CN104654653A - Combined thermal dynamic system - Google Patents

Combined thermal dynamic system Download PDF

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Publication number
CN104654653A
CN104654653A CN201510043223.0A CN201510043223A CN104654653A CN 104654653 A CN104654653 A CN 104654653A CN 201510043223 A CN201510043223 A CN 201510043223A CN 104654653 A CN104654653 A CN 104654653A
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communicated
generator
absorber
solution
heat exchanger
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CN104654653B (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
    • F25B15/025—Liquid transfer means
    • 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
    • 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
    • F25B2315/00—Sorption refrigeration cycles or details thereof
    • 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

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  • Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)

Abstract

The invention provides a combined thermal dynamic system, which belongs to the technical field of thermal dynamic combination and heat pumps. Power is supplied to a working machine by a power machine, exhaust steam is supplied to a generator and an evaporator by the power machine, middle extraction steam is supplied to a second generator and a heat exchanger by the power machine, the generator is communicated the second generator through a solution pump and a solution heat exchanger, the second generator is communicated with an absorber through a second solution heat exchanger, the absorber is communicated with a second absorber through a second solution pump and the second solution heat exchanger, the second absorber is communicated with the generator through the solution heat exchanger, refrigerant steam is supplied to the second absorber by the second generator, the generator is provided with a refrigerant steam channel which is communicated with a condenser, the condenser is communicated with the evaporator through a refrigerant liquid pump, the evaporator is provided with a refrigerant steam channel which is communicated with the absorber, the condenser is provided with a cooling medium pipeline which is communicated with the outside, and the absorber, the second absorber and the heat exchanger are respectively provided with heated medium pipelines which are communicated with the outside, so as to form the combined thermal dynamic system.

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:
Doing in the thermodynamic cycle device of circulatory mediator with steam, for making engine (steam turbine) have higher internal heat efficiency and increase its property safe and reliable to operation, then requiring that the pressure and temperature of engine steam discharge can not be too low; In the time so in the winter time, environment temperature is lower, and engine exhaust temperature is higher, then the temperature difference of 40 DEG C even higher of will having an appointment therebetween can not be used; Moreover be in the Steam Power Circulation system of representative with Thermal Power Station, although the grade of steam discharge is very low, its thermic load also had is often very abundant, if effectively utilize then significant in addition.
The existing heat for winter heating moves alliance, and also or have the heat of other heat supply purposes to move alliance, 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.
Adopt the 3rd class absorption heat pump principle, make full use of the temperature difference between engine steam discharge and cold environment, and consider that following thermal energy step utilizes principle, and consider making full use of of the temperature difference between steam source and heated medium, heating of 3rd class absorption heat pump heat supply and engine being drawn gas combines, with meet heat demand under different situations and realize heat energy utilization rationalization---this can not only realize effective utilization of the temperature difference, and can reduce or eliminate the operation interval of engine blade at wet-steam region, increase the internal heat efficiency of engine.
The multiple concrete operating mode such as the thermic load that the height of temperature difference size, cold ambient temperature, steam discharge contain owing to relating to heat user thermal parameter and thermic load, between steam discharge and cold environment is how many, therefore needs 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine and working machine, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, the finisher that engine also has exhaust passage to be communicated with generator and evaporimeter successively has condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the second condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second 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 cooling medium pipeline and ft connection, absorber and the second absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, that heat described in the 1st is moved in co-feeding system, cancel evaporimeter, engine is had exhaust passage be communicated with successively generator and the finisher of evaporimeter 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, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up exhaust passage to be communicated with absorber, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine and working machine, 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 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second 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 cooling medium pipeline and ft connection, absorber and the second absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, that heat described in the 3rd is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection, evaporimeter to have refrigerant steam channel to be communicated with absorber to be adjusted in the lump again has the second steam channel to be communicated with absorber in engine, there is by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd 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, the finisher that engine also has exhaust passage to be communicated with the 3rd generator, generator and evaporimeter successively has condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the second condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, 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 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 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 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 and the 3rd absorber also have cooling medium pipeline and ft connection respectively, absorber and the second absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, that heat described in the 5th is moved in co-feeding system, cancel evaporimeter, exhaust passage is had by engine to be communicated with the 3rd generator successively, generator and the finisher of evaporimeter have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with the 3rd generator and generator successively after generator have condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up exhaust passage to be communicated with absorber, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd 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 3rd generator after the 3rd generator have condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with successively, and finisher that generator is communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, 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 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 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 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 and the 3rd absorber also have cooling medium pipeline and ft connection respectively, absorber and the second absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, that heat described in the 7th is moved in co-feeding system, cancel evaporimeter, had by engine the second steam channel to be communicated with successively finisher that generator is communicated with evaporimeter 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, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up the second steam channel to be communicated with absorber, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd 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 3rd generator and generator successively 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 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, 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 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 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 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 and the 3rd absorber also have cooling medium pipeline and ft connection respectively, absorber and the second absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, that heat described in the 9th is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection, evaporimeter to have refrigerant steam channel to be communicated with absorber to be adjusted in the lump again has the second steam channel to be communicated with absorber in engine, there is by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second 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, evaporimeter and the second evaporimeter successively after the second evaporimeter have condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the second condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, that heat described in the 11st is moved in co-feeding system, cancel evaporimeter, exhaust passage is had to be communicated with generator successively in engine, evaporimeter and the second evaporimeter after the second evaporimeter have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with generator and the second evaporimeter successively after the second evaporimeter have condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up exhaust passage to be communicated with absorber, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the 3rd generator and to have cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second 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 and the second evaporimeter successively after the second evaporimeter 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 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, that heat described in the 13rd is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection, evaporimeter to have refrigerant steam channel to be communicated with absorber to be adjusted to engine in the lump again has the second steam channel to be communicated with absorber, there is by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the 3rd generator and to have cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second 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 second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, that heat described in the 15th is moved in co-feeding system, cancel evaporimeter, engine is had the second steam channel be communicated with successively evaporimeter and the second evaporimeter after the second evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine 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, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up