CN104654658A - Combined thermal dynamic system - Google Patents

Combined thermal dynamic system Download PDF

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Publication number
CN104654658A
CN104654658A CN201510043114.9A CN201510043114A CN104654658A CN 104654658 A CN104654658 A CN 104654658A CN 201510043114 A CN201510043114 A CN 201510043114A CN 104654658 A CN104654658 A CN 104654658A
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communicated
absorber
solution
heat exchanger
pipeline
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CN104654658B (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
    • 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
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • 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
    • F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
    • 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

Abstract

The invention provides a combined thermal dynamic system, which belongs to the technical field of thermal dynamic combination and heat pumps. Exhaust steam is supplied to a generation-evaporator by a power machine, second steam is supplied to a heat exchanger by the power machine, a steam separating chamber is communicated with an absorber through a solution pump and a solution heat exchanger, the absorber is communicated with the steam separating chamber through the solution heat exchanger, a solution throttle valve and the generation-evaporator, the steam separating chamber is provided with a refrigerant steam channel which is communicated with a second absorber, the second absorber is communicated with a second steam separating chamber through a second solution pump, a second solution heat exchanger and the generation-evaporator, the second steam separating chamber is communicated with the second absorber through the second solution heat exchanger, the second steam separating chamber is provided with a refrigerant steam channel which is communicated with a condenser, the condenser is communicated with the absorber through a refrigerant liquid pump and the generation-evaporator, the condenser and the second absorber are provided with cooling medium pipelines which are communicated with the outside, and the absorber and the heat exchanger are 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 heat-electricity-cold combined supply 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 outlet exhaust steam can not be too low; In the time so in the winter time, environment temperature is lower, and engine outlet exhaust steam 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 exhaust steam 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 second-kind absorption-type heat pump principle, make full use of the temperature difference between engine exhaust steam and cold environment, and consider that following thermal energy step utilizes principle, heating of second-kind absorption-type 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, exhaust steam contain owing to relating to heat user thermal parameter and thermic load, between exhaust steam and cold environment is how many, and the adaptation of consideration to existing heat power generating system, therefore need 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 generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine and a 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 has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, engine also has the second steam channel to be communicated with heat exchanger, and heat exchanger also has the second condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with generation-evaporimeter, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber again, condenser also has cooling medium pipeline and ft connection, absorber also has heated medium pipeline and ft connection, 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, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up exhaust passage and is communicated with absorber, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator and an evaporimeter, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, 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, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with generator, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cooling medium pipeline and ft connection, absorber also has heated medium pipeline and ft connection, 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 to engine in the lump again has the second steam channel to be communicated with absorber, 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 generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, engine also has the second steam channel to be communicated with heat exchanger, and heat exchanger also has the second condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with generation-evaporimeter, steam chest is divided to also have refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline through the second solution pump, second solution heat exchanger is communicated with second point of steam chest with generation-evaporimeter, second point of steam chest also has concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, second point of steam chest also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber again, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up exhaust passage and is communicated with absorber, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, 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, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with generator, steam chest is divided to also have refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline through the second solution pump, second solution heat exchanger is communicated with second point of steam chest with generator, second point of steam chest also has concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, second point of steam chest 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 second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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, 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 refrigerant steam channel to be communicated with absorber, forms the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, and engine also has the second steam channel to be communicated with generation-evaporimeter, and generation-evaporimeter also has the second condensate liquid pipeline and ft connection, engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with generation-evaporimeter, steam chest is divided to also have refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline through the second solution pump, second solution heat exchanger is communicated with second point of steam chest with generator, second point of steam chest also has concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, second point of steam chest also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber again, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up the second steam channel and is communicated with absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second generator, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, the finisher that engine also has the second steam channel to be communicated with the second generator and evaporimeter successively has the second condensate liquid pipeline and ft connection again, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the second generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline through the second solution pump, second solution heat exchanger is communicated with a point steam chest with generator, steam chest is divided to also have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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, engine is had the second steam channel be communicated with successively the second 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 the second generator after the second 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.
The dynamic co-feeding system of 13. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest and second generator, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, engine also has the second steam channel to be communicated with the second generator, second generator also has the second condensate liquid pipeline and ft connection, the finisher that engine also has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, engine also has the 4th steam channel to be communicated with heat exchanger, heat exchanger also has the 4th condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline through solution heat exchanger, solution choke valve is communicated with a point steam chest with the second generator, steam chest is divided to also have refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline through the second solution pump, second solution heat exchanger is communicated with second point of steam chest with generator, second point of steam chest also has concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, second point of steam chest 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 second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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 3rd steam channel to be communicated with evaporimeter has the 3rd 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 3rd steam channel to be communicated with absorber, 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 15. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second generator, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, engine also have the second steam channel be communicated with the second generator after the second generator have the second condensate liquid pipeline and ft connection again, the finisher that engine also has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, engine also has the 4th steam channel to be communicated with heat exchanger, heat exchanger also has the 4th condensate liquid pipeline and ft connection, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the second generator through solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline through the second solution pump, second solution heat exchanger is communicated with a point steam chest with generator, steam chest is divided to also have concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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, the finisher being had by engine the 3rd steam channel to be communicated with evaporimeter has the 3rd 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 3rd steam channel to be communicated with absorber, 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 17. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump and second point of steam chest, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, engine also has the second steam channel to be communicated with heat exchanger, and heat exchanger also has the second condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the second absorber through solution heat exchanger, second absorber also has weak solution pipeline to be communicated with second point of steam chest with generation-evaporimeter through the second solution pump, second point of steam chest also has concentrated solution pipeline to be communicated with a point steam chest with generation-evaporimeter through solution choke valve, steam chest is divided to also have refrigerant steam channel to be communicated with the second absorber, second point of steam chest also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber again, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up exhaust passage and is communicated with absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, and engine also has the second steam channel generation-evaporimeter to be communicated with, and generation-evaporimeter also has the second condensate liquid pipeline and ft connection, engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the second absorber through solution heat exchanger, second absorber also has weak solution pipeline through the second solution pump, second solution heat exchanger is communicated with second point of steam chest with generation-evaporimeter, second point of steam chest also has concentrated solution pipeline to be communicated with a point steam chest with generator through the second solution heat exchanger, steam chest is divided to also have refrigerant steam channel to be communicated with the second absorber, second point of steam chest also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber again, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, 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, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up the second steam channel and is communicated with absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and a 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 has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, engine also has the second steam channel to be communicated with heat exchanger, and heat exchanger also has the second condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and generation-evaporimeter, point steam chest also have refrigerant steam channel be communicated with generator after generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, the second cryogen liquid pump also have cryogen liquid pipeline be communicated with generation-evaporimeter after occur-evaporimeter has refrigerant steam channel to be communicated with absorber again, generator also has concentrated 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 the second solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the second absorber again, 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.
The dynamic co-feeding system of 22. heat, that heat described in the 21st is moved in co-feeding system, second cryogen liquid pump is had cryogen liquid pipeline be communicated with generation-evaporimeter after occur-evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to the second cryogen liquid pump again cryogen liquid pipeline and ft connection, engine is set up exhaust passage and is communicated with absorber, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, that heat described in the 21st is moved in co-feeding system, second cryogen liquid pump is had cryogen liquid pipeline be communicated with generation-evaporimeter after occur-evaporimeter has refrigerant steam channel to be communicated with absorber to be adjusted to the second cryogen liquid pump again cryogen liquid pipeline and ft connection, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the second absorber to be adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up exhaust passage and is communicated with the second absorber with absorber respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and a 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 has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, 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, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and generation-evaporimeter, point steam chest also have refrigerant steam channel be communicated with generator after 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, generator also has concentrated 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 the second solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the second absorber again, 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.
