated solution in the 4th absorber 24, absorb refrigerant vapour and heat release in heated medium, the weak solution of the 4th absorber 24 enters the second absorber 7 through the 4th solution heat exchanger 26; The refrigerant vapour heat release flowing through the second generator 14 is divided into three tunnels after becoming cryogen liquid, and the 3rd road cryogen liquid enters the 4th evaporimeter 27 through the 4th cryogen liquid pump 28 pressurization, absorbs heat into refrigerant vapour and provide to the 4th absorber 24, forms the dynamic co-feeding system of heat.
Heat shown in Figure 85 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 61, increase by the 4th absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator 14 there is concentrated solution pipeline through solution pump 9, solution heat exchanger 12 and the second solution heat exchanger 13 are communicated with the second absorber 7 and are adjusted to the second generator 14 and have concentrated solution pipeline through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 is communicated with the 4th absorber 24 with the 3rd solution heat exchanger 17, 4th absorber 24 has weak solution pipeline to be communicated with the second absorber 7 through the 3rd solution heat exchanger 17 again, the 3rd evaporimeter 19 after the 3rd steam channel is communicated with the 3rd evaporimeter 19 set up by engine 1 the 3rd condensate liquid pipeline and ft connection again, condenser 4 is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter 19 through the 3rd cryogen liquid pump 20, 3rd evaporimeter 19 also has refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has heated medium pipeline and ft connection.
(2) in flow process, engine 1 provides the 3rd steam to the 3rd evaporimeter 19, and the heat release in the 3rd evaporimeter 19 of the 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid; The concentrated solution of the second generator 14 enters the 4th absorber 24 through solution pump 9, solution heat exchanger 12, second solution heat exchanger 13 and the 3rd solution heat exchanger 17, concentrated solution in the 4th absorber 24, absorb refrigerant vapour and heat release in heated medium, the weak solution of the 4th absorber 24 enters the second absorber 7 through the 3rd solution heat exchanger 17; The cryogen liquid of condenser 4 is divided into three tunnels, and the 3rd tunnel the 3rd cryogen liquid pump 20 pressurization enters the 3rd evaporimeter 19, absorbs into refrigerant vapour and provide to the 4th absorber 24, forms the dynamic co-feeding system of heat.
Heat shown in Figure 86 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 1, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber C has weak solution pipeline to be communicated with newly-increased second absorber D with newly-increased solution heat exchanger J through newly-increased solution pump H, newly-increased second absorber D also has weak solution pipeline to be communicated with newly-increased generator A with newly-increased second solution heat exchanger K through newly-increased second solution pump I, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased second generator B through newly-increased second solution heat exchanger K, newly-increased second generator B also has concentrated solution pipeline to be communicated with newly-increased absorber C through newly-increased solution heat exchanger J, newly-increased second generator B also has refrigerant steam channel to be communicated with newly-increased second absorber D, newly-increased generator A also has refrigerant steam channel to be communicated with newly-increased condenser E, newly-increased condenser E also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter F through newly-increased choke valve G, newly-increased evaporimeter F also has refrigerant steam channel to be communicated with newly-increased absorber C, absorber 5 and the second absorber 7 there are heated medium pipeline and ft connection to be adjusted to absorber 5 respectively and have that circulating thermal medium pipeline is communicated with the second absorber 7 successively, newly-increased generator A, newly-increased second generator B, newly-increased heat exchanger L, newly-increased evaporimeter F and circulating pump M after circulating pump M have circulating thermal medium pipeline be communicated with absorber 5 and form closed-loop path again, newly-increased absorber C, newly-increased second absorber D, increase condenser E and newly-increased heat exchanger L newly and also have heated medium pipeline and ft connection respectively.
(2) in flow process, circulating thermal medium flows through absorber 5 successively and the heat absorption of the second absorber 7 heats up, circulating thermal medium after intensification flows through newly-increased generator A, newly-increased second generator B, newly-increased heat exchanger L and newly-increased evaporimeter F also progressively heat release cooling successively, and the circulating thermal medium after cooling provides to absorber 5 after being pressurizeed by circulating pump M again, the weak solution of newly-increased absorber C enters newly-increased second absorber D through newly-increased solution pump H and newly-increased solution heat exchanger J, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased second absorber D enters newly-increased generator A through newly-increased second solution pump I and newly-increased second solution heat exchanger K, absorb heat and discharge refrigerant vapour and provide to newly-increased condenser E, the concentrated solution of newly-increased generator A enters newly-increased second generator B through newly-increased second solution heat exchanger K, heat absorption release refrigerant vapour also provides to newly-increased second absorber D, the concentrated solution of newly-increased second generator B enters newly-increased absorber C through newly-increased solution heat exchanger J, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of newly-increased condenser E becomes cryogen liquid in heated medium, and the cryogen liquid of newly-increased condenser E enters newly-increased evaporimeter F through newly-increased choke valve G reducing pressure by regulating flow, absorbs heat into refrigerant vapour and provide to newly-increased absorber C, forms the dynamic co-feeding system of heat.
Heat shown in Figure 87 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Figure 86, increase newly-increased 3rd generator, newly-increased 3rd absorber, newly-increased 3rd solution pump and newly-increased 3rd solution heat exchanger, had by newly-increased absorber C weak solution pipeline to be communicated with newly-increased second absorber D through newly-increased solution pump H and newly-increased solution heat exchanger J to be adjusted to newly-increased absorber C and to have weak solution pipeline warp to increase solution pump H newly to be communicated with newly-increased 3rd absorber O with newly-increased solution heat exchanger J, newly-increased 3rd absorber O has weak solution pipeline to be communicated with newly-increased second absorber D with newly-increased 3rd solution heat exchanger Q through newly-increased 3rd solution pump P again, had by newly-increased second generator B concentrated solution pipeline to be communicated with newly-increased absorber C through newly-increased solution heat exchanger J to be adjusted to newly-increased second generator B and to have concentrated solution pipeline warp to increase the 3rd solution heat exchanger Q newly to be communicated with newly-increased 3rd generator N, newly-increased 3rd generator N has concentrated solution pipeline to be communicated with newly-increased absorber C through newly-increased solution heat exchanger J again, newly-increased 3rd generator N also has refrigerant steam channel to be communicated with newly-increased 3rd absorber O, had by newly-increased second generator B circulating thermal medium pipeline to be communicated with newly-increased evaporimeter F through newly-increased heat exchanger L to be adjusted to newly-increased second generator B and to have circulating thermal medium pipeline warp to increase the 3rd generator N newly to be communicated with newly-increased evaporimeter F with newly-increased heat exchanger L.