the second steam channel to be communicated with absorber, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the 3rd generator and to have cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter, the second cryogen liquid pump and the 4th generator, 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 4th generator after the 4th generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with generator, evaporimeter and the second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 4th generator, 4th generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, 4th generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 18. heat, that heat described in the 17th is moved in co-feeding system, cancel evaporimeter, the second steam channel is had by engine to be communicated with generator successively, evaporimeter and the second evaporimeter after the second evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator and the second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up the second steam channel to be communicated with absorber, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the 3rd generator and to have cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, the finisher that engine also has exhaust passage to be communicated with generator and evaporimeter successively has condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the second condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd 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 the 3rd absorber with absorber respectively, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, that heat described in the 19th is moved in co-feeding system, cancel evaporimeter, had by engine exhaust passage to be communicated with generator and the finisher of evaporimeter successively to have condensate liquid pipeline and ft connection to be adjusted to generator after exhaust passage is communicated with generator again to have condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine to set up exhaust passage to be communicated with the 3rd absorber with absorber respectively, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the 3rd generator and to have cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second 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, 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 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd 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 the 3rd absorber with absorber respectively, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 22. heat, that heat described in the 21st is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine in the lump has the second steam channel to be communicated with the 3rd absorber with absorber respectively, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the 3rd generator and to have cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump and the 4th generator, 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 4th generator after the 4th generator have condensate liquid pipeline and ft connection again, the finisher that engine also has the second steam channel to be communicated with generator and evaporimeter successively has the second condensate liquid pipeline and ft connection again, engine also has the 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the second solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, 3rd generator also has concentrated solution pipeline to be communicated with the 4th generator, 4th generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, 4th 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 the 3rd absorber with absorber respectively, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, that heat described in the 23rd is moved in co-feeding system, cancel evaporimeter, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter 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, had by evaporimeter refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine to set up the second steam channel to be communicated with the 3rd absorber with absorber respectively, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the 3rd generator and to have cryogen liquid pipeline through the second cryogen liquid pump and ft connection, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 25. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, the finisher that engine also has exhaust passage to be communicated with generator and evaporimeter successively has condensate liquid pipeline and ft connection again, engine also has the second steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the second condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second generator with the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the 3rd solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with the 4th absorber with the 4th solution heat exchanger through the 3rd solution pump, 4th absorber also has weak solution pipeline to be communicated with generator with solution heat exchanger through the 4th solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second 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 the 3rd absorber with absorber respectively, condenser also has cryogen liquid pipeline the 3rd absorber after the second cryogen liquid pump is communicated with the 3rd absorber to have refrigerant steam channel to be communicated with the 4th absorber again, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 4th absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, that heat described in the 25th is moved in co-feeding system, cancel evaporimeter, engine is had exhaust passage be communicated with successively generator and the finisher of evaporimeter 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, had by evaporimeter refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine to set up exhaust passage to be communicated with the 3rd absorber with absorber respectively, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th 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 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second generator with the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the 3rd solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with the 4th absorber with the 4th solution heat exchanger through the 3rd solution pump, 4th absorber also has weak solution pipeline to be communicated with generator with solution heat exchanger through the 4th solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second 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 the 3rd absorber with absorber respectively, condenser also has cryogen liquid pipeline the 3rd absorber after the second cryogen liquid pump is communicated with the 3rd absorber to have refrigerant steam channel to be communicated with the 4th absorber again, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 4th absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, that heat described in the 27th is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection, evaporimeter to have refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine in the lump again has the second steam channel to be communicated with the 3rd absorber with absorber respectively, there is by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 29. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter, the second cryogen liquid pump, the 4th absorber, the 4th 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 generator and the second evaporimeter successively after the second evaporimeter 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 3rd steam channel to be communicated with the second generator and heat exchanger successively, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline through solution pump, solution heat exchanger is communicated with the second generator with the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber with the 3rd solution heat exchanger through the second solution pump, second absorber also has weak solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, 3rd absorber also has weak solution pipeline to be communicated with the 4th absorber with the 4th solution heat exchanger through the 3rd solution pump, 4th absorber also has weak solution pipeline to be communicated with generator with solution heat exchanger through the 4th solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second 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 the 3rd absorber after the second cryogen liquid pump is communicated with the 3rd absorber to have refrigerant steam channel to be communicated with the 4th absorber again, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through the 3rd cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser also has cooling medium pipeline and ft connection, absorber, second absorber and the 4th absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, that heat described in the 29th is moved in co-feeding system, cancel evaporimeter and the second evaporimeter, the finisher being had by engine the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to engine in the lump has the second steam channel to be communicated with absorber, engine is had exhaust passage be communicated with successively generator and the second evaporimeter after the second evaporimeter have again cryogen liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with generator after generator have cryogen liquid pipeline and ft connection again, had by second evaporimeter refrigerant steam channel to be communicated with the 3rd absorber to be adjusted to engine to set up exhaust passage to be communicated with the 3rd absorber, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, had by condenser cryogen liquid pipeline to be communicated with the second evaporimeter through the 3rd cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through the 3rd cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, that arbitrary heat described in 1-2,5-6,11-12,19-20,25-26 item is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger, engine is had the second steam channel be communicated with successively the second generator and heat exchanger, heat exchanger have the second condensate liquid pipeline and ft connection be adjusted in the lump engine 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, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, that arbitrary heat described in 3-4,7-10,13-18,21-24,27-29 item is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger, engine is had the 3rd steam channel be communicated with successively the second generator and heat exchanger, heat exchanger have the 3rd condensate liquid pipeline and ft connection be adjusted in the lump engine have the 3rd steam channel be communicated with the second generator after the second generator have the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
Feature of the present invention and essence is further illustrated below in conjunction with the dynamic co-feeding system of heat shown in Fig. 4 and Fig. 8:
(1) between steam discharge and cold environment, the temperature difference is less, and when exhaust steam flow is larger, adopts the dynamic co-feeding system of heat shown in Fig. 4, and classification realizes the rising of part steam discharge heat quality.