The dynamic co-feeding system of 25. heat, that heat described in the 24th 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 generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to 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 26. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump and second evaporimeter, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, 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 heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and generator, point steam chest also have refrigerant steam channel be communicated with the second generator after the second 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, second generator also has concentrated 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 the second generator through the second solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser also has cooling medium pipeline and ft connection, 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.
The dynamic co-feeding system of 27. heat, that heat described in the 26th 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 second generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the second 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 28. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump and second evaporimeter, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, the finisher that engine also has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, engine also has the 4th steam channel to be communicated with heat exchanger, heat exchanger also has the 4th condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and generator, point steam chest also have refrigerant steam channel be communicated with the second generator after the second 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, second generator also has concentrated 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 the second generator through the second solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the second absorber, condenser also has cooling medium pipeline and ft connection, 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.
The dynamic co-feeding system of 29. heat, that heat described in the 28th is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the 3rd steam channel to be communicated with evaporimeter has the 3rd 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 3rd steam channel to be communicated with absorber, there is by second generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the second 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 30. heat, primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, divides steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator and the second cryogen liquid pump and formed, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, 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, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with a point steam chest through solution heat exchanger, solution choke valve and generator, divide a steam chest also have refrigerant steam channel be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, second generator also has concentrated 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 the second generator through the second solution heat exchanger, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with the second absorber with absorber respectively, 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.
The dynamic co-feeding system of 31. heat, that heat described in the 30th 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 second absorber with absorber to be respectively adjusted to engine in the lump has the second steam channel to be communicated with the second 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 second generator cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump to be adjusted to the second 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 32. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump and the 3rd absorber, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, engine also has the second steam channel to be communicated with heat exchanger, and heat exchanger also has the second condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the 3rd absorber, 3rd 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 through the second solution heat exchanger, solution heat exchanger, solution choke valve is communicated with a point steam chest with generation-evaporimeter, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber respectively again, 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 second absorber again, 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.
The dynamic co-feeding system of 33. heat, that heat described in the 32nd is moved in co-feeding system, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up exhaust passage and is communicated with the 3rd absorber with absorber respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 34. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump and the 3rd absorber, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, 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, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the 3rd absorber, 3rd 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 through the second solution heat exchanger, solution heat exchanger, solution choke valve is communicated with a point steam chest with generator, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with 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 second absorber again, 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.
The dynamic co-feeding system of 35. heat, that heat described in the 34th 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 36. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump, the 3rd absorber, the 3rd cryogen liquid pump and a second solution choke valve, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, 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, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the 3rd absorber through the second solution choke valve, 3rd 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 through the second solution heat exchanger, solution heat exchanger, solution choke valve is communicated with a point steam chest with generation-evaporimeter, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser also has cryogen liquid pipeline 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 second absorber again, condenser also have cryogen liquid pipeline occur after the 3rd cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber again, 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.
The dynamic co-feeding system of 37. heat, that heat described in the 36th 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 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 38. heat, that heat described in the 36th 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 absorber to be adjusted to engine in the lump has 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, condenser is had cryogen liquid pipeline occur after the 3rd cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber to be adjusted to condenser again has cryogen liquid pipeline through the 3rd cryogen liquid pump and ft connection, engine is set up exhaust passage and is communicated with the 3rd absorber, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th 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 has exhaust passage to be communicated with generation-evaporimeter, generation-evaporimeter also has condensate liquid pipeline and ft connection, engine also has the second steam channel to be communicated with heat exchanger, and heat exchanger also has the second condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the 3rd absorber, 3rd 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 through the second solution heat exchanger, solution heat exchanger, solution choke valve is communicated with a point steam chest with generation-evaporimeter, steam chest is divided to also have refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has weak solution pipeline through the 3rd solution pump, 3rd solution heat exchanger is communicated with second point of steam chest with generation-evaporimeter, second point of steam chest also has concentrated solution pipeline to be communicated with the 4th absorber through the 3rd solution heat exchanger, second point of steam chest also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber respectively again, 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 second absorber again, condenser and the 4th 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.
The dynamic co-feeding system of 40. heat, that heat described in the 39th is moved in co-feeding system, condenser is had cryogen liquid pipeline occur after cryogen liquid pump is communicated with generation-evaporimeter-evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to condenser again has cryogen liquid pipeline through cryogen liquid pump and ft connection, engine is set up exhaust passage and is communicated with the 3rd absorber with absorber respectively, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th 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 has exhaust passage to be communicated with generator, generator also has condensate liquid pipeline and ft connection, 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, and engine also has the 3rd steam channel to be communicated with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, steam chest is divided to have concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the 3rd absorber, 3rd 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 through the second solution heat exchanger, solution heat exchanger, solution choke valve is communicated with a point steam chest with generator, steam chest is divided to also have refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has weak solution pipeline through the 3rd solution pump, 3rd solution heat exchanger is communicated with second point of steam chest with generator, second point of steam chest also has concentrated solution pipeline to be communicated with the 4th absorber through the 3rd solution heat exchanger, second point of steam chest 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 second absorber again, condenser and the 4th 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.
The dynamic co-feeding system of 42. heat, that heat described in the 41st 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 43. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump, the 3rd absorber, the 4th 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 has exhaust passage to be communicated with the second generator, second generator also has condensate liquid pipeline and ft connection, 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 heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the 3rd absorber, 3rd 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 with solution heat exchanger through the second solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has weak solution pipeline through the 3rd solution pump, 3rd solution heat exchanger is communicated with a point steam chest with generator, steam chest is divided to also have concentrated solution pipeline to be communicated with the 4th absorber through the 3rd solution heat exchanger, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with 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 second absorber again, condenser and the 4th 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.
The dynamic co-feeding system of 44. heat, that heat described in the 43rd 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 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 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 45. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump, the 3rd absorber, the 4th 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 has exhaust passage to be communicated with the second generator, second generator also has condensate liquid pipeline and ft connection, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, the finisher that engine also has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, engine also has the 4th steam channel to be communicated with heat exchanger, heat exchanger also has the 4th condensate liquid pipeline and ft connection, generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through solution pump, absorber also has weak solution pipeline to be communicated with the 3rd absorber, 3rd 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 with solution heat exchanger through the second solution heat exchanger, generator also has refrigerant steam channel to be communicated with the 4th absorber, 4th absorber also has weak solution pipeline through the 3rd solution pump, 3rd solution heat exchanger is communicated with a point steam chest with generator, steam chest is divided to also have concentrated solution pipeline to be communicated with the 4th absorber through the 3rd solution heat exchanger, steam chest is divided to also have refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with 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 second absorber again, condenser and the 4th 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.
The dynamic co-feeding system of 46. heat, that heat described in the 45th is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the 3rd steam channel to be communicated with evaporimeter has the 3rd 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 3rd 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 47. heat, that arbitrary heat described in 1-2,5-6,17-18,21-23,32-33,39-40 item is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger, cancel the second steam channel be communicated with heat exchanger, cancel the second condensate liquid pipeline be communicated with heat exchanger, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, that arbitrary heat described in 3-4,7-12,19-20,24-27,30-31,34-38,41-44 item is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger, cancel the 3rd steam channel be communicated with heat exchanger, cancel the 3rd condensate liquid pipeline be communicated with heat exchanger, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, that arbitrary heat described in 13-16,28-29,45-46 item is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger, cancel the 4th steam channel be communicated with heat exchanger, cancel the 4th condensate liquid pipeline be communicated with heat exchanger, form the dynamic co-feeding system of heat.
Accompanying drawing illustrates:
Fig. 1 moves co-feeding system the 1st kind of principled thermal system figure according to heat provided by the present invention.