(2) in flow process, circulating thermal medium flows through absorber 5 successively and the heat absorption of the second absorber 7 heats up, circulating thermal medium after intensification flows through newly-increased generator A, newly-increased second generator B, newly-increased 3rd generator N, newly-increased heat exchanger L and newly-increased evaporimeter F also progressively heat release cooling successively, and the circulating thermal medium after cooling provides to absorber 5 after being pressurizeed by circulating pump M again; The weak solution of newly-increased absorber C enters newly-increased 3rd absorber O through newly-increased solution pump H and newly-increased solution heat exchanger J, absorb refrigerant vapour and heat release in heated medium, the weak solution of newly-increased 3rd absorber O enters newly-increased second absorber D through newly-increased 3rd solution pump P and newly-increased 3rd solution heat exchanger Q; The concentrated solution of newly-increased second generator B enters newly-increased 3rd generator N through newly-increased 3rd solution heat exchanger Q, absorbing heat discharges refrigerant vapour and provide to newly-increased 3rd absorber O, the concentrated solution of newly-increased 3rd generator N enters newly-increased absorber C through newly-increased solution heat exchanger J, forms the dynamic co-feeding system of heat.
Heat shown in Figure 88 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 1, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and newly-increased point steam chest; newly-increased absorber C has weak solution pipeline to be communicated with newly-increased second absorber D with newly-increased solution heat exchanger J through newly-increased solution pump H, newly-increased second absorber D also has weak solution pipeline to be communicated with newly-increased second generator B through solution choke valve T, newly-increased second generator B also has concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased second solution pump I, newly-increased generator A also has concentrated solution pipeline to be communicated with a newly-increased point steam chest V with newly-increased second absorber D through newly-increased second solution choke valve U, a newly-increased point steam chest V also has concentrated solution pipeline to be communicated with newly-increased absorber C through newly-increased solution heat exchanger J, newly-increased generator A also has refrigerant steam channel to be communicated with newly-increased second absorber D, newly-increased second generator B also has refrigerant steam channel to be communicated with newly-increased condenser E, newly-increased condenser E also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter F through newly-increased choke valve G, a newly-increased point steam chest V also has refrigerant steam channel to be communicated with newly-increased second condenser R, newly-increased second condenser R also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter F through newly-increased second throttle S, newly-increased evaporimeter F also has refrigerant steam channel to be communicated with newly-increased absorber C, absorber 5 and the second absorber 7 there are heated medium pipeline and ft connection to be adjusted to absorber 5 respectively and have that circulating thermal medium pipeline is communicated with the second absorber 7 successively, newly-increased generator A, newly-increased second generator B, newly-increased heat exchanger L, newly-increased evaporimeter F and circulating pump M after circulating pump M have circulating thermal medium pipeline be communicated with absorber 5 and form closed-loop path again, newly-increased absorber C, newly-increased condenser E, increase the second condenser R and newly-increased heat exchanger L newly and also have heated medium pipeline and ft connection respectively.
(2) in flow process, circulating thermal medium flows through absorber 5 successively and the heat absorption of the second absorber 7 heats up, circulating thermal medium after intensification flows through newly-increased generator A, newly-increased second generator B, newly-increased heat exchanger L and newly-increased evaporimeter F also progressively heat release cooling successively, and the circulating thermal medium after cooling provides to absorber 5 after being pressurizeed by circulating pump M again, the weak solution of newly-increased absorber C enters newly-increased second absorber D through newly-increased solution pump H and newly-increased solution heat exchanger J, absorb refrigerant vapour heat release in solution, the weak solution of newly-increased second absorber D enters newly-increased second generator B through solution choke valve T reducing pressure by regulating flow, heat absorption release refrigerant vapour also provides to newly-increased condenser E, the concentrated solution of newly-increased second generator B enters newly-increased generator A through newly-increased second solution pump I pressurization, heat absorption release refrigerant vapour also provides to newly-increased second absorber D, the concentrated solution of newly-increased generator A flows through newly-increased second absorber D after the second solution choke valve U reducing pressure by regulating flow, heat absorbing part vaporization enters newly-increased point steam chest V, newly-increased point steam chest V discharges refrigerant vapour and provides to newly-increased second condenser R, the concentrated solution of newly-increased point steam chest V enters newly-increased absorber C through newly-increased solution heat exchanger J, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of newly-increased condenser E becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased condenser E enters newly-increased evaporimeter F through newly-increased choke valve G reducing pressure by regulating flow, the refrigerant vapour heat release of newly-increased second condenser R becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased second condenser R enters newly-increased evaporimeter F through newly-increased second throttle S throttling, the cryogen liquid of newly-increased evaporimeter F absorbs heat into refrigerant vapour and provides to newly-increased absorber C, forms the dynamic co-feeding system of heat.
The heat that the effect that the technology of the present invention can realize---the present invention proposes is moved co-feeding system and is had following effect and advantage:
(1) realize the utilization to the temperature difference between engine steam discharge and environment, improve heat utilization rate.
(2) the first work done (generating) of high-grade steam, for heat supply after grade reduces, meets thermal energy step and utilizes principle.
(3) engine segmentation provides low-grade steam, reduces the flow of steam at engine latter end, is conducive to the internal heat efficiency improving engine.
(4) absorber and the second absorber, or add the 3rd absorber, jointly complete the intensification to heated medium, be conducive to improving the temperature difference and utilize level, improve heat utilization rate.
(5) provide multiple concrete technical scheme, numerous different actual state can be tackled, have the wider scope of application.
(6) work steam discharge and engine intermediate extraction combines for the thermal source of absorption heat pump flow process, for meeting different user and duty requirements brings good flexibility.
(7) enriched the type of hot dynamic co-feeding system, extended the range of application of second-kind absorption-type heat pump, be conducive to adopting second-kind absorption-type heat pump to realize making full use of of the temperature difference better.