(2) between steam discharge and cold environment, the temperature difference is larger, cold ambient temperature is lower, single solution is adopted to be difficult to fully to realize the temperature difference when utilizing, adopt the dynamic co-feeding system of heat shown in Fig. 8, realize the rising making full use of (economic benefits and social benefits) and another part steam discharge heat quality of part steam discharge heat energy along separate routes.
(3) second generators 2 are to the second absorber 4 heat release, and the externally heat supply of the second absorber 4 is the utilization to the temperature difference between the second steam and heated medium, are conducive to the utilization ratio improving high-grade heat energy.
(4) in practical application, install flow control valve additional at the second steam channel, and change the thermic load of heat exchanger 12---such as reduce to flow through the heated medium flow of heat exchanger 12, actual condition change and energy-conservation needs can be met.
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.
In figure, 1-generator, 2-second generator, 3-absorber, 4-second absorber, 5-condenser, 6-evaporimeter, 7-solution pump, 8-second solution pump, 9-cryogen liquid pump, 10-solution heat exchanger, 11-second solution heat exchanger, 12-heat exchanger, 13-engine, 14-working machine, 15-the 3rd generator, 16-the 3rd absorber, 17-the 3rd solution pump, 18-the 3rd solution heat exchanger, 19-second evaporimeter, 20-second cryogen liquid pump, 21-the 4th generator, 22-the 4th absorber, 23-the 4th solution heat exchanger, 24-the 3rd cryogen liquid pump.
Here also following explanation to be provided:
(1) steam discharge---refer to engine export medium, as the low-pressure steam in steam turbine outlet moist steam.
(2) second steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of steam discharge.
(3) 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) relevant with engine, but do not relate to operation principle of the present invention, the parts (as power output part etc.) irrelevant with content of the present invention and flow process (as dynamical system backheat flow process), not in express ranges of the present invention.
(5) for Fig. 8, the circulation be made up of the 3rd generator 15, the 3rd absorber 16, condenser 5, second evaporimeter 19, the 3rd solution pump 17, cryogen liquid pump 9 and the 3rd solution heat exchanger 18, when making working medium with ammonia-aqueous solution, 3rd generator is referred to as rectifying column by custom---and now as required, the 3rd generator 15 sets up cooling medium pipeline and ft connection.
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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine and working machine, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also has exhaust passage and ft connection, the finisher 6 that engine 13 also has exhaust passage to be communicated with generator 1 and evaporimeter 6 successively has condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the second condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 also has cooling medium pipeline and ft connection, absorber 3 and the second absorber 4 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the second steam to the second generator 2 and heat exchanger 12, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with heat exchanger 12, progressively heat release through the second generator 2, engine 13 provides steam discharge to generator 1 and evaporimeter 6, and steam discharge flows through generator 1 and becomes with evaporimeter 6, progressively heat release after condensate liquid and discharge through condensate line road, the concentrated solution of generator 1 enters the second generator 2 through solution pump 7 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 4 enters generator 1 after solution heat exchanger 10 and pipeline step-down, heat absorption release refrigerant vapour also provides to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine and working machine, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with generator 1 after generator 1 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 also has cooling medium pipeline and ft connection, absorber 3 and the second absorber 4 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Fig. 1, main difference part is: engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12,3rd vapor stream becomes after condensate liquid through the 3rd condensate liquid pipeline discharge with heat exchanger 12, progressively heat release through the second generator 2, engine 13 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 13 only provides steam discharge to generator 1.
Heat shown in Fig. 3 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 2, cancel evaporimeter, the finisher 6 being had by engine 13 second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection, evaporimeter 6 to have refrigerant steam channel to be communicated with absorber 3 to be adjusted in the lump and to have the second steam channel to be communicated with absorber 3 in engine 13 again, there is by condenser 5 cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9 to be adjusted to condenser 5 and to have cryogen liquid pipeline through cryogen liquid pump 9 and ft connection, form the dynamic co-feeding system of heat.
Heat shown in Fig. 4 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 13 connects working machine 14, the finisher 6 that engine 13 also has exhaust passage to be communicated with the 3rd generator 15, generator 1 and evaporimeter 6 successively has condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the second condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with the 3rd absorber 16, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 and the 3rd absorber 16 also have cooling medium pipeline and ft connection respectively, absorber 3 and the second absorber 4 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the second steam to the second generator 2 and heat exchanger 12, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with heat exchanger 12, progressively heat release through the second generator 2, engine 13 provides steam discharge to the 3rd generator 15, generator 1 and evaporimeter 6, part or all of steam discharge flow through the 3rd generator 15, generator 1 and evaporimeter 6 progressively heat release discharge through condensate line road after becoming condensate liquid, the concentrated solution of generator 1 enters the second generator 2 through solution pump 7 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 4 enters generator 1 through solution heat exchanger 10, heat absorption release refrigerant vapour also provides to the 3rd absorber 16, the weak solution of the 3rd absorber 16 enters the 3rd generator 15, heat absorption release refrigerant vapour providing to condenser 5 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, the concentrated solution of the 3rd generator 15 enters the 3rd absorber 16 through the 3rd solution heat exchanger 18, absorb refrigerant vapour and heat release in cooling medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 5 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 4, cancel evaporimeter, exhaust passage is had by engine 13 to be communicated with the 3rd generator 15 successively, generator 1 and the finisher 6 of evaporimeter 6 have again condensate liquid pipeline and ft connection be adjusted to engine 13 have exhaust passage be communicated with the 3rd generator 15 and generator 1 successively after generator 1 have condensate liquid pipeline and ft connection again, had by evaporimeter 6 refrigerant steam channel to be communicated with absorber 3 to be adjusted to engine 13 to set up exhaust passage to be communicated with absorber 3, had by condenser 5 cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9 to be adjusted to condenser 5 and to have cryogen liquid pipeline through cryogen liquid pump 9 and ft connection, form the dynamic co-feeding system of heat.