Fig. 2 moves co-feeding system the 2nd kind of principled thermal system figure according to heat provided by the present invention.
Fig. 3 moves co-feeding system the 3rd kind of principled thermal system figure according to heat provided by the present invention.
Fig. 4 moves co-feeding system the 4th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 5 moves co-feeding system the 5th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 6 moves co-feeding system the 6th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 7 moves co-feeding system the 7th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 8 moves co-feeding system the 8th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 9 moves co-feeding system the 9th kind of principled thermal system figure according to heat provided by the present invention.
Figure 10 moves co-feeding system the 10th kind of principled thermal system figure according to heat provided by the present invention.
Figure 11 moves co-feeding system the 11st kind of principled thermal system figure according to heat provided by the present invention.
Figure 12 moves co-feeding system the 12nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 13 moves co-feeding system the 13rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 14 moves co-feeding system the 14th kind of principled thermal system figure according to heat provided by the present invention.
Figure 15 moves co-feeding system the 15th kind of principled thermal system figure according to heat provided by the present invention.
Figure 16 moves co-feeding system the 16th kind of principled thermal system figure according to heat provided by the present invention.
Figure 17 moves co-feeding system the 17th kind of principled thermal system figure according to heat provided by the present invention.
Figure 18 moves co-feeding system the 18th kind of principled thermal system figure according to heat provided by the present invention.
Figure 19 moves co-feeding system the 19th kind of principled thermal system figure according to heat provided by the present invention.
Figure 20 moves co-feeding system the 20th kind of principled thermal system figure according to heat provided by the present invention.
Figure 21 moves co-feeding system the 21st kind of principled thermal system figure according to heat provided by the present invention.
Figure 22 moves co-feeding system the 22nd kind of principled thermal system figure according to heat provided by the present invention.
In figure, 1-generation-evaporimeter, 2-absorber, 3-condenser, 4-solution pump, 5-cryogen liquid pump, 6-solution heat exchanger, 7-solution choke valve, 8-divides steam chest, 9-heat exchanger, 10-engine, 11-working machine, 12-generator, 13-evaporimeter, 14-second absorber, 15-second solution pump, 16-second solution heat exchanger, 17-second point of steam chest, 18-second generator, 19-second cryogen liquid pump, 20-second evaporimeter, 21-the 3rd absorber, 22-the 3rd cryogen liquid pump, 23-second solution choke valve, 24-the 4th absorber, 25-the 3rd solution pump, 26-the 3rd solution heat exchanger.
Here also following explanation to be provided:
(1) live steam---refer to for hot merit conversion, pressure and temperature all higher than the engine working media drawn gas.
(2) steam discharge---refer to engine export medium, as the low-pressure steam in steam turbine outlet moist steam.
(3) second steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of steam discharge.
(4) the 3rd steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the second steam.
(4) the 4th steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the 3rd steam.
(5) liquid that condensate liquid---steam discharge exothermic condensation is formed.
(6) second condensate liquids---the liquid that the second steam exothermic condensation is formed.
(7) the 3rd condensate liquids---the liquid that the 3rd steam exothermic condensation is formed.
(8) the 4th condensate liquids---the liquid that the 4th steam exothermic condensation is formed.
(9) relevant with engine, but do not relate to operation principle of the present invention, the parts (as dynamical system backheat heat exchanger components etc.) irrelevant with content of the present invention and flow process (recovery etc. as condensate liquid), not in express ranges of the present invention.
(10) cryogen liquid and condensate liquid---the refrigerant vapour exothermic condensation that generator solution discharges forms cryogen liquid, and the working steam exothermic condensation of engine forms condensate liquid; Refrigerant vapour and working steam claim cryogen liquid when being same material.
(11) engine outlet steam discharge utilization---move co-feeding system for concrete heat, the utilization of exhaust steam heat load is divided into three kinds of situations: 1. exhaust steam heat load is all utilized; 2. exhaust steam heat load part is utilized; 3. exhaust steam heat load is not utilized.For this reason, " engine 1 or in addition exhaust passage and ft connection " such statement is adopted to summarize steam discharge utilization power.
(12) about the name of generator and generation-evaporimeter---be called generator, as the generator 12 in Fig. 2 time only heat vaporized for solution; When being respectively used to be called generation-evaporimeter, as the generation-evaporimeter 1 in Fig. 3 when the heat vaporized and cryogen liquid of solution is heat vaporized.
(13) effect of choke valve and solution choke valve---for fluid step-down, can be replaced by gravity pressure reduction or pipe resistance.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, do not repeat in inessential situation; Apparent flow process is not stated.The present invention is described in detail below in conjunction with accompanying drawing and example.
Heat shown in Fig. 1 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine and a working machine, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generation-evaporimeter 1, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with absorber 2 again, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the second steam, the heat release in heat exchanger 9 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, steam discharge heat release in generation-evaporimeter 1 becomes condensate liquid externally to discharge, and engine 10 also externally discharges steam discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generation-evaporimeter 1 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and provides to condenser 3; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 flows through generation-evaporimeter 1, absorbs heat into refrigerant vapour and provide to absorber 2 after cryogen liquid pump 5 pressurizes, and 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 absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator and an evaporimeter, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with evaporimeter 13 has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13, the heat release in evaporimeter 13 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generator 12 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and provides to condenser 3; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide to absorber 2, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 3 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generation-evaporimeter 1, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the second absorber 14, second absorber 14 also has weak solution pipeline through the second solution pump 15, second solution heat exchanger 16 is communicated with second point of steam chest 17 with generation-evaporimeter 1, second point of steam chest 17 also has concentrated solution pipeline to be communicated with the second absorber 14 through the second solution heat exchanger 16, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with absorber 2 again, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the second steam, the heat release in heat exchanger 9 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, and the heat release in generation-evaporimeter 1 of all or part of steam discharge becomes condensate liquid externally to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generation-evaporimeter 1 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and provides to the second absorber 14; The weak solution of the second absorber 14 flows through generation-evaporimeter 1 after the second solution pump 15 and the second solution heat exchanger 16, heat absorbing part vaporization enters second point of steam chest 17, second point of steam chest 17 discharges refrigerant vapour and provides to condenser 3, the concentrated solution of second point of steam chest 17 enters the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release in cooling medium; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 flows through generation-evaporimeter 1, absorbs heat into refrigerant vapour and provide to absorber 2 after cryogen liquid pump 5 pressurizes, and forms 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 absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with evaporimeter 13 has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the second absorber 14, second absorber 14 also has weak solution pipeline through the second solution pump 15, second solution heat exchanger 16 is communicated with second point of steam chest 17 with generator 12, second point of steam chest 17 also has concentrated solution pipeline to be communicated with the second absorber 14 through the second solution heat exchanger 16, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13, the heat release in evaporimeter 13 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generator 12 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges and provides refrigerant vapour to the second absorber 14; The weak solution of the second absorber 14 flows through generator 12 after the second solution pump 15 and the second solution heat exchanger 16, heat absorbing part vaporization enters second point of steam chest 17, second point of steam chest 17 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of second point of steam chest 17 enters the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release in cooling medium; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide to absorber 2, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 5 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has the second condensate liquid pipeline and ft connection, and engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generation-evaporimeter 1, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the second absorber 14, second absorber 14 also has weak solution pipeline through the second solution pump 15, second solution heat exchanger 16 is communicated with second point of steam chest 17 with generator 12, second point of steam chest 17 also has concentrated solution pipeline to be communicated with the second absorber 14 through the second solution heat exchanger 16, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with absorber 2 again, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to generation-evaporimeter 1, the heat release in generation-evaporimeter 1 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, and all or part of steam discharge becomes condensate liquid externally to discharge in generator 12; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generation-evaporimeter 1 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and provides to the second absorber 14; The weak solution of the second absorber 14 flows through generator 12 after the second solution pump 15 and the second solution heat exchanger 16, heat absorbing part vaporization enters second point of steam chest 17, second point of steam chest 17 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of second point of steam chest 17 enters the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release in cooling medium; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 flows through generation-evaporimeter 1, absorbs heat into refrigerant vapour and provide to absorber 2 after cryogen liquid pump 5 pressurizes, and forms 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 absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second generator, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with the second generator 18 and evaporimeter 13 