Claims (145)

1. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with evaporimeter (6) and generator (3) successively after generator (3) have condensate liquid pipeline and ft connection again, engine (1) in addition the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the second condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) also has cooling medium pipeline and ft connection, and absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has exhaust passage to be communicated with absorber (5), and engine (1) also has the second steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) also has cooling medium pipeline and ft connection, and absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 1, engine (1) is had exhaust passage be communicated with evaporimeter (6) and generator (3) successively after generator (3) have again condensate liquid pipeline and ft connection be adjusted to engine (1) have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, engine (1) is had the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the second condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the second steam channel to be communicated with evaporimeter (6) have the second condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 3rd steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 2, cancel the exhaust passage that engine (1) is communicated with absorber (5), being had by engine (1) the second steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the second steam channel to be communicated with absorber (5), engine (1) is set up the 3rd steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with evaporimeter (6) and generator (3) successively after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) in addition the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) also has cooling medium pipeline and ft connection, and absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger and the second solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with absorber (5), and engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) also has cooling medium pipeline and ft connection, and absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 5, engine (1) is had the second steam channel be communicated with evaporimeter (6) and generator (3) successively after generator (3) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 6, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also has exhaust passage to be communicated with generator (3) after evaporimeter (6), the second generator (14) and generator (3) successively and has condensate liquid pipeline and ft connection again, engine (1) in addition the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the second condensate liquid pipeline and ft connection again; generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has exhaust passage to be communicated with absorber (5), and engine (1) also has the second steam channel to be communicated with the second absorber (7); generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, move in co-feeding system in heat according to claim 9, exhaust passage is had to be communicated with evaporimeter (6) successively in engine (1), after second generator (14) and generator (3) generator (3) have again condensate liquid pipeline and ft connection be adjusted to engine (1) have exhaust passage be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) is had the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the second condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the second steam channel to be communicated with evaporimeter (6) have the second condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 3rd steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
12. main heat move co-feeding system, move in co-feeding system in heat according to claim 10, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the second steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the second steam channel to be communicated with absorber (5), engine (1) is set up the 3rd steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with the second generator (14) after the second generator (14) have condensate liquid pipeline and ft connection again, engine (1) also have the second steam channel be communicated with successively evaporimeter (6) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
14. main heat moves co-feeding system, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with the second generator (14) after the second generator (14) have condensate liquid pipeline and ft connection again, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with absorber (5), engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, move in co-feeding system in heat according to claim 13, engine (1) is had the second steam channel be communicated with evaporimeter (6) and generator (3) successively after generator (3) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, move in co-feeding system in heat according to claim 14, cancelling engine (1) has the second steam channel to be communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also has the second steam channel to be communicated with generator (3) after evaporimeter (6), the second generator (14) and generator (3) successively and has the second condensate liquid pipeline and ft connection again, engine (1) in addition the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again; generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
18. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with absorber (5), and engine (1) also has the 3rd steam channel to be communicated with the second absorber (7); generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, move in co-feeding system in heat according to claim 17, the second steam channel is had to be communicated with evaporimeter (6) successively in engine (1), after second generator (14) and generator (3) generator (3) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, move in co-feeding system in heat according to claim 18, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with the second generator (14) after the second generator (14) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with successively evaporimeter (6) and generator (3) afterwards generator (3) have the 3rd condensate liquid pipeline and ft connection again, engine (1) also have the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 4th condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
22. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with the second generator (14) after the second generator (14) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with generator (3) after generator (3) have the 3rd condensate liquid pipeline and ft connection again, engine (1) also has the 3rd steam channel to be communicated with absorber (5), engine (1) also has the 4th steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) with the 3rd solution heat exchanger (17) through the second solution pump (16), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, move in co-feeding system in heat according to claim 21, engine (1) is had the 3rd steam channel be communicated with evaporimeter (6) and generator (3) successively after generator (3) have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine (1) have the 3rd steam channel be communicated with generator (3) after generator (3) have the 3rd condensate liquid pipeline and ft connection again, engine (1) is had the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 4th steam channel to be communicated with evaporimeter (6) have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 5th steaming passage is communicated with the second evaporimeter (8) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, move in co-feeding system in heat according to claim 22, cancel the 3rd steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 4th steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 4th steam channel to be communicated with absorber (5), engine (1) is set up the 5th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 25. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also has exhaust passage to be communicated with generator (3) after evaporimeter (6), the 3rd evaporimeter (19) and generator (3) successively and has condensate liquid pipeline and ft connection again, engine (1) in addition the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the second condensate liquid pipeline and ft connection again; steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7): generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), second condenser (18) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has exhaust passage to be communicated with the 3rd absorber (15), engine (1) also has exhaust passage to be communicated with absorber (5), and engine (1) also has the second steam channel to be communicated with the second absorber (7), steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), and the second condenser (18) also has cryogen liquid pipeline through the second cryogen liquid pump (11) and ft connection, condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, move in co-feeding system in heat according to claim 25, exhaust passage is had to be communicated with evaporimeter (6) successively in engine (1), after 3rd evaporimeter (19) and generator (3) generator (3) have again condensate liquid pipeline and ft connection be adjusted to engine (1) have exhaust passage be communicated with successively the 3rd evaporimeter (19) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) is had the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the second condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the second steam channel to be communicated with evaporimeter (6) have the second condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 3rd steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, move in co-feeding system in heat according to claim 26, cancel the exhaust passage that engine (1) is communicated with absorber (5), being had by engine (1) the second steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the second steam channel to be communicated with absorber (5), engine (1) is set up the 3rd steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 29. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, engine (1) also have the second steam channel be communicated with successively evaporimeter (6) and the 3rd evaporimeter (19) afterwards the 3rd evaporimeter (19) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), second condenser (18) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with the 3rd absorber (15), engine (1) also has the second steam channel to be communicated with absorber (5), engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), and the second condenser (18) also has cryogen liquid pipeline through the second cryogen liquid pump (11) and ft connection, condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, move in co-feeding system in heat according to claim 29, engine (1) is had the second steam channel be communicated with evaporimeter (6) and the 3rd evaporimeter (19) successively after the 3rd evaporimeter (19) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with the 3rd evaporimeter (19) after the 3rd evaporimeter (19) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, move in co-feeding system in heat according to claim 30, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 33. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also has the second steam channel to be communicated with generator (3) after evaporimeter (6), the 3rd evaporimeter (19) and generator (3) successively and has the second condensate liquid pipeline and ft connection again, engine (1) in addition the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), second condenser (18) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 34. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with the 3rd absorber (15), engine (1) also has the second steam channel to be communicated with absorber (5), engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), and the second condenser (18) also has cryogen liquid pipeline through the second cryogen liquid pump (11) and ft connection, condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 35. heat, move in co-feeding system in heat according to claim 33, the second steam channel is had to be communicated with evaporimeter (6) successively in engine (1), after 3rd evaporimeter (19) and generator (3) generator (3) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with successively the 3rd evaporimeter (19) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 36. heat, move in co-feeding system in heat according to claim 34, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 37. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, the 3rd evaporimeter, the 3rd cryogen liquid pump, solution choke valve and a point steam chest, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with successively evaporimeter (6) and the 3rd evaporimeter (19) afterwards the 3rd evaporimeter (19) have the 3rd condensate liquid pipeline and ft connection again, engine (1) also have the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 4th condensate liquid pipeline and ft connection again, steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), second condenser (18) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 38. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the second condenser, solution choke valve and a point steam chest, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the 3rd steam channel to be communicated with the 3rd absorber (15), engine (1) also has the 3rd steam channel to be communicated with absorber (5), engine (1) also has the 4th steam channel to be communicated with the second absorber (7), steam chest (22) is divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline through solution heat exchanger (12), solution choke valve (21) is communicated with a point steam chest (22) with the 3rd absorber (15), steam chest (22) is divided to also have refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, generator (3) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the 3rd solution heat exchanger (17), generator (3) also has refrigerant steam channel to be communicated with the second condenser (18), and the second condenser (18) also has cryogen liquid pipeline through the second cryogen liquid pump (11) and ft connection, condenser (4) and the second condenser (18) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, move in co-feeding system in heat according to claim 37, engine (1) is had the 3rd steam channel be communicated with evaporimeter (6) and the 3rd evaporimeter (19) successively after the 3rd evaporimeter (19) have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine (1) have the 3rd steam channel be communicated with the 3rd evaporimeter (19) after the 3rd evaporimeter (19) have the 3rd condensate liquid pipeline and ft connection again, engine (1) is had the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 4th steam channel to be communicated with evaporimeter (6) have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 5th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 40. heat, move in co-feeding system in heat according to claim 38, cancel the 3rd steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 4th steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 4th steam channel to be communicated with absorber (5), engine (1) is set up the 5th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also has exhaust passage to be communicated with generator (3) after evaporimeter (6), the 3rd evaporimeter (19) and generator (3) successively and has condensate liquid pipeline and ft connection again, engine (1) in addition the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the second condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively again, cryogen liquid pump (10) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), second cryogen liquid pump (11) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 42. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with successively evaporimeter (6) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has exhaust passage to be communicated with absorber (5), and engine (1) also has the second steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline again through the second cryogen liquid pump (11) and ft connection, second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 43. heat, move in co-feeding system in heat according to claim 41, exhaust passage is had to be communicated with evaporimeter (6) successively in engine (1), after 3rd evaporimeter (19) and generator (3) generator (3) have again condensate liquid pipeline and ft connection be adjusted to engine (1) have exhaust passage be communicated with successively the 3rd evaporimeter (19) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) is had the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the second condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the second steam channel to be communicated with evaporimeter (6) have the second condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 3rd steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 44. heat, move in co-feeding system in heat according to claim 42, cancel the exhaust passage that engine (1) is communicated with absorber (5), being had by engine (1) the second steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the second steam channel to be communicated with absorber (5), engine (1) is set up the 3rd steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 45. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, engine (1) also have the second steam channel be communicated with successively evaporimeter (6) and the 3rd evaporimeter (19) afterwards the 3rd evaporimeter (19) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively again, cryogen liquid pump (10) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), second cryogen liquid pump (11) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 46. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (1) also has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with absorber (5), engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline again through the second cryogen liquid pump (11) and ft connection, second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 47. heat, move in co-feeding system in heat according to claim 45, engine (1) is had the second steam channel be communicated with evaporimeter (6) and the 3rd evaporimeter (19) successively after the 3rd evaporimeter (19) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with the 3rd evaporimeter (19) after the 3rd evaporimeter (19) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, move in co-feeding system in heat according to claim 46, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also has the second steam channel to be communicated with generator (3) after evaporimeter (6), the 3rd evaporimeter (19) and generator (3) successively and has the second condensate liquid pipeline and ft connection again, engine (1) in addition the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively again, cryogen liquid pump (10) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), second cryogen liquid pump (11) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has rare molten, liquid pipeline is communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 50. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with successively evaporimeter (6) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with absorber (5), and engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline again through the second cryogen liquid pump (11) and ft connection, second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 51. heat, move in co-feeding system in heat according to claim 49, the second steam channel is had to be communicated with evaporimeter (6) successively in engine (1), after 3rd evaporimeter (19) and generator (3) generator (3) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with successively the 3rd evaporimeter (19) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 52. heat, move in co-feeding system in heat according to claim 50, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 53. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, the 3rd evaporimeter and the 3rd cryogen liquid pump, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with successively evaporimeter (6) and the 3rd evaporimeter (19) afterwards the 3rd evaporimeter (19) have the 3rd condensate liquid pipeline and ft connection again, engine (1) also have the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 4th condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively again, cryogen liquid pump (10) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), second cryogen liquid pump (11) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 54. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, the finisher (6) that engine (1) also has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, engine (1) also has the 3rd steam channel to be communicated with absorber (5), engine (1) also has the 4th steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline again through the second cryogen liquid pump (11) and ft connection, second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 55. heat, that heat described in claim 53 is moved in co-feeding system, engine (1) is had the 3rd steam channel be communicated with evaporimeter (6) and the 3rd evaporimeter (19) successively after the 3rd evaporimeter (19) have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine (1) have the 3rd steam channel be communicated with the 3rd evaporimeter (19) after the 3rd evaporimeter (19) have the 3rd condensate liquid pipeline and ft connection again, engine (1) is had the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 4th steam channel to be communicated with evaporimeter (6) have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 5th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 56. heat, that heat described in claim 54 is moved in co-feeding system, cancel the 3rd steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 4th steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 4th steam channel to be communicated with absorber (5), engine (1) is set up the 5th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 57. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger and the 3rd cryogen liquid pump, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with evaporimeter (6) and generator (3) successively after generator (3) have condensate liquid pipeline and ft connection again, engine (1) in addition the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the second condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively again, cryogen liquid pump (10) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), second cryogen liquid pump (11) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd cryogen liquid pump (20), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 58. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with generator (3) after generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has exhaust passage to be communicated with the 3rd absorber (15), engine (1) also has exhaust passage to be communicated with absorber (5), and engine (1) also has the second steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline again through the second cryogen liquid pump (11) and ft connection, second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), and condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 59. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger and the 3rd cryogen liquid pump, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with evaporimeter (6) and generator (3) successively after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) in addition the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively again, cryogen liquid pump (10) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), second cryogen liquid pump (11) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through the 3rd cryogen liquid pump (20), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (15), condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 60. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with the 3rd absorber (15) with absorber (5) respectively, and engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline again through the second cryogen liquid pump (11) and ft connection, second generator (14) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17) through the second solution pump (16), 3rd absorber (15) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), and condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) also has cooling medium pipeline and ft connection, absorber (5), the second absorber (7) and the 3rd absorber (15) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 61. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also has exhaust passage to be communicated with generator (3) after evaporimeter (6), the second generator (14) and generator (3) successively and has condensate liquid pipeline and ft connection again, engine (1) in addition the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the second condensate liquid pipeline and ft connection again; second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through solution choke valve (21), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
62. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has exhaust passage to be communicated with absorber (5), and engine (1) also has the second steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through solution choke valve (21), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 63. heat, that heat described in claim 61 is moved in co-feeding system, exhaust passage is had to be communicated with evaporimeter (6) successively in engine (1), after second generator (14) and generator (3) generator (3) have again condensate liquid pipeline and ft connection be adjusted to engine (1) have exhaust passage be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) is had the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the second condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the second steam channel to be communicated with evaporimeter (6) have the second condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 3rd steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 64. heat, that heat described in claim 62 is moved in co-feeding system, cancel the exhaust passage that engine (1) is communicated with absorber (5), being had by engine (1) the second steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the second steam channel to be communicated with absorber (5), engine (1) is set up the 3rd steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 65. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with the second generator (14) after the second generator (14) have condensate liquid pipeline and ft connection again, engine (1) also have the second steam channel be communicated with successively evaporimeter (6) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again, second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) with the 3rd solution heat exchanger (17) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
66. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with the second generator (14) after the second generator (14) have condensate liquid pipeline and ft connection again, engine (1) also have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with absorber (5), engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) with the 3rd solution heat exchanger (17) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 67. heat, that heat described in claim 65 is moved in co-feeding system, engine (1) is had the second steam channel be communicated with evaporimeter (6) and generator (3) successively after generator (3) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with generator (3) after generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 68. heat, that heat described in claim 66 is moved in co-feeding system, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 69. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also has the second steam channel to be communicated with generator (3) after evaporimeter (6), the second generator (14) and generator (3) successively and has the second condensate liquid pipeline and ft connection again, engine (1) in addition the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 3rd condensate liquid pipeline and ft connection again; second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through solution choke valve (21), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
70. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and solution choke valve, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) also has the second steam channel to be communicated with absorber (5), and engine (1) also has the 3rd steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through solution choke valve (21), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 71. heat, that heat described in claim 69 is moved in co-feeding system, the second steam channel is had to be communicated with evaporimeter (6) successively in engine (1), after second generator (14) and generator (3) generator (3) have again the second condensate liquid pipeline and ft connection be adjusted to engine (1) have the second steam channel be communicated with successively the second generator (14) and generator (3) afterwards generator (3) have the second condensate liquid pipeline and ft connection again, engine (1) is had the 3rd steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 3rd steam channel to be communicated with evaporimeter (6) have the 3rd condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 4th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 72. heat, that heat described in claim 70 is moved in co-feeding system, cancel the second steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 3rd steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 3rd steam channel to be communicated with absorber (5), engine (1) is set up the 4th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 73. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with the second generator (14) after the second generator (14) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with successively evaporimeter (6) and generator (3) afterwards generator (3) have the 3rd condensate liquid pipeline and ft connection again, engine (1) also have the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the 4th condensate liquid pipeline and ft connection again, second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) with the 3rd solution heat exchanger (17) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
74. the dynamic co-feeding system of heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump and the 3rd solution heat exchanger, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) also has exhaust passage and ft connection, engine (1) also have the second steam channel be communicated with the second generator (14) after the second generator (14) have the second condensate liquid pipeline and ft connection again, engine (1) also have the 3rd steam channel be communicated with generator (3) after generator (3) have the 3rd condensate liquid pipeline and ft connection again, engine (1) also has the 3rd steam channel to be communicated with absorber (5), engine (1) also has the 4th steam channel to be communicated with the second absorber (7), second generator (14) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with the 3rd absorber (15) through solution heat exchanger (12), 3rd absorber (15) also has weak solution pipeline to be communicated with generator (3) with the 3rd solution heat exchanger (17) through the second solution pump (16), generator (3) also has concentrated solution pipeline to be communicated with the second generator (14) through the 3rd solution heat exchanger (17), second generator (14) also has refrigerant steam channel to be communicated with the 3rd absorber (15), generator (3) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4) and the 3rd absorber (15) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 75. heat, that heat described in claim 73 is moved in co-feeding system, engine (1) is had the 3rd steam channel be communicated with evaporimeter (6) and generator (3) successively after generator (3) have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine (1) have the 3rd steam channel be communicated with generator (3) after generator (3) have the 3rd condensate liquid pipeline and ft connection to adjust again, engine (1) is had the 4th steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the 4th condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the 4th steam channel to be communicated with evaporimeter (6) have the 4th condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 5th steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 76. heat, that heat described in claim 74 is moved in co-feeding system, cancel the 3rd steam channel that engine (1) is communicated with absorber (5), being had by engine (1) the 4th steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the 4th steam channel to be communicated with absorber (5), engine (1) is set up the 5th steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 77. heat, formed primarily of engine, working machine, generator, condenser, absorber, evaporimeter, the second absorber, the second evaporimeter, solution pump, cryogen liquid pump, the second cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, solution choke valve, the 3rd generator, the 4th absorber and the 3rd solution pump, engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also has exhaust passage to be communicated with evaporimeter (6) successively, 3rd generator (23), second generator (14) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) also have the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) have the second condensate liquid pipeline and ft connection again, generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17) through the second solution pump (16), 4th absorber (24) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution pump (25), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd generator (23) through solution choke valve (21), 3rd generator (23) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), 3rd generator (23) also has refrigerant steam channel to be communicated with the 4th absorber (24), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (10), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (5), condenser (4) also has cryogen liquid pipeline to be communicated with the second evaporimeter (8) through the second cryogen liquid pump (11), second evaporimeter (8) also has refrigerant steam channel to be communicated with the second absorber (7), condenser (4), the 3rd absorber (15) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 78. heat, formed primarily of engine, working machine, generator, condenser, absorber, the second absorber, solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, the second generator, the 3rd absorber, the second solution pump, the 3rd solution heat exchanger, solution choke valve, the 3rd generator, the 4th absorber and the 3rd solution pump; Engine (1) connects working machine (2), engine (1) has live steam passage and ft connection, engine (1) or in addition exhaust passage and ft connection, engine (1) also have exhaust passage be communicated with successively the 3rd generator (23), the second generator (14) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) also has exhaust passage to be communicated with absorber (5), and engine (1) also has the second steam channel to be communicated with the second absorber (7); generator (3) also has concentrated solution pipeline through solution pump (9), solution heat exchanger (12) is communicated with the second absorber (7) with the second solution heat exchanger (13), second absorber (7) also has weak solution pipeline to be communicated with absorber (5) through the second solution heat exchanger (13), absorber (5) also has weak solution pipeline to be communicated with generator (3) through solution heat exchanger (12), generator (3) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has weak solution pipeline to be communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17) through the second solution pump (16), 4th absorber (24) also has weak solution pipeline to be communicated with the second