Heat shown in Fig. 6 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the 3rd generator 15 after the 3rd generator 15 have condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with successively, and finisher 6 that generator 1 is communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with the 3rd absorber 16, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 and the 3rd absorber 16 also have cooling medium pipeline and ft connection respectively, absorber 3 and the second absorber 4 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Fig. 4, difference is: engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream is through generator 1 and evaporimeter 6, progressively heat release is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 13 only provides steam discharge to the 3rd generator 15, part or all of steam discharge flows through the 3rd generator 15, heat release is discharged through condensate line road after becoming condensate liquid.
Heat shown in Fig. 7 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the 3rd generator 15 and generator 1 successively after generator 1 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with the 3rd absorber 16, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 and the 3rd absorber 16 also have cooling medium pipeline and ft connection respectively, absorber 3 and the second absorber 4 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Fig. 4, difference is: engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 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, engine 13 provides steam discharge to the 3rd generator 15 and generator 1, part or all of steam discharge flows through the 3rd generator 15 and generator 1, progressively heat release is discharged through condensate line road after becoming condensate liquid.
Heat shown in Fig. 8 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also has exhaust passage to be communicated with the second evaporimeter 19 after generator 1, evaporimeter 6 and the second evaporimeter 19 successively and has condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the second condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 15 after the 3rd generator 15 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 again, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 19 through cryogen liquid pump 9, second evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 16, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the second steam to the second generator 2 and heat exchanger 12, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with heat exchanger 12, progressively heat release through the second generator 2, engine 13 provides steam discharge to generator 1 and evaporimeter 6, and part or all of steam discharge flows through generator 1 and becomes with evaporimeter 6, progressively heat release after condensate liquid and discharge through condensate line road, the concentrated solution of generator 1 enters the second generator 2 through solution pump 7 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 4 enters generator 1 through solution heat exchanger 10, heat absorption release refrigerant vapour is also supplied to the 3rd generator 15 do driving thermal medium, the concentrated solution of the 3rd generator 15 enters the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 16 enters the 3rd generator 15 through the 3rd solution heat exchanger 18, refrigerant vapour flows through the 3rd generator 15, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters the second evaporimeter 19 through cryogen liquid pump 9 pressurization, absorb heat into refrigerant vapour and provide to the 3rd absorber 16, the refrigerant vapour heat release flowing through the 3rd generator 15 enters evaporimeter 6 through the second cryogen liquid pump 20 pressurization after becoming cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 3, form the dynamic co-feeding system of heat.
Heat shown in Fig. 9 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 8, cancel evaporimeter, exhaust passage is had to be communicated with generator 1 successively in engine 13, after evaporimeter 6 and the second evaporimeter 19 second evaporimeter 19 have again condensate liquid pipeline and ft connection be adjusted to engine 13 have exhaust passage be communicated with successively generator 1 and the second evaporimeter 19 afterwards the second evaporimeter 19 have condensate liquid pipeline and ft connection again, had by evaporimeter 6 refrigerant steam channel to be communicated with absorber 3 to be adjusted to engine 13 to set up exhaust passage to be communicated with absorber 3, had by 3rd generator 15 cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 to be adjusted to the 3rd generator 15 and to have cryogen liquid pipeline through the second cryogen liquid pump 20 and ft connection, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with generator 1 and the second evaporimeter 19 successively after the second evaporimeter 19 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 15 after the 3rd generator 15 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 again, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 19 through cryogen liquid pump 9, second evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 16, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Fig. 8, difference is: engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 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, engine 13 provides steam discharge to generator 1 and the second evaporimeter 19, part or all of steam discharge flows through generator 1 and the second evaporimeter 19, progressively heat release is discharged through condensate line road after becoming condensate liquid.
Heat shown in Figure 11 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with generator 1 after generator 1 have condensate liquid pipeline and ft connection again, engine 13 also have the second steam channel be communicated with evaporimeter 6 and the second evaporimeter 19 successively after the second evaporimeter 19 have the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 15 after the 3rd generator 15 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 again, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 19 through cryogen liquid pump 9, second evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 16, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Fig. 8, difference is: engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 provides the second steam to evaporimeter 6 and the second evaporimeter 19, second vapor stream is through evaporimeter 6 and the second evaporimeter 19, progressively heat release is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 13 provides steam discharge to generator 1, part or all of steam discharge flows through generator 1, heat release is discharged through condensate line road 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 11, cancel evaporimeter, engine 13 is had the second steam channel be communicated with evaporimeter 6 and the second evaporimeter 19 successively after the second evaporimeter 19 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel be communicated with the second evaporimeter 19 after the second evaporimeter 19 have the second condensate liquid pipeline and ft connection again, had by evaporimeter 6 refrigerant steam channel to be communicated with absorber 3 to be adjusted to engine 13 to set up the second steam channel to be communicated with absorber 3, had by 3rd generator 15 cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 to be adjusted to the 3rd generator 15 and to have cryogen liquid pipeline through the second cryogen liquid pump 20 and ft connection, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter, the second cryogen liquid pump and the 4th generator, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the 4th generator 21 after the 4th generator 21 have condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second evaporimeter 19 after generator 1, evaporimeter 6 and the second evaporimeter 19 successively and has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 15 after the 3rd generator 15 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 again, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 4th generator 21, 4th generator 21 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, 4th generator 21 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 19 through cryogen liquid pump 9, second evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 16, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 is to generator 1, evaporimeter 6 and the second evaporimeter 19 provide the second steam, second vapor stream is through generator 1, evaporimeter 6 and the second evaporimeter 19 progressively heat release are discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 13 provides steam discharge to the 4th generator 21, part or all of steam discharge flows through the 4th generator 21, heat release is discharged through condensate line road after becoming condensate liquid, the concentrated solution of generator 1 enters the second generator 2 through solution pump 7 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 4 enters generator 1 through solution heat exchanger 10, heat absorption release refrigerant vapour is also supplied to the 3rd generator 15 do driving thermal medium, the concentrated solution of the 3rd generator 15 enters the 4th generator 21, heat absorption release refrigerant vapour also provides to condenser 5, the concentrated solution of the 4th generator 21 enters the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 16 enters the 3rd generator 15 through the 3rd solution heat exchanger 18, refrigerant vapour flows through the 3rd generator 15, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters the second evaporimeter 19 through cryogen liquid pump 9 pressurization, absorb heat into refrigerant vapour and provide to the 3rd absorber 16, the refrigerant vapour heat release flowing through the 3rd generator 15 enters evaporimeter 6 through the second cryogen liquid pump 20 pressurization after becoming cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 3, form the dynamic co-feeding system of heat.