successively has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, second generator 18 also has concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the second generator 18 through solution heat exchanger 6, second generator 18 also has refrigerant steam channel to be communicated with the second absorber 14, second absorber 14 also has weak solution pipeline through the second solution pump 15, second solution heat exchanger 16 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have concentrated solution pipeline to be communicated with the second absorber 14 through the second solution heat exchanger 16, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to the second generator 18 and evaporimeter 13, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with evaporimeter 13, progressively heat release through the second generator 18, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge; The concentrated solution of the second generator 18 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the second generator 18, heat absorption release refrigerant vapour providing to the second absorber 14 through solution heat exchanger 6; The weak solution of the second absorber 14 flows through generator 12 after the second solution pump 15 and the second solution heat exchanger 16, heat absorbing part vaporization enters point steam chest 8, point steam chest 8 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of point steam chest 8 enters the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release in cooling medium; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide to absorber 2, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 7 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest and second generator, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with the second generator 18, second generator 18 also has the second condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the 3rd steam channel to be communicated with evaporimeter 13 has the 3rd condensate liquid pipeline and ft connection again, engine 10 also has the 4th steam channel to be communicated with heat exchanger 9, heat exchanger 9 also has the 4th condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with the second generator 18, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the second absorber 14, second absorber 14 also has weak solution pipeline through the second solution pump 15, second solution heat exchanger 16 is communicated with second point of steam chest 17 with generator 12, second point of steam chest 17 also has concentrated solution pipeline to be communicated with the second absorber 14 through the second solution heat exchanger 16, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 4th steam, the heat release in heat exchanger 9 of 4th steam is discharged through the 4th condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the 3rd steam to evaporimeter 13, the heat release in evaporimeter 13 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 10 provides the second steam to the second generator 18, the heat release in the second generator 18 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, all or part of steam discharge becomes condensate liquid externally to discharge in generator 12, the concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through the second generator 18 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and provides to the second absorber 14, the weak solution of the second absorber 14 flows through generator 12 after the second solution pump 15 and the second solution heat exchanger 16, heat absorbing part vaporization enters point steam chest 8, point steam chest 8 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of point steam chest 8 enters the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release in cooling medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide to absorber 2, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 8 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second generator, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also have the second steam channel be communicated with the second generator 18 after the second generator 18 have the second condensate liquid pipeline and ft connection again, the finisher 13 that engine 10 also has the 3rd steam channel to be communicated with evaporimeter 13 has the 3rd condensate liquid pipeline and ft connection again, engine 10 also has the 4th steam channel to be communicated with heat exchanger 9, heat exchanger 9 also has the 4th condensate liquid pipeline and ft connection, second generator 18 also has concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the second generator 18 through solution heat exchanger 6, second generator 18 also has refrigerant steam channel to be communicated with the second absorber 14, second absorber 14 also has weak solution pipeline through the second solution pump 15, second solution heat exchanger 16 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have concentrated solution pipeline to be communicated with the second absorber 14 through the second solution heat exchanger 16, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 4th steam, the heat release in heat exchanger 9 of 4th steam is discharged through the 4th condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the 3rd steam to evaporimeter 13, the heat release in evaporimeter 13 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 10 provides the second steam to the second generator 18, the heat release in the second generator 18 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of the second generator 18 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the second generator 18, heat absorption release refrigerant vapour providing to the second absorber 14 through solution heat exchanger 6, the weak solution of the second absorber 14 flows through generator 12 after the second solution pump 15 and the second solution heat exchanger 16, heat absorbing part vaporization enters point steam chest 8, point steam chest 8 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of point steam chest 8 enters the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release in cooling medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide to absorber 2, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 9 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump and second point of steam chest, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the second absorber 14 through solution heat exchanger 6, second absorber 14 also has weak solution pipeline to be communicated with second point of steam chest 17 with generation-evaporimeter 1 through the second solution pump 15, second point of steam chest 17 also has concentrated solution pipeline to be communicated with a point steam chest 8 with generation-evaporimeter 1 through solution choke valve 7, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the second absorber 14, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with absorber 2 again, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the second steam, the heat release in heat exchanger 9 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, and the heat release in generation-evaporimeter 1 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of steam chest 8 is divided to enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 2 enters the second absorber 14 through solution heat exchanger 6, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 14 flows through generation-evaporimeter 1 after the second solution pump 15 is pressurizeed, heat absorbing part vaporization enters second point of steam chest 17, second point of steam chest 17 discharges refrigerant vapour and provides to condenser 3, the concentrated solution of second point of steam chest 17 flows through generation-evaporimeter 1 after solution choke valve 17 reducing pressure by regulating flow, heat absorbing part vaporization enters point steam chest 8, steam chest 8 is divided to discharge refrigerant vapour and provide to the second absorber 14, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 flows through generation-evaporimeter 1, absorbs heat into refrigerant vapour and provide to absorber 2 after cryogen liquid pump 5 pressurizes, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 10 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel generation-evaporimeter 1 to be communicated with, generation-evaporimeter 1 also has the second condensate liquid pipeline and ft connection, and engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the second absorber 14 through solution heat exchanger 6, second absorber 14 also has weak solution pipeline through the second solution pump 15, second solution heat exchanger 16 is communicated with second point of steam chest 17 with generation-evaporimeter 1, second point of steam chest 17 also has concentrated solution pipeline to be communicated with a point steam chest 8 with generator 12 through the second solution heat exchanger 17, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the second absorber 14, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with absorber 2 again, condenser 3 and the second absorber 14 also have cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to generation-evaporimeter 1, the heat release in generation-evaporimeter 1 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of steam chest 8 is divided to enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 2 enters the second absorber 14 through solution heat exchanger 6, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 14 flows through generation-evaporimeter 1 after the second solution pump 15 and the second solution heat exchanger 16, heat absorbing part vaporization enters second point of steam chest 17, second point of steam chest 17 discharges refrigerant vapour and provides to condenser 3, the concentrated solution of second point of steam chest 17 flows through generator 12 after the second solution heat exchanger 16 is lowered the temperature, heat absorbing part vaporization enters point steam chest 8, steam chest 8 is divided to discharge refrigerant vapour and provide to the second absorber 14, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 3 flows through generation-evaporimeter 1, absorbs heat into refrigerant vapour and provide to absorber 2 after cryogen liquid pump 5 pressurizes, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 11 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and a second cryogen liquid pump, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with a point steam chest 8 through solution heat exchanger 6, solution choke valve 7 and generation-evaporimeter 1, point steam chest 8 also have refrigerant steam channel be communicated with generator 12 after generator 12 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 19 again, the second cryogen liquid pump 19 also have cryogen liquid pipeline be communicated with generation-evaporimeter 1 after occur-evaporimeter 1 has refrigerant steam channel to be communicated with absorber 2 again, generator 12 also has concentrated solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline to be communicated with generator 12 through the second solution heat exchanger 16, generator 12 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the second steam, the heat release in heat exchanger 9 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, and the heat release in generation-evaporimeter 1 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generation-evaporimeter 1 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and is supplied to generator 12 to be done to drive thermal medium, the concentrated solution of generator 12 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 14 enters generator 12 through the second solution heat exchanger 16, refrigerant vapour flows through generator 18, heating enters the solution release in it and provides refrigerant vapour to condenser 3, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 flows through generation-evaporimeter 1 after cryogen liquid pump 5 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, the refrigerant vapour heat release flowing through generator 12 becomes cryogen liquid, then flows through generations-evaporimeter 1, absorb heat into refrigerant vapour and provide to absorber 2 after the second cryogen liquid pump 19 pressurizes, and forms heat and moves co-feeding system.