generator (14) through the 3rd solution pump (25), second generator (14) also has concentrated solution pipeline to be communicated with the 3rd generator (23) through solution choke valve (21), 3rd generator (23) also has concentrated solution pipeline to be communicated with the 3rd absorber (15) through the 3rd solution heat exchanger (17), 3rd generator (23) also has refrigerant steam channel to be communicated with the 4th absorber (24), second generator (14) also has refrigerant steam channel to be communicated with condenser (4), condenser (4) also has cryogen liquid pipeline through cryogen liquid pump (10) and ft connection, condenser (4), the 3rd absorber (15) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, absorber (5) and the second absorber (7) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 79. heat, that heat shown in claim 77 is moved in co-feeding system, exhaust passage is had to be communicated with evaporimeter (6) successively in engine (1), 3rd generator (23), second generator (14) has condensate liquid pipeline and ft connection to be adjusted to engine (1) with generator (3) after generator (3) again has exhaust passage to be communicated with the 3rd generator (23) successively, second generator (14) and generator (3) afterwards generator (3) have condensate liquid pipeline and ft connection again, engine (1) is had the second steam channel be communicated with the second evaporimeter (8) after the second evaporimeter (8) finisher (6) of having the second condensate liquid pipeline and ft connection to be adjusted to engine (1) again to have the second steam channel to be communicated with evaporimeter (6) have the second condensate liquid pipeline and ft connection again, the second evaporimeter (8) after the 3rd steam channel is communicated with the second evaporimeter (8) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 80. heat, that heat shown in claim 78 is moved in co-feeding system, cancel the exhaust passage that engine (1) is communicated with absorber (5), being had by engine (1) the second steam channel to be communicated with the second absorber (7) to be adjusted to engine (1) has the second steam channel to be communicated with absorber (5), engine (1) is set up the 3rd steam channel and is communicated with the second absorber (7), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 81. heat, move in co-feeding system in heat according to claim 1, increase by the 3rd absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17), 3rd absorber (15) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, the 3rd evaporimeter (19) after the 3rd steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 82. heat, move in co-feeding system in heat according to claim 2, increase the 3rd absorber and the 3rd solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17), 3rd absorber (15) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, engine (1) is set up the 3rd steam channel and is communicated with the 3rd absorber (15), 3rd absorber (15) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 83. heat, move in co-feeding system in claim 3 or heat according to claim 5, increase by the 3rd absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17), 3rd absorber (15) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, the 3rd evaporimeter (19) after the 4th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 84. heat, move in co-feeding system in claim 4 or heat according to claim 6, increase the 3rd absorber and the 3rd solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17), 3rd absorber (15) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, engine (1) is set up the 4th steam channel and is communicated with the 3rd absorber (15), 3rd absorber (15) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 85. heat, move in co-feeding system in heat according to claim 7, increase by the 3rd absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17), 3rd absorber (15) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, the 3rd evaporimeter (19) after the 5th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (15), 3rd absorber (15) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 86. heat, move in co-feeding system in heat according to claim 8, increase the 3rd absorber and the 3rd solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 3rd absorber (15) with the 3rd solution heat exchanger (17), 3rd absorber (15) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, engine (1) is set up the 5th steam channel and is communicated with the 3rd absorber (15), 3rd absorber (15) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 87. heat, move in co-feeding system in heat according to claim 9, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 3rd steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 88. heat, move in co-feeding system in heat according to claim 10, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 3rd steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 89. heat, in claim 11, 13, arbitrary heat described in 17 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 4th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 90. heat, in claim 12, 14, heat described in 18 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 4th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 91. heat, in claim 15, 19, arbitrary heat described in 21 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 5th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 92. heat, in claim 16, 20, arbitrary heat described in 22 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 5th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 93. heat, move in co-feeding system in heat according to claim 23, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 6th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 6th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 94. heat, move in co-feeding system in heat according to claim 24, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 6th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 95. heat, move in co-feeding system in heat according to claim 25, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 4th evaporimeter (27) after the 3rd steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter (27) through the 4th cryogen liquid pump (28), 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 96. heat, move in co-feeding system in heat according to claim 26, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 3rd steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 97. heat, in claim 27, 29, arbitrary heat described in 33 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, steam chest (22) will be divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to a point steam chest (22) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 4th evaporimeter (27) after the 4th steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter (27) through the 4th cryogen liquid pump (28), 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 98. heat, in claim 28, 30, arbitrary heat described in 34 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, steam chest (22) will be divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to a point steam chest (22) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 4th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 99. heat, in claim 31, 35, arbitrary heat described in 37 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, steam chest (22) will be divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to a point steam chest (22) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 4th evaporimeter (27) after the 5th steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter (27) through the 4th cryogen liquid pump (28), 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 100. heat, in claim 32, 36, arbitrary heat described in 38 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, steam chest (22) will be divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to a point steam chest (22) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 5th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 101. heat, move in co-feeding system in heat according to claim 39, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, steam chest (22) will be divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to a point steam chest (22) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 4th evaporimeter (27) after the 6th steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 6th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 4th evaporimeter (27) through the 4th cryogen liquid pump (28), 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 102. heat, move in co-feeding system in heat according to claim 40, increase the 4th absorber and the 4th solution heat exchanger, steam chest (22) will be divided to have concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to a point steam chest (22) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 6th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 103. heat, move in co-feeding system in heat according to claim 41, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, generator (3) is had refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively to be again adjusted to generator (3) have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have again cryogen liquid pipeline respectively with cryogen liquid pump (10), second cryogen liquid pump (11) is communicated with the 4th cryogen liquid pump (28), 4th cryogen liquid pump (28) also has cryogen liquid pipeline to be communicated with the 4th evaporimeter (27), the 4th evaporimeter (27) after the 3rd steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 104. heat, move in co-feeding system in heat according to claim 42, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 3rd steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 105. heat, in claim 43, 45, arbitrary heat described in 49 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, generator (3) is had refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively to be again adjusted to generator (3) have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have again cryogen liquid pipeline respectively with cryogen liquid pump (10), second cryogen liquid pump (11) is communicated with the 4th cryogen liquid pump (28), 4th cryogen liquid pump (28) also has cryogen liquid pipeline to be communicated with the 4th evaporimeter (27), the 4th evaporimeter (27) after the 4th steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 106. heat, in claim 44, 46, arbitrary heat described in 50 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 4th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 107. heat, in claim 47, 51, arbitrary heat described in 53 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, generator (3) is had refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively to be again adjusted to generator (3) have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have again cryogen liquid pipeline respectively with cryogen liquid pump (10), second cryogen liquid pump (11) is communicated with the 4th cryogen liquid pump (28), 4th cryogen liquid pump (28) also has cryogen liquid pipeline to be communicated with the 4th evaporimeter (27), the 4th evaporimeter (27) after the 5th steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 108. heat, in claim 48, 52, arbitrary heat described in 54 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 5th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 109. heat, that heat described in claim 55 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 4th evaporimeter and the 4th cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, generator (3) is had refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively to be again adjusted to generator (3) have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have again cryogen liquid pipeline respectively with cryogen liquid pump (10), second cryogen liquid pump (11) is communicated with the 4th cryogen liquid pump (28), 4th cryogen liquid pump (28) also has cryogen liquid pipeline to be communicated with the 4th evaporimeter (27), the 4th evaporimeter (27) after the 6th steam channel is communicated with