Heat shown in Figure 14 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, the finisher 6 that engine 13 also has exhaust passage to be communicated with generator 1 and evaporimeter 6 successively has condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the second condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 15 after the 3rd generator 15 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 again, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 16 with absorber 3 respectively, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the second steam to the second generator 2 and heat exchanger 12, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with heat exchanger 12, progressively heat release through the second generator 2, engine 13 provides steam discharge to generator 1 and evaporimeter 6, and steam discharge flows through generator 1 and becomes with evaporimeter 6, progressively heat release after condensate liquid and discharge through condensate line road, the concentrated solution of generator 1 enters the second generator 2 through solution pump 7 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 4 enters generator 1 through solution heat exchanger 10, heat absorption release refrigerant vapour is also supplied to the 3rd generator 15 do driving thermal medium, the concentrated solution of the 3rd generator 15 enters the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 16 enters the 3rd generator 15 through the 3rd solution heat exchanger 18, refrigerant vapour flows through the 3rd generator 15, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, the refrigerant vapour heat release flowing through the 3rd generator 15 enters evaporimeter 6 through the second cryogen liquid pump 20 pressurization after becoming cryogen liquid, the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour and provides respectively to absorber 3 and the 3rd absorber 16, form the dynamic co-feeding system of heat.
Heat shown in Figure 15 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with generator 1 after generator 1 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 15 after the 3rd generator 15 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 again, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 16 with absorber 3 respectively, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Figure 14, difference is: engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 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, engine 13 provides steam discharge to generator 1, part or all of steam discharge flows through generator 1, heat release is discharged through condensate line road after becoming condensate liquid.
Heat shown in Figure 16 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump and the 4th generator, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the 4th generator 21 after the 4th generator 21 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with generator 1 and evaporimeter 6 successively has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with solution heat exchanger 10 through solution pump 7, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the second solution heat exchanger 11 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 15 after the 3rd generator 15 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 20 again, 3rd generator 15 also has concentrated solution pipeline to be communicated with the 4th generator 21, 4th generator 21 also has concentrated solution pipeline to be communicated with the 3rd absorber 16 with the 3rd solution heat exchanger 18 through the 3rd solution pump 17, 3rd absorber 16 also has weak solution pipeline to be communicated with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be communicated with condenser 5, 4th generator 21 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 16 with absorber 3 respectively, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream is through generator 1 and evaporimeter 6, progressively heat release is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 13 provides steam discharge to the 4th generator 11, part or all of steam discharge flows through the 4th generator 21, heat release is discharged through condensate line road after becoming condensate liquid, the concentrated solution of generator 1 enters the second generator 2 through solution pump 7 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 4 enters generator 1 through solution heat exchanger 10, heat absorption release refrigerant vapour is also supplied to the 3rd generator 15 do driving thermal medium, the concentrated solution of the 3rd generator 15 enters the 4th generator 21, heat absorption release refrigerant vapour also provides to condenser 5, the concentrated solution of the 4th generator 21 enters the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 16 enters the 3rd generator 15 through the 3rd solution heat exchanger 18, refrigerant vapour flows through the 3rd generator 15, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, the refrigerant vapour heat release flowing through the 3rd generator 15 enters evaporimeter 6 through the second cryogen liquid pump 20 pressurization after becoming cryogen liquid, the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour and provides respectively to absorber 3 and the 3rd absorber 16, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat exchanger, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, the finisher 6 that engine 13 also has exhaust passage to be communicated with generator 1 and evaporimeter 6 successively has condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the second condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline through solution pump 7, solution heat exchanger 10 is communicated with the second generator 2 with the second solution heat exchanger 11, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the 3rd solution heat exchanger 18 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with the 3rd absorber 16 through the 3rd solution heat exchanger 18, 3rd absorber 16 also has weak solution pipeline to be communicated with the 4th absorber 22 with the 4th solution heat exchanger 23 through the 3rd solution pump 17, 4th absorber 22 also has weak solution pipeline to be communicated with generator 1 with solution heat exchanger 10 through the 4th solution heat exchanger 23, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 16 with absorber 3 respectively, condenser 5 also has cryogen liquid pipeline the 3rd absorber 16 after the second cryogen liquid pump 20 is communicated with the 3rd absorber 16 to have refrigerant steam channel to be communicated with the 4th absorber 22 again, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 4th absorber 22 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the second steam to the second generator 2 and heat exchanger 12, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with heat exchanger 12, progressively heat release through the second generator 2, engine 13 provides steam discharge to generator 1 and evaporimeter 6, and part or all of steam discharge flows through generator 1 and becomes with evaporimeter 6, progressively heat release after condensate liquid and discharge through condensate line road, the concentrated solution of generator 1 is through solution pump 7, solution heat exchanger 10 and the second solution heat exchanger 11 enter the second generator 2, concentrated solution is absorbed heat and is discharged refrigerant vapour and provide to the second absorber 4 in the second generator 2, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution pipeline of absorber 3 enters the second absorber 4 through the second solution pump 8 and the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in heated medium, the weak solution pipeline of the second absorber 4 enters the 3rd absorber 16 through the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in cryogen liquid, the weak solution of the 3rd absorber 16 enters the 4th absorber 22 through the 3rd solution pump 17 and the 4th solution heat exchanger 23, absorb refrigerant vapour heat release in heated medium, the weak solution of the 4th absorber 22 enters generator 1 through the 4th solution heat exchanger 23 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 is divided into two-way---and the first via enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide respectively to absorber 3 and the 3rd absorber 16, flow through the 3rd absorber 16 after second tunnel second cryogen liquid pump 20 pressurizes, absorb heat into refrigerant vapour and provide to the 4th absorber 22, form the dynamic co-feeding system of heat.