Heat shown in Figure 12 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and a second cryogen liquid pump, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with evaporimeter 13 has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with a point steam chest 8 through solution heat exchanger 6, solution choke valve 7 and generation-evaporimeter 1, point steam chest 8 also have refrigerant steam channel be communicated with generator 12 after generator 12 have cryogen liquid pipeline to be communicated with evaporimeter 13 through the second cryogen liquid pump 19 again, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, generator 12 also has concentrated solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline to be communicated with generator 12 through the second solution heat exchanger 16, generator 12 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13, the heat release in evaporimeter 13 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, and the heat release in generation-evaporimeter 1 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generation-evaporimeter 1 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and is supplied to generator 12 to be done to drive thermal medium, the concentrated solution of generator 12 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 14 enters generator 12 through the second solution heat exchanger 16, refrigerant vapour flows through generator 12, heating enters the solution release in it and provides refrigerant vapour to condenser 3, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 flows through generation-evaporimeter 1 after cryogen liquid pump 5 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, the refrigerant vapour heat release flowing through generator 12 enters evaporimeter 13 through the second cryogen liquid pump 19 pressurization after becoming cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 2, 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 absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump and second evaporimeter, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also have the second steam channel be communicated with evaporimeter 13 and the second evaporimeter 20 successively after the second evaporimeter 20 have the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with a point steam chest 8 through solution heat exchanger 6, solution choke valve 7 and generator 12, point steam chest 8 also have refrigerant steam channel be communicated with the second generator 18 after the second generator 18 have cryogen liquid pipeline to be communicated with evaporimeter 13 through the second cryogen liquid pump 19 again, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, second generator 18 also has concentrated solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline to be communicated with the second generator 18 through the second solution heat exchanger 16, second generator 18 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with the second evaporimeter 20 through cryogen liquid pump 5, second evaporimeter 20 also has refrigerant steam channel to be communicated with the second absorber 14, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13 and the second evaporimeter 20, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with the second evaporimeter 20, progressively heat release through evaporimeter 13, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generator 12 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and is supplied to the second generator 18 to be done to drive thermal medium, the concentrated solution of the second generator 18 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 14 enters the second generator 18 through the second solution heat exchanger 16, refrigerant vapour flows through the second generator 18, heating enters the solution release in it and provides refrigerant vapour to condenser 3, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 enters the second evaporimeter 20 through cryogen liquid pump 5 pressurization, absorb heat into refrigerant vapour and provide to the second absorber 14, the refrigerant vapour heat release flowing through the second generator 18 enters evaporimeter 13 through the second cryogen liquid pump 19 pressurization after becoming cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 2, 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 absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump and second evaporimeter, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also have the second steam channel be communicated with the second evaporimeter 20 after the second evaporimeter 20 have the second condensate liquid pipeline and ft connection again, the finisher 13 that engine 10 also has the 3rd steam channel to be communicated with evaporimeter 13 has the 3rd condensate liquid pipeline and ft connection again, engine 10 also has the 4th steam channel to be communicated with heat exchanger 9, heat exchanger 9 also has the 4th condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with a point steam chest 8 through solution heat exchanger 6, solution choke valve 7 and generator 12, point steam chest 8 also have refrigerant steam channel be communicated with the second generator 18 after the second generator 18 have cryogen liquid pipeline to be communicated with evaporimeter 13 through the second cryogen liquid pump 19 again, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, second generator 18 also has concentrated solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline to be communicated with the second generator 18 through the second solution heat exchanger 16, second generator 18 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with the second evaporimeter 20 through cryogen liquid pump 5, second evaporimeter 20 also has refrigerant steam channel to be communicated with the second absorber 14, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 4th steam, the heat release in heat exchanger 9 of 4th steam is discharged through the 4th condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the 3rd steam to evaporimeter 13, the heat release in evaporimeter 13 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 10 provides the second steam to the second evaporimeter 20, the heat release in the second evaporimeter 20 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generator 12 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and is supplied to the second generator 18 to be done to drive thermal medium, the concentrated solution of the second generator 18 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 14 enters the second generator 18 through the second solution heat exchanger 16, refrigerant vapour flows through the second generator 18, heating enters the solution release in it and provides refrigerant vapour to condenser 3, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 enters the second evaporimeter 20 through cryogen liquid pump 5 pressurization, absorb heat into refrigerant vapour and provide to the second absorber 14, the refrigerant vapour heat release flowing through the second generator 18 enters evaporimeter 13 through the second cryogen liquid pump 19 pressurization after becoming cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 2, 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 is primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator and the second cryogen liquid pump and formed, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with evaporimeter 13 has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with a point steam chest 8 through solution heat exchanger 6, solution choke valve 7 and generator 12, a point steam chest 8 also have refrigerant steam channel be communicated with the second generator 18 after the second generator 18 have cryogen liquid pipeline to be communicated with evaporimeter 13 through the second cryogen liquid pump 19 again, second generator 18 also has concentrated solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline to be communicated with the second generator 18 through the second solution heat exchanger 16, second generator 18 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with the second absorber 14 with absorber 2 respectively, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13, the heat release in evaporimeter 13 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 flows through generator 12 after solution heat exchanger 6 cooling and solution choke valve 7 step-down, heat absorbing part is vaporized and entered point steam chest 8, and a point steam chest 8 discharges refrigerant vapour and is supplied to the second generator 18 to be done to drive thermal medium, the concentrated solution of the second generator 18 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 14 enters the second generator 18 through the second solution heat exchanger 16, refrigerant vapour flows through the second generator 18, heating enters the solution release in it and provides refrigerant vapour to condenser 3, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 enters evaporimeter 13 through cryogen liquid pump 5 pressurization, the refrigerant vapour heat release flowing through the second generator 18 enters evaporimeter 13 through the second cryogen liquid pump 19 pressurization after becoming cryogen liquid, the cryogen liquid of evaporimeter 13 absorbs heat into refrigerant vapour and provides respectively to absorber 2 and the second absorber 14, form the dynamic co-feeding system of heat.