the 4th evaporimeter (27) set up by engine (1) the 6th condensate liquid pipeline and ft connection again, 4th evaporimeter (27) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 110. heat, that heat described in claim 56 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 6th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 111. heat, that heat described in claim 57 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 4th cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, generator (3) is had refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively to be again adjusted to generator (3) have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have again cryogen liquid pipeline respectively with cryogen liquid pump (10), second cryogen liquid pump (11) is communicated with the 4th cryogen liquid pump (28), 4th cryogen liquid pump (28) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19), the 3rd evaporimeter (19) after the 3rd steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 112. heat, that heat described in claim 58 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 3rd steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 113. heat, that heat described in claim 59 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 4th cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, generator (3) is had refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (11) with cryogen liquid pump (10) respectively to be again adjusted to generator (3) have refrigerant steam channel be communicated with the second generator (14) after the second generator (14) have again cryogen liquid pipeline respectively with cryogen liquid pump (10), second cryogen liquid pump (11) is communicated with the 4th cryogen liquid pump (28), 4th cryogen liquid pump (28) also has cryogen liquid pipeline to be communicated with the 3rd evaporimeter (19), the 3rd evaporimeter (19) after the 4th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 114. heat, that heat described in claim 60 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 4th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 115. heat, that heat described in claim 61 is moved in co-feeding system, increase by the 4th absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, the 3rd evaporimeter (19) after the 3rd steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 116. heat, that heat described in claim 62 is moved in co-feeding system, increase the 4th absorber and the 3rd solution heat exchanger, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, engine (1) is set up the 3rd steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 117. heat, that heat described in claim 65 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 4th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 118. heat, that heat described in claim 66 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 4th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 119. heat, in claim 63, arbitrary heat described in 69 is moved in co-feeding system, increase by the 4th absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, the 3rd evaporimeter (19) after the 4th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 120. heat, in claim 64, heat arbitrary described in 70 is moved in co-feeding system, increase the 4th absorber and the 3rd solution heat exchanger, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, engine (1) is set up the 4th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 121. heat, that heat described in claim 71 is moved in co-feeding system, increase by the 4th absorber, 3rd solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, the 3rd evaporimeter (19) after the 5th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 122. heat, that heat described in claim 72 is moved in co-feeding system, increase the 4th absorber and the 3rd solution heat exchanger, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 3rd solution heat exchanger (17), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 3rd solution heat exchanger (17) again, engine (1) is set up the 5th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 123. heat, in claim 67, arbitrary heat described in 73 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 5th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 5th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 124. heat, in claim 68, heat arbitrary described in 74 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 5th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 125. heat, that heat described in claim 75 is moved in co-feeding system, increase by the 4th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 6th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 6th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 126. heat, that heat described in claim 76 is moved in co-feeding system, increase the 4th absorber and the 4th solution heat exchanger, second generator (14) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to the second generator (14) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 4th absorber (24) with the 4th solution heat exchanger (26), 4th absorber (24) has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 6th steam channel and is communicated with the 4th absorber (24), 4th absorber (24) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 127. heat, that heat described in claim 77 is moved in co-feeding system, increase by the 5th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 5th absorber with the 4th solution heat exchanger (26), 5th absorber has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 3rd steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 3rd condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 128. heat, that heat described in claim 78 is moved in co-feeding system, increase the 5th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 5th absorber with the 4th solution heat exchanger (26), 5th absorber has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 3rd steam channel and is communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 129. heat, that heat described in claim 79 is moved in co-feeding system, increase by the 5th absorber, 4th solution heat exchanger, 3rd evaporimeter and the 3rd cryogen liquid pump, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 5th absorber with the 4th solution heat exchanger (26), 5th absorber has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, the 3rd evaporimeter (19) after the 4th steam channel is communicated with the 3rd evaporimeter (19) set up by engine (1) the 4th condensate liquid pipeline and ft connection again, condenser (4) is set up cryogen liquid pipeline and is communicated with the 3rd evaporimeter (19) through the 3rd cryogen liquid pump (20), 3rd evaporimeter (19) also has refrigerant steam channel to be communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 130. heat, that heat described in claim 80 is moved in co-feeding system, increase the 5th absorber and the 4th solution heat exchanger, generator (3) there is concentrated solution pipeline through solution pump (9), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second absorber (7) and are adjusted to generator (3) and have concentrated solution pipeline through solution pump (9), solution heat exchanger (12), second solution heat exchanger (13) is communicated with the 5th absorber with the 4th solution heat exchanger (26), 5th absorber has weak solution pipeline to be communicated with the second absorber (7) through the 4th solution heat exchanger (26) again, engine (1) is set up the 4th steam channel and is communicated with the 5th absorber, 5th absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 131. heat, be that arbitrary heat described in claim 1-40,61-80 is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased second solution heat exchanger (K) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased second generator (B) through newly-increased second solution heat exchanger (K), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), absorber (5) and the second absorber (7) being had heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased second absorber (D), newly-increased condenser (E) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 132. heat, be move in co-feeding system in the arbitrary heat described in claim 41-60, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased second solution heat exchanger (K) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased second generator (B) through newly-increased second solution heat exchanger (K), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by the 3rd absorber (15), absorber (5) and the second absorber (7) have heated medium pipeline and ft connection to be adjusted to the 3rd absorber (15) respectively has circulating thermal medium pipeline to be communicated with absorber (5) successively, second absorber (7), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with the 3rd absorber (15) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased second absorber (D), newly-increased condenser (E) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 133. heat, be in the arbitrary dynamic co-feeding system of the heat described in claim 81-86, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased second solution heat exchanger (K) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased second generator (B) through newly-increased second solution heat exchanger (K), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 3rd absorber (15) have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 3rd absorber (15), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased second absorber (D), newly-increased condenser (E) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 134. heat, be move in co-feeding system in the arbitrary heat described in claim 87-102, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased second solution heat exchanger (K) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased second generator (B) through newly-increased second solution heat exchanger (K), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 4th absorber (24) have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 4th absorber (24), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased second absorber (D), newly-increased condenser (E) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 135. heat, be move in co-feeding system in the arbitrary heat described in claim 103-114, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased second solution heat exchanger (K) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased second generator (B) through newly-increased second solution heat exchanger (K), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by the 3rd absorber (15), absorber (5), second absorber (7) and the 4th absorber (24) have heated medium pipeline and ft connection to be adjusted to the 3rd absorber (15) respectively has circulating thermal medium pipeline to be communicated with absorber (5) successively, second absorber (7), 4th absorber (24), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with the 3rd absorber (15) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased second absorber (D), newly-increased condenser (E) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 136. heat, be move in co-feeding system in the arbitrary heat described in claim 115-126, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased second solution heat exchanger (K) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased second generator (B) through newly-increased second solution heat exchanger (K), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 4th absorber (24) have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 4th absorber (24), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased second absorber (D), newly-increased condenser (E) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 137. heat, be move in co-feeding system in the arbitrary heat described in claim 127-130, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased second solution heat exchanger, newly-increased heat exchanger and newly-increased circulating pump, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased second solution heat exchanger (K) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased second generator (B) through newly-increased second solution heat exchanger (K), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 5th absorber have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 5th absorber, newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased second absorber (D), newly-increased condenser (E) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 138. heat, move in co-feeding system in the arbitrary heat described in claim 131-137, increase newly-increased 3rd generator, newly-increased 3rd absorber, newly-increased 3rd solution pump and newly-increased 3rd solution heat exchanger, absorber (C) will be increased newly have weak solution pipeline to be communicated with newly-increased second absorber (D) through newly-increased solution pump (H) and newly-increased solution heat exchanger (J) to be adjusted to newly-increased absorber (C) and to have weak solution pipeline warp to increase solution pump (H) newly to be communicated with newly-increased 3rd absorber (0) with newly-increased solution heat exchanger (J), newly-increased 3rd absorber (0) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased 3rd solution heat exchanger (Q) through newly-increased 3rd solution pump (P) again, the second generator (B) will be increased newly have concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J) to be adjusted to newly-increased second generator (B) and to have concentrated solution pipeline warp to increase the 3rd solution heat exchanger (Q) newly to be communicated with newly-increased 3rd generator (N), newly-increased 3rd generator (N) has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J) again, newly-increased 3rd generator (N) also has refrigerant steam channel to be communicated with newly-increased 3rd absorber (O), the second generator (B) will be increased newly have circulating thermal medium pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased heat exchanger (L) to be adjusted to newly-increased second generator (B) and to have circulating thermal medium pipeline warp to increase the 3rd generator (N) newly to be communicated with newly-increased evaporimeter (F) with newly-increased heat exchanger (L), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 139. heat, be that arbitrary heat described in claim 1-40,61-80 is moved in co-feeding system, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and a newly-increased point steam chest, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased second generator (B) through solution choke valve (T), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (V) with newly-increased second absorber (D) through newly-increased second solution choke valve (U), newly-increased point steam chest (V) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased point steam chest (V) also has refrigerant steam channel to be communicated with newly-increased second condenser (R), newly-increased second condenser (R) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased second throttle (S), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), absorber (5) and the second absorber (7) being had heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased condenser (E), newly-increased second condenser (R) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 140. heat, be move in co-feeding system in the arbitrary heat described in claim 41-60, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and newly-increased point steam chest, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased second generator (B) through solution choke valve (T), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (V) with newly-increased second absorber (D) through newly-increased second solution choke valve (U), newly-increased point steam chest (V) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased point steam chest (V) also has refrigerant steam channel to be communicated with newly-increased second condenser (R), newly-increased second condenser (R) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased second throttle (S), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by the 3rd absorber (15), absorber (5) and the second absorber (7) have heated medium pipeline and ft connection to be adjusted to the 3rd absorber (15) respectively has circulating thermal medium pipeline to be communicated with absorber (5) successively, second absorber (7), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with the 3rd absorber (15) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased condenser (E), newly-increased second condenser (R) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 141. heat, be move in co-feeding system in the arbitrary heat described in claim 81-86, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and newly-increased point steam chest, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased second generator (B) through solution choke valve (T), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (V) with newly-increased second absorber (D) through newly-increased second solution choke valve (U), newly-increased point steam chest (V) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased point steam chest (V) also has refrigerant steam channel to be communicated with newly-increased second condenser (R), newly-increased second condenser (R) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased second throttle (S), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 3rd absorber (15) have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 3rd absorber (15), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased condenser (E), newly-increased second condenser (R) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 142. heat, be move in co-feeding system in the arbitrary heat described in claim 87-102, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and newly-increased point steam chest, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased second generator (B) through solution choke valve (T), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (V) with newly-increased second absorber (D) through newly-increased second solution choke valve (U), newly-increased point steam chest (V) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased point steam chest (V) also has refrigerant steam channel to be communicated with newly-increased second condenser (R), newly-increased second condenser (R) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased second throttle (S), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 4th absorber (24) have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 4th absorber (24), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased condenser (E), newly-increased second condenser (R) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 143. heat, be move in co-feeding system in the arbitrary heat described in claim 103-114, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and newly-increased point steam chest, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased second generator (B) through solution choke valve (T), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (V) with newly-increased second absorber (D) through newly-increased second solution choke valve (U), newly-increased point steam chest (V) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased point steam chest (V) also has refrigerant steam channel to be communicated with newly-increased second condenser (R), newly-increased second condenser (R) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased second throttle (S), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by the 3rd absorber (15), absorber (5), second absorber (7) and the 4th absorber (24) have heated medium pipeline and ft connection to be adjusted to the 3rd absorber (15) respectively has circulating thermal medium pipeline to be communicated with absorber (5) successively, second absorber (7), 4th absorber (24), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with the 3rd absorber (15) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased condenser (E), newly-increased second condenser (R) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 144. heat, be move in co-feeding system in the arbitrary heat described in claim 115-126, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and newly-increased point steam chest, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased second generator (B) through solution choke valve (T), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (V) with newly-increased second absorber (D) through newly-increased second solution choke valve (U), newly-increased point steam chest (V) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased point steam chest (V) also has refrigerant steam channel to be communicated with newly-increased second condenser (R), newly-increased second condenser (R) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased second throttle (S), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 4th absorber (24) have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 4th absorber (24), newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased condenser (E), newly-increased second condenser (R) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 145. heat, be move in co-feeding system in the arbitrary heat described in claim 127-130, increase newly-increased generator, newly-increased second generator, newly-increased absorber, newly-increased second absorber, newly-increased condenser, newly-increased evaporimeter, newly-increased choke valve, newly-increased solution pump, newly-increased second solution pump, newly-increased solution heat exchanger, newly-increased heat exchanger, newly-increased circulating pump, newly-increased second condenser, newly-increased second throttle, new solubilization liquid choke valve, newly-increased second solution choke valve and newly-increased point steam chest, newly-increased absorber (C) has weak solution pipeline to be communicated with newly-increased second absorber (D) with newly-increased solution heat exchanger (J) through newly-increased solution pump (H), newly-increased second absorber (D) also has weak solution pipeline to be communicated with newly-increased second generator (B) through solution choke valve (T), newly-increased second generator (B) also has concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased second solution pump (I), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a newly-increased point steam chest (V) with newly-increased second absorber (D) through newly-increased second solution choke valve (U), newly-increased point steam chest (V) also has concentrated solution pipeline to be communicated with newly-increased absorber (C) through newly-increased solution heat exchanger (J), newly-increased generator (A) also has refrigerant steam channel to be communicated with newly-increased second absorber (D), newly-increased second generator (B) also has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased choke valve (G), newly-increased point steam chest (V) also has refrigerant steam channel to be communicated with newly-increased second condenser (R), newly-increased second condenser (R) also has cryogen liquid pipeline to be communicated with newly-increased evaporimeter (F) through newly-increased second throttle (S), newly-increased evaporimeter (F) also has refrigerant steam channel to be communicated with newly-increased absorber (C), by absorber (5), second absorber (7) and the 5th absorber have heated medium pipeline and ft connection to be adjusted to absorber (5) respectively has circulating thermal medium pipeline to be communicated with the second absorber (7) successively, 5th absorber, newly-increased generator (A), newly-increased second generator (B), newly-increased heat exchanger (L), newly-increased evaporimeter (F) has circulating thermal medium pipeline be communicated with absorber (5) and form closed-loop path with circulating pump (M) after circulating pump (M) again, newly-increased absorber (C), newly-increased condenser (E), newly-increased second condenser (R) and newly-increased heat exchanger (L) also have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.
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