Heat shown in Figure 18 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat exchanger, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with generator 1 after generator 1 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline through solution pump 7, solution heat exchanger 10 is communicated with the second generator 2 with the second solution heat exchanger 11, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the 3rd solution heat exchanger 18 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with the 3rd absorber 16 through the 3rd solution heat exchanger 18, 3rd absorber 16 also has weak solution pipeline to be communicated with the 4th absorber 22 with the 4th solution heat exchanger 23 through the 3rd solution pump 17, 4th absorber 22 also has weak solution pipeline to be communicated with generator 1 with solution heat exchanger 10 through the 4th solution heat exchanger 23, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 16 with absorber 3 respectively, condenser 5 also has cryogen liquid pipeline the 3rd absorber 16 after the second cryogen liquid pump 20 is communicated with the 3rd absorber 16 to have refrigerant steam channel to be communicated with the 4th absorber 22 again, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 4th absorber 22 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Figure 17, difference is: engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 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, engine 13 provides steam discharge to generator 1, part or all of steam discharge flows through generator 1, heat release is discharged through condensate line road after becoming condensate liquid.
Heat shown in Figure 19 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter, the second cryogen liquid pump, the 4th absorber, the 4th solution heat exchanger and the 3rd cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with generator 1 and the second evaporimeter 19 successively after the second evaporimeter 19 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd steam channel to be communicated with the second generator 2 and heat exchanger 12 successively, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection, generator 1 also has concentrated solution pipeline through solution pump 7, solution heat exchanger 10 is communicated with the second generator 2 with the second solution heat exchanger 11, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 with the 3rd solution heat exchanger 18 through the second solution pump 8, second absorber 4 also has weak solution pipeline to be communicated with the 3rd absorber 16 through the 3rd solution heat exchanger 18, 3rd absorber 16 also has weak solution pipeline to be communicated with the 4th absorber 22 with the 4th solution heat exchanger 23 through the 3rd solution pump 17, 4th absorber 22 also has weak solution pipeline to be communicated with generator 1 with solution heat exchanger 10 through the 4th solution heat exchanger 23, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 also has cryogen liquid pipeline the 3rd absorber 16 after the second cryogen liquid pump 20 is communicated with the 3rd absorber 16 to have refrigerant steam channel to be communicated with the 4th absorber 22 again, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 19 through the 3rd cryogen liquid pump 24, second evaporimeter 19 also has refrigerant steam channel to be communicated with the 3rd absorber 16, condenser 5 also has cooling medium pipeline and ft connection, absorber 3, second absorber 4 and the 4th absorber 22 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 provides the 3rd steam to the second generator 2 and heat exchanger 12, 3rd vapor stream is through the second generator 2 and heat exchanger 12, progressively heat release is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 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, engine 13 provides steam discharge to generator 1 and the second evaporimeter 19, part or all of steam discharge flows through generator 1 and the second evaporimeter 19, progressively heat release is discharged through condensate line road after becoming condensate liquid, the concentrated solution of generator 1 is through solution pump 7, solution heat exchanger 10 and the second solution heat exchanger 11 enter the second generator 2, concentrated solution is absorbed heat and is discharged refrigerant vapour and provide to the second absorber 4 in the second generator 2, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution pipeline of absorber 3 enters the second absorber 4 through the second solution pump 8 and the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in heated medium, the weak solution pipeline of the second absorber 4 enters the 3rd absorber 16 through the 3rd solution heat exchanger 18, absorb refrigerant vapour heat release in cryogen liquid, the weak solution of the 3rd absorber 16 enters the 4th absorber 22 through the 3rd solution pump 17 and the 4th solution heat exchanger 23, absorb refrigerant vapour heat release in heated medium, the weak solution of the 4th absorber 22 enters generator 1 through the 4th solution heat exchanger 23 and solution heat exchanger 10, heat absorption release refrigerant vapour also provides to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 is divided into three tunnels---and the first via enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, flow through the 3rd absorber 16 after second tunnel second cryogen liquid pump 20 pressurizes, absorb heat into refrigerant vapour and provide to the 4th absorber 22,3rd tunnel the 3rd cryogen liquid pump 24 pressurization enters the second evaporimeter 19, absorbs heat into refrigerant vapour and provide to the 3rd absorber 16, forms the dynamic co-feeding system of heat.
The effect that the technology of the present invention can realize---heat proposed by the invention is moved co-feeding system and is had following effect and advantage:
(1) temperature difference between engine steam discharge and cold environment is utilized, and realizes the rationalization of total system heat energy utilization.
(2) the first work done (generating) of high-grade steam, for heat supply after grade reduces, meets thermal energy step and utilizes principle.
(3) farthest reduce the heat transfer temperature difference between thermal source and heated medium, improve utilization efficiency of heat energy.
(4) provide multiple concrete technical scheme, numerous different actual state can be tackled, have the wider scope of application.
(5) steam discharge and engine intermediate extraction combine as the thermal source of absorption heat pump flow process, for meeting different user and duty requirements brings flexibility.
(6) during variable working condition, can preferentially adopt the 3rd class absorption heat pump for thermal flow process, the thermic load of heat exchanger has and regulates visible, which ensure that the efficient and flexible of system.
(7) there is the double dominant of extraction for heat supply and condensing heat supply, avoid the impact of heating demand change on work done (generating) largely.
(8) enriched the type of hot dynamic co-feeding system, extended the range of application of the 3rd class absorption heat pump, be conducive to adopting the 3rd class absorption heat pump to realize making full use of of the temperature difference better.

Claims (32)

1. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine and working machine; Engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, the finisher (6) that engine (13) also has exhaust passage to be communicated with generator (1) and evaporimeter (6) successively has condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, and heat exchanger (12) also has the second condensate liquid pipeline and ft connection; generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) also has cooling medium pipeline and ft connection, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 1, cancel evaporimeter, engine (13) is had exhaust passage be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with generator (1) after generator (1) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up exhaust passage to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine and working machine, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with generator (1) after generator (1) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) also has cooling medium pipeline and ft connection, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, 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 3, cancel evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted in the lump and to have the second steam channel to be communicated with absorber (3) in engine (13), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also has exhaust passage to be communicated with the 3rd generator (15) successively, the finisher (6) of generator (1) and evaporimeter (6) has condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the second condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with the 3rd absorber (16), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) and the 3rd absorber (16) also have cooling medium pipeline and ft connection respectively, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 5, cancel evaporimeter, exhaust passage is had by engine (13) to be communicated with the 3rd generator (15) successively, generator (1) and the finisher (6) of evaporimeter (6) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with the 3rd generator (15) and generator (1) successively after generator (1) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up exhaust passage to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the 3rd generator (15) after the 3rd generator (15) have condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with the finisher (6) that generator (1) is communicated with evaporimeter (6) successively and has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with the 3rd absorber (16), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) and the 3rd absorber (16) also have cooling medium pipeline and ft connection respectively, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, 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 7, cancel evaporimeter, had by engine (13) the second steam channel to be communicated with successively finisher (6) that generator (1) is communicated with evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with successively the 3rd generator (15) and generator (1) afterwards generator (1) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with the 3rd absorber (16), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) and the 3rd absorber (16) also have cooling medium pipeline and ft connection respectively, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 9, cancel evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted in the lump and to have the second steam channel to be communicated with absorber (3) in engine (13), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also has exhaust passage to be communicated with generator (1) successively, evaporimeter (6) and the second evaporimeter (19) afterwards the second evaporimeter (19) have condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the second condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (15) after the 3rd generator (15) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) again, evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (19) through cryogen liquid pump (9), second evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (16), condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, move in co-feeding system in heat according to claim 11, cancel evaporimeter, exhaust passage is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second evaporimeter (19) the second evaporimeter (19) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with successively generator (1) and the second evaporimeter (19) afterwards the second evaporimeter (19) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up exhaust passage to be communicated with absorber (3), had by 3rd generator (15) cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and to have cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with successively generator (1) and the second evaporimeter (19) afterwards the second evaporimeter (19) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (15) after the 3rd generator (15) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) again, evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (19) through cryogen liquid pump (9), second evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (16), condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, move in co-feeding system in heat according to claim 13, cancel evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the second steam channel to be communicated with absorber (3), had by 3rd generator (15) cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and to have cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with generator (1) after generator (1) have condensate liquid pipeline and ft connection again, engine (13) also have the second steam channel be communicated with successively evaporimeter (6) and the second evaporimeter (19) afterwards the second evaporimeter (19) have the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (15) after the 3rd generator (15) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) again, evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (19) through cryogen liquid pump (9), second evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (16), condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, 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 15, cancel evaporimeter, engine (13) is had the second steam channel be communicated with evaporimeter (6) and the second evaporimeter (19) successively after the second evaporimeter (19) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with the second evaporimeter (19) after the second evaporimeter (19) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), had by 3rd generator (15) cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and to have cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter, the second cryogen liquid pump and the 4th generator, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the 4th generator (21) after the 4th generator (21) have condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with generator (1) successively, evaporimeter (6) and the second evaporimeter (19) afterwards the second evaporimeter (19) have the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (15) after the 3rd generator (15) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) again, evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (15) also has concentrated solution pipeline to be communicated with the 4th generator (21), 4th generator (21) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), 4th generator (21) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (19) through cryogen liquid pump (9), second evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (16), condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 18. heat, move in co-feeding system in heat according to claim 17, cancel evaporimeter, the second steam channel is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second evaporimeter (19) the second evaporimeter (19) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with successively generator (1) and the second evaporimeter (19) afterwards the second evaporimeter (19) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), had by 3rd generator (15) cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and to have cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, the finisher (6) that engine (13) also has exhaust passage to be communicated with generator (1) and evaporimeter (6) successively has condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, and heat exchanger (12) also has the second condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (15) after the 3rd generator (15) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) again, 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, 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 19, cancel evaporimeter, had by engine (13) exhaust passage to be communicated with generator (1) and the finisher (6) of evaporimeter (6) successively to have condensate liquid pipeline and ft connection to be adjusted to generator (1) after exhaust passage is communicated with generator (1) again to have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) to be respectively adjusted to engine (13) to set up exhaust passage