Heat shown in Figure 16 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump and the 3rd absorber; Engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection; steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the 3rd absorber 21,3rd absorber 21 also has weak solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generation-evaporimeter 1, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with the 3rd absorber 21 with absorber 2 respectively again, condenser 3 also has cryogen liquid pipeline the 3rd absorber 21 after the second cryogen liquid pump 19 is communicated with the 3rd absorber 21 to have refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the second steam, the heat release in heat exchanger 9 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, and the heat release in generation-evaporimeter 1 of all or part of steam discharge becomes condensate liquid externally to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorb refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium; The weak solution of the second absorber 14 flows through generation-evaporimeter 1 after the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve 7 and vaporization of absorbing heat enters point steam chest 8, and a point steam chest 8 discharges and provides refrigerant vapour to condenser 3; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 is divided into two-way---and the first via flows through generation-evaporimeter 1, absorbs heat into refrigerant vapour and provide respectively to absorber 2 and the 3rd absorber 21 after cryogen liquid pump 5 pressurizes, flow through the 3rd absorber 21 after second tunnel second cryogen liquid pump 19 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, 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 absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump and the 3rd absorber, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with evaporimeter 13 has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the 3rd absorber 21, 3rd absorber 21 also has weak solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with the 3rd absorber 21 with absorber 2 respectively, condenser 3 also has cryogen liquid pipeline the 3rd absorber 21 after the second cryogen liquid pump 19 is communicated with the 3rd absorber 21 to have refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13, the heat release in evaporimeter 13 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid externally to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorb refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium; The weak solution of the second absorber 14 flows through generator 12 after the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve 7, and enter point steam chest 8 after heat absorbing part vaporization, a point steam chest 8 discharges and provides refrigerant vapour to condenser 3; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 is divided into two-way---and the first via enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide respectively to absorber 2 and the 3rd absorber 21, flow through the 3rd absorber 21 after second tunnel second cryogen liquid pump 19 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, 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 generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump, the 3rd absorber, the 3rd cryogen liquid pump and a second solution choke valve, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with evaporimeter 13 has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the 3rd absorber 21 through the second solution choke valve 23, 3rd absorber 21 also has weak solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generation-evaporimeter 1, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with absorber 2, condenser 3 also has cryogen liquid pipeline the 3rd absorber 21 after the second cryogen liquid pump 19 is communicated with the 3rd absorber 21 to have refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 also have cryogen liquid pipeline occur after the 3rd cryogen liquid pump 22 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with the 3rd absorber 21 again, condenser 3 also has cooling medium pipeline and ft connection, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13, the heat release in evaporimeter 13 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, and the heat release in generation-evaporimeter 1 of all or part of steam discharge becomes condensate liquid to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21 after the second solution choke valve 23 reducing pressure by regulating flow, absorb refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium; The weak solution of the second absorber 14 flows through generation-evaporimeter 1 after the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve 7, and enter point steam chest 8 after heat absorbing part vaporization, a point steam chest 8 discharges and provides refrigerant vapour to condenser 3; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 is divided into three tunnels---and the first via enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide to absorber 2, flow through the 3rd absorber 21 after second tunnel second cryogen liquid pump 19 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, flow through generation-evaporimeter 1 after 3rd tunnel the 3rd cryogen liquid pump 22 pressurizes, absorb heat into refrigerant vapour and provide to the 3rd absorber 21, form the dynamic co-feeding system of heat.
Heat shown in Figure 19 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generation-evaporimeter 1, generation-evaporimeter 1 also has condensate liquid pipeline and ft connection, engine 10 also has the second steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the 3rd absorber 21, 3rd absorber 21 also has weak solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generation-evaporimeter 1, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has weak solution pipeline through the 3rd solution pump 25, 3rd solution heat exchanger 26 is communicated with second point of steam chest 17 with generation-evaporimeter 1, second point of steam chest 17 also has concentrated solution pipeline to be communicated with the 4th absorber 24 through the 3rd solution heat exchanger 26, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also have cryogen liquid pipeline occur after cryogen liquid pump 5 is communicated with generation-evaporimeter 1-evaporimeter 1 has refrigerant steam channel to be communicated with the 3rd absorber 21 with absorber 2 respectively again, condenser 3 also has cryogen liquid pipeline the 3rd absorber 21 after the second cryogen liquid pump 19 is communicated with the 3rd absorber 21 to have refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 and the 4th absorber 24 also have cooling medium pipeline and ft connection respectively, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the second steam, the heat release in heat exchanger 9 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides steam discharge to generation-evaporimeter 1, and the heat release in generation-evaporimeter 1 of all or part of steam discharge becomes condensate liquid to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorb refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium; The weak solution of the second absorber 14 flows through generation-evaporimeter 1 after the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve 7, and heat absorbing part vaporization enters point steam chest 8, and a point steam chest 8 discharges and provides refrigerant vapour to the 4th absorber 24; The weak solution of the 4th absorber 24 enters second point of steam chest 17 after flowing through generation-evaporimeter 1, heat absorbing part vaporization after the 3rd solution pump 25 and the 3rd solution heat exchanger 26, the concentrated solution of second point of steam chest 17 enters the 4th absorber 24 through the 3rd solution heat exchanger 26, absorb refrigerant vapour and heat release in cooling medium, second point of steam chest 17 discharges and provides refrigerant vapour to condenser 3; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, condenser 3 cryogen liquid is divided into two-way---and the first via flows through generation-evaporimeter 1, absorbs heat into refrigerant vapour and provide respectively to absorber 2 and the 3rd absorber 21 after cryogen liquid pump 5 pressurizes, flow through the 3rd absorber 21 after second tunnel second cryogen liquid pump 19 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, form the dynamic co-feeding system of heat.
Heat shown in Figure 20 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with generator 12, generator 12 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with evaporimeter 13 has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, steam chest 8 is divided to have concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the 3rd absorber 21, 3rd absorber 21 also has weak solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, solution choke valve 7 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has weak solution pipeline through the 3rd solution pump 25, 3rd solution heat exchanger 26 is communicated with second point of steam chest 17 with generator 12, second point of steam chest 17 also has concentrated solution pipeline to be communicated with the 4th absorber 24 through the 3rd solution heat exchanger 26, second point of steam chest 17 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with the 3rd absorber 21 with absorber 2 respectively, condenser 3 also has cryogen liquid pipeline the 3rd absorber 21 after the second cryogen liquid pump 19 is communicated with the 3rd absorber 21 to have refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 and the 4th absorber 24 also have cooling medium pipeline and ft connection respectively, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to evaporimeter 13, the heat release in evaporimeter 13 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to generator 12, and the heat release in generator 12 of all or part of steam discharge becomes condensate liquid to discharge; The concentrated solution of point steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorb refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium; The weak solution of the second absorber 14 flows through generator 12 after the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve 7, and enter point steam chest 8 after heat absorbing part vaporization, a point steam chest 8 discharges and provides refrigerant vapour to the 4th absorber 24; The weak solution of the 4th absorber 24 flows through generator 12 after the 3rd solution pump 25 and the 3rd solution heat exchanger 26, heat absorbing part vaporization enters second point of steam chest 17, the concentrated solution of second point of steam chest 17 enters the 4th absorber 24 through the 3rd solution heat exchanger 26, absorb refrigerant vapour and heat release in cooling medium, second point of steam chest 17 discharges and provides refrigerant vapour to condenser 3; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 is divided into two-way---and the first via enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide respectively to absorber 2 and the 3rd absorber 21, flow through the 3rd absorber 21 after second tunnel second cryogen liquid pump 19 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, form the dynamic co-feeding system of heat.
Heat shown in Figure 21 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with the second generator 18, second generator 18 also has condensate liquid pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be communicated with generator 12 and evaporimeter 13 successively has the second condensate liquid pipeline and ft connection again, engine 10 also has the 3rd steam channel to be communicated with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection, generator 12 also has concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the 3rd absorber 21, 3rd absorber 21 also has weak solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline to be communicated with generator 12 with solution heat exchanger 6 through the second solution heat exchanger 16, generator 12 also has refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has weak solution pipeline through the 3rd solution pump 25, 3rd solution heat exchanger 26 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have concentrated solution pipeline to be communicated with the 4th absorber 24 through the 3rd solution heat exchanger 26, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with the 3rd absorber 21 with absorber 2 respectively, condenser 3 also has cryogen liquid pipeline the 3rd absorber 21 after the second cryogen liquid pump 19 is communicated with the 3rd absorber 21 to have refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 and the 4th absorber 24 also have cooling medium pipeline and ft connection respectively, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 3rd steam, the heat release in heat exchanger 9 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the second steam to generator 12 and evaporimeter 13, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with evaporimeter 13, progressively heat release through generator 12, engine 10 provides steam discharge to the second generator 18, and the heat release in the second generator 18 of all or part of steam discharge becomes condensate liquid to discharge; The concentrated solution of generator 12 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorb refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium; The weak solution of the second absorber 14 enters generator 12 through the second solution heat exchanger 16 and solution heat exchanger 6, absorbing heat discharges refrigerant vapour and provide to the 4th absorber 24; The weak solution of the 4th absorber 24 flows through the second generator 18 after the 3rd solution pump 25 and the 3rd solution heat exchanger 26, heat absorbing part vaporization enters point steam chest 8, point steam chest 8 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of point steam chest 8 enters the 4th absorber 24 through the 3rd solution heat exchanger 26, absorb refrigerant vapour and heat release in cooling medium; The refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 is divided into two-way---and the first via enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide respectively to absorber 2 and the 3rd absorber 21, flow through the 3rd absorber 21 after second tunnel second cryogen liquid pump 19 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, form the dynamic co-feeding system of heat.
Heat shown in Figure 22 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 10 connects working machine 11, engine 10 has live steam passage and ft connection, engine 10 also has exhaust passage to be communicated with the second generator 18, second generator 18 also has condensate liquid pipeline and ft connection, engine 10 also have the second steam channel be communicated with generator 12 after generator 12 have the second condensate liquid pipeline and ft connection again, the finisher 13 that engine 10 also has the 3rd steam channel to be communicated with evaporimeter 13 has the 3rd condensate liquid pipeline and ft connection again, engine 10 also has the 4th steam channel to be communicated with heat exchanger 9, heat exchanger 9 also has the 4th condensate liquid pipeline and ft connection, generator 12 also has concentrated solution pipeline to be communicated with absorber 2 with solution heat exchanger 6 through solution pump 4, absorber 2 also has weak solution pipeline to be communicated with the 3rd absorber 21, 3rd absorber 21 also has weak solution pipeline to be communicated with the second absorber 14 with the second solution heat exchanger 16 through the second solution pump 15, second absorber 14 also has weak solution pipeline to be communicated with generator 12 with solution heat exchanger 6 through the second solution heat exchanger 16, generator 12 also has refrigerant steam channel to be communicated with the 4th absorber 24, 4th absorber 24 also has weak solution pipeline through the 3rd solution pump 25, 3rd solution heat exchanger 26 is communicated with a point steam chest 8 with generator 12, steam chest 8 is divided to also have concentrated solution pipeline to be communicated with the 4th absorber 24 through the 3rd solution heat exchanger 26, steam chest 8 is divided to also have refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with evaporimeter 13 through cryogen liquid pump 5, evaporimeter 13 also has refrigerant steam channel to be communicated with the 3rd absorber 21 with absorber 2 respectively, condenser 3 also has cryogen liquid pipeline the 3rd absorber 21 after the second cryogen liquid pump 19 is communicated with the 3rd absorber 21 to have refrigerant steam channel to be communicated with the second absorber 14 again, condenser 3 and the 4th absorber 24 also have cooling medium pipeline and ft connection respectively, absorber 2 and the second absorber 14 also have heated medium pipeline and ft connection respectively, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 10 step-down work done, engine 10 heat exchanger 9 provides the 4th steam, the heat release in heat exchanger 9 of 4th steam is discharged through the 4th condensate liquid pipeline after heated medium becomes condensate liquid, engine 10 provides the 3rd steam to evaporimeter 13, the heat release in evaporimeter 13 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 10 provides the second steam to generator 12, the heat release in generator 12 of second steam is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 10 provides steam discharge to the second generator 18, the heat release in the second generator 18 of all or part of steam discharge becomes condensate liquid externally to discharge, the concentrated solution of generator 12 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorb refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium, the weak solution of the second absorber 14 enters generator 12 through the second solution heat exchanger 16 and solution heat exchanger 6, absorbing heat discharges refrigerant vapour and provide to the 4th absorber 24, the weak solution of the 4th absorber 24 flows through the second generator 18 after the 3rd solution pump 25 and the 3rd solution heat exchanger 26, heat absorbing part vaporization enters point steam chest 8, point steam chest 8 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of point steam chest 8 enters the 4th absorber 24 through the 3rd solution heat exchanger 26, absorb refrigerant vapour and heat release in cooling medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 3 is divided into two-way---and the first via enters evaporimeter 13 through cryogen liquid pump 5 pressurization, absorbs heat into refrigerant vapour and provide respectively to absorber 2 and the 3rd absorber 21, flow through the 3rd absorber 21 after second tunnel second cryogen liquid pump 19 pressurizes, absorb heat into refrigerant vapour and provide to the second absorber 14, form 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 outlet 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) provide multiple concrete technical scheme, numerous different actual state can be tackled, have the wider scope of application.
(4) during variable working condition, can preferentially adopt second-kind absorption-type heat pump for thermal flow process, the thermic load of heat exchanger has adjustment space, ensure that the efficient and flexible of system.
(5) steam discharge and engine intermediate extraction combine for the thermal source of absorption heat pump flow process, for meeting different user and duty requirements brings good flexibility.
(6) there is the double dominant of extraction for heat supply and condensing heat supply, avoid heating demand change largely to the impact of generating.
(7) generation-evaporimeter can use, for the layout of single unit system brings flexibility as the condensing unit of engine simultaneously.
(8) enriched the type of hot dynamic co-feeding system, extended the range of application of second-kind absorption-type heat pump, be conducive to adopting second-kind absorption-type heat pump to realize making full use of of the temperature difference better.

Claims (49)

1. the dynamic co-feeding system of heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine and a working machine, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with absorber (2) again, condenser (3) also has cooling medium pipeline and ft connection, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with absorber (2) to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up exhaust passage and is communicated with absorber (2), forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator and an evaporimeter, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), condenser (3) also has cooling medium pipeline and ft connection, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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 (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump has the second steam channel to be communicated with absorber (2), had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest; Engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection; steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the second absorber (14), second absorber (14) also has weak solution pipeline through the second solution pump (15), second solution heat exchanger (16) is communicated with second point of steam chest (17) with generation-evaporimeter (1), second point of steam chest (17) also has concentrated solution pipeline to be communicated with the second absorber (14) through the second solution heat exchanger (16), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with absorber (2) again, condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with absorber (2) to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up exhaust passage and is communicated with absorber (2), forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the second absorber (14), second absorber (14) also has weak solution pipeline through the second solution pump (15), second solution heat exchanger (16) is communicated with second point of steam chest (17) with generator (12), second point of steam chest (17) also has concentrated solution pipeline to be communicated with the second absorber (14) through the second solution heat exchanger (16), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, the finisher (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection, evaporimeter (13) to have refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump again has refrigerant steam channel to be communicated with absorber (2), forms the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has the second condensate liquid pipeline and ft connection, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the second absorber (14), second absorber (14) also has weak solution pipeline through the second solution pump (15), second solution heat exchanger (16) is communicated with second point of steam chest (17) with generator (12), second point of steam chest (17) also has concentrated solution pipeline to be communicated with the second absorber (14) through the second solution heat exchanger (16), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with absorber (2) again, condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with absorber (2) to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up the second steam channel and is communicated with absorber (2), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second generator, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with the second generator (18) and evaporimeter (13) successively has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, second generator (18) also has concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the second generator (18) through solution heat exchanger (6), second generator (18) also has refrigerant steam channel to be communicated with the second absorber (14), second absorber (14) also has weak solution pipeline through the second solution pump (15), second solution heat exchanger (16) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have concentrated solution pipeline to be communicated with the second absorber (14) through the second solution heat exchanger (16), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, engine (10) is had the second steam channel be communicated with successively the second generator (18) and the finisher (13) of evaporimeter (13) have again the second condensate liquid pipeline and ft connection be adjusted to engine (10) have the second steam channel be communicated with the second generator (18) after the second generator (18) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (13) refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) to set up the second steam channel to be communicated with absorber (2), had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest and second generator, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with the second generator (18), second generator (18) also has the second condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, engine (10) also has the 4th steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 4th condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with the second generator (18), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the second absorber (14), second absorber (14) also has weak solution pipeline through the second solution pump (15), second solution heat exchanger (16) is communicated with second point of steam chest (17) with generator (12), second point of steam chest (17) also has concentrated solution pipeline to be communicated with the second absorber (14) through the second solution heat exchanger (16), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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 (13) being had by engine (10) the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump has the 3rd steam channel to be communicated with absorber (2), had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and second generator, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) also have the second steam channel be communicated with the second generator (18) after the second generator (18) have the second condensate liquid pipeline and ft connection again, the finisher (13) that engine (10) also has the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, engine (10) also has the 4th steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 4th condensate liquid pipeline and ft connection, second generator (18) also has concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the second generator (18) through solution heat exchanger (6), second generator (18) also has refrigerant steam channel to be communicated with the second absorber (14), second absorber (14) also has weak solution pipeline through the second solution pump (15), second solution heat exchanger (16) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have concentrated solution pipeline to be communicated with the second absorber (14) through the second solution heat exchanger (16), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, the finisher (13) being had by engine (10) the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump has the 3rd steam channel to be communicated with absorber (2), had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump and second point of steam chest; Engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection; steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the second absorber (14) through solution heat exchanger (6), second absorber (14) also has weak solution pipeline to be communicated with second point of steam chest (17) with generation-evaporimeter (1) through the second solution pump (15), second point of steam chest (17) also has concentrated solution pipeline to be communicated with a point steam chest (8) with generation-evaporimeter (1) through solution choke valve (7), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the second absorber (14), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with absorber (2) again, condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with absorber (2) to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up exhaust passage and is communicated with absorber (2), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and second point of steam chest, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel generation-evaporimeter (1) to be communicated with, generation-evaporimeter (1) also has the second condensate liquid pipeline and ft connection, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the second absorber (14) through solution heat exchanger (6), second absorber (14) also has weak solution pipeline through the second solution pump (15), second solution heat exchanger (16) is communicated with second point of steam chest (17) with generation-evaporimeter (1), second point of steam chest (17) also has concentrated solution pipeline to be communicated with a point steam chest (8) with generator (12) through the second solution heat exchanger (17), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the second absorber (14), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with absorber (2) again, condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) 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, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with absorber (2) to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up the second steam channel and is communicated with absorber (2), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger and a second cryogen liquid pump, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), point steam chest (8) also have refrigerant steam channel be communicated with generator (12) after generator (12) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (19) again, second cryogen liquid pump (19) also have cryogen liquid pipeline be communicated with generation-evaporimeter (1) after there is-evaporimeter (1) and have refrigerant steam channel to be communicated with absorber (2) again, generator (12) also has concentrated solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline to be communicated with generator (12) through the second solution heat exchanger (16), generator (12) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) 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, second cryogen liquid pump (19) is had cryogen liquid pipeline be communicated with generation-evaporimeter (1) after there is-evaporimeter (1) and have refrigerant steam channel to be communicated with absorber (2) to be again adjusted to the second cryogen liquid pump (19) and have cryogen liquid pipeline and ft connection, engine (10) is set up exhaust passage and is communicated with absorber (2), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, move in co-feeding system in heat according to claim 21, second cryogen liquid pump (19) is had cryogen liquid pipeline be communicated with generation-evaporimeter (1) after there is-evaporimeter (1) and have refrigerant steam channel to be communicated with absorber (2) to be again adjusted to the second cryogen liquid pump (19) and have cryogen liquid pipeline and ft connection, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with the second absorber (14) to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up exhaust passage and is communicated with the second absorber (14) with absorber (2) respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger and a second cryogen liquid pump, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), point steam chest (8) also have refrigerant steam channel be communicated with generator (12) after generator (12) have cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) again, evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), generator (12) also has concentrated solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline to be communicated with generator (12) through the second solution heat exchanger (16), generator (12) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 25. heat, move in co-feeding system in heat according to claim 24, cancel evaporimeter, the finisher (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump has the second steam channel to be communicated with absorber (2), had by generator (12) cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) to be adjusted to generator (12) and to have cryogen liquid pipeline through the second cryogen liquid pump (19) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump and second evaporimeter, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) also have the second steam channel be communicated with successively evaporimeter (13) and the second evaporimeter (20) afterwards the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generator (12), point steam chest (8) also have refrigerant steam channel be communicated with the second generator (18) after the second generator (18) have cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) again, evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), second generator (18) also has concentrated solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline to be communicated with the second generator (18) through the second solution heat exchanger (16), second generator (18) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with the second evaporimeter (20) through cryogen liquid pump (5), second evaporimeter (20) also has refrigerant steam channel to be communicated with the second absorber (14), condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, move in co-feeding system in heat according to claim 26, cancel evaporimeter, engine (10) is had the second steam channel be communicated with evaporimeter (13) and the second evaporimeter (20) successively after the second evaporimeter (20) have again the second condensate liquid pipeline and ft connection be adjusted to engine (10) have the second steam channel be communicated with the second evaporimeter (20) after the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (13) refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) to set up the second steam channel to be communicated with absorber (2), had by second generator (18) cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) to be adjusted to the second generator (18) and to have cryogen liquid pipeline through the second cryogen liquid pump (19) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump and second evaporimeter, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) also have the second steam channel be communicated with the second evaporimeter (20) after the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, the finisher (13) that engine (10) also has the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, engine (10) also has the 4th steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 4th condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generator (12), point steam chest (8) also have refrigerant steam channel be communicated with the second generator (18) after the second generator (18) have cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) again, evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), second generator (18) also has concentrated solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline to be communicated with the second generator (18) through the second solution heat exchanger (16), second generator (18) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with the second evaporimeter (20) through cryogen liquid pump (5), second evaporimeter (20) also has refrigerant steam channel to be communicated with the second absorber (14), condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 29. heat, move in co-feeding system in heat according to claim 28, cancel evaporimeter, the finisher (13) being had by engine (10) the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump has the 3rd steam channel to be communicated with absorber (2), had by second generator (18) cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) to be adjusted to the second generator (18) and to have cryogen liquid pipeline through the second cryogen liquid pump (19) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, divides steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second generator and the second cryogen liquid pump and formed, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with a point steam chest (8) through solution heat exchanger (6), solution choke valve (7) and generator (12), divide steam chest (8) in addition refrigerant steam channel be communicated with the second generator (18) after the second generator (18) have cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) again, second generator (18) also has concentrated solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline to be communicated with the second generator (18) through the second solution heat exchanger (16), second generator (18) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with the second absorber (14) with absorber (2) respectively, condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, move in co-feeding system in heat according to claim 30, cancel evaporimeter, the finisher (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with the second absorber (14) with absorber (2) to be respectively adjusted to engine (10) in the lump has the second steam channel to be communicated with the second absorber (14) with absorber (2) respectively, had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, had by second generator (18) cryogen liquid pipeline to be communicated with evaporimeter (13) through the second cryogen liquid pump (19) to be adjusted to the second generator (18) and to have cryogen liquid pipeline through the second cryogen liquid pump (19) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump and the 3rd absorber; Engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection; steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16), solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively again, condenser (3) also has cryogen liquid pipeline the 3rd absorber (21) after the second cryogen liquid pump (19) is communicated with the 3rd absorber (21) to have refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 33. heat, move in co-feeding system in heat according to claim 32, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up exhaust passage and is