to be communicated with the 3rd absorber (16) with absorber (3) respectively, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, had by 3rd generator (15) cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and to have cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with generator (1) after generator (1) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (15) after the 3rd generator (15) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) again, 3rd generator (15) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 22. heat, move in co-feeding system in heat according to claim 21, cancel evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) to be respectively adjusted to engine (13) in the lump has the second steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, had by 3rd generator (15) cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and to have cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump and the 4th generator, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the 4th generator (21) after the 4th generator (21) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with generator (1) and evaporimeter (6) successively has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with solution heat exchanger (10) through solution pump (7), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the second solution heat exchanger (11) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (15) after the 3rd generator (15) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) again, 3rd generator (15) also has concentrated solution pipeline to be communicated with the 4th generator (21), 4th generator (21) also has concentrated solution pipeline to be communicated with the 3rd absorber (16) with the 3rd solution heat exchanger (18) through the 3rd solution pump (17), 3rd absorber (16) also has weak solution pipeline to be communicated with the 3rd generator (15) through the 3rd solution heat exchanger (18), 3rd generator (15) also has refrigerant steam channel to be communicated with condenser (5), 4th generator (21) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, 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 23, cancel evaporimeter, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) to be respectively adjusted to engine (13) to set up the second steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, had by 3rd generator (15) cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and to have cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 25. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat exchanger; Engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, the finisher (6) that engine (13) also has exhaust passage to be communicated with generator (1) and evaporimeter (6) successively has condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, and heat exchanger (12) also has the second condensate liquid pipeline and ft connection; generator (1) also has concentrated solution pipeline through solution pump (7), solution heat exchanger (10) is communicated with the second generator (2) with the second solution heat exchanger (11), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the 3rd solution heat exchanger (18) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with the 3rd absorber (16) through the 3rd solution heat exchanger (18), 3rd absorber (16) also has weak solution pipeline to be communicated with the 4th absorber (22) with the 4th solution heat exchanger (23) through the 3rd solution pump (17), 4th absorber (22) also has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (10) through the 4th solution heat exchanger (23), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, condenser (5) also has cryogen liquid pipeline the 3rd absorber (16) after the second cryogen liquid pump (20) is communicated with the 3rd absorber (16) to have refrigerant steam channel to be communicated with the 4th absorber (22) again, condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 4th absorber (22) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, move in co-feeding system in heat according to claim 25, cancel evaporimeter, engine (13) is had exhaust passage be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with generator (1) after generator (1) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) to be respectively adjusted to engine (13) to set up exhaust passage to be communicated with the 3rd absorber (16) with absorber (3) respectively, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat exchanger, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with generator (1) after generator (1) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline through solution pump (7), solution heat exchanger (10) is communicated with the second generator (2) with the second solution heat exchanger (11), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the 3rd solution heat exchanger (18) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with the 3rd absorber (16) through the 3rd solution heat exchanger (18), 3rd absorber (16) also has weak solution pipeline to be communicated with the 4th absorber (22) with the 4th solution heat exchanger (23) through the 3rd solution pump (17), 4th absorber (22) also has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (10) through the 4th solution heat exchanger (23), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, condenser (5) also has cryogen liquid pipeline the 3rd absorber (16) after the second cryogen liquid pump (20) is communicated with the 3rd absorber (16) to have refrigerant steam channel to be communicated with the 4th absorber (22) again, condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 4th absorber (22) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, 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 27, cancel evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with the 3rd absorber (16) with absorber (3) to be respectively adjusted to engine (13) in the lump has the second steam channel to be communicated with the 3rd absorber (16) with absorber (3) respectively, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 29. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, the second solution heat exchanger, heat exchanger, engine, working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter, the second cryogen liquid pump, the 4th absorber, the 4th solution heat exchanger and the 3rd cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with successively generator (1) and the second evaporimeter (19) afterwards the second evaporimeter (19) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection, generator (1) also has concentrated solution pipeline through solution pump (7), solution heat exchanger (10) is communicated with the second generator (2) with the second solution heat exchanger (11), second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) with the 3rd solution heat exchanger (18) through the second solution pump (8), second absorber (4) also has weak solution pipeline to be communicated with the 3rd absorber (16) through the 3rd solution heat exchanger (18), 3rd absorber (16) also has weak solution pipeline to be communicated with the 4th absorber (22) with the 4th solution heat exchanger (23) through the 3rd solution pump (17), 4th absorber (22) also has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (10) through the 4th solution heat exchanger (23), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) also has cryogen liquid pipeline the 3rd absorber (16) after the second cryogen liquid pump (20) is communicated with the 3rd absorber (16) to have refrigerant steam channel to be communicated with the 4th absorber (22) again, condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the 3rd cryogen liquid pump (24), second evaporimeter (19) also has refrigerant steam channel to be communicated with the 3rd absorber (16), condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second absorber (4) and the 4th absorber (22) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, move in co-feeding system in heat according to claim 29, cancel evaporimeter and the second evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the second steam channel to be communicated with absorber (3), engine (13) is had exhaust passage be communicated with generator (1) and the second evaporimeter (19) successively after the second evaporimeter (19) have again cryogen liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with generator (1) after generator (1) have cryogen liquid pipeline and ft connection again, had by second evaporimeter (19) refrigerant steam channel to be communicated with the 3rd absorber (16) to be adjusted to engine (13) to set up exhaust passage to be communicated with the 3rd absorber (16), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, had by condenser (5) cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the 3rd cryogen liquid pump (24) to be adjusted to condenser (5) and to have cryogen liquid pipeline through the 3rd cryogen liquid pump (24) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, at claim 1-2, 5-6, 11-12, 19-20, arbitrary heat described in 25-26 is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger (12), the second steam channel is had by engine (13) to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) have the second condensate liquid pipeline and ft connection be adjusted in the lump engine (13) have the second steam channel be communicated with the second generator (2) after the second generator (2) have the second condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, at claim 3-4, 7-10, 13-18, 21-24, arbitrary heat described in 27-29 is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger (12), the 3rd steam channel is had by engine (13) to be communicated with the second generator (2) and heat exchanger (12) successively, heat exchanger (12) have the 3rd condensate liquid pipeline and ft connection be adjusted in the lump engine (13) have the 3rd steam channel be communicated with the second generator (2) after the second generator (2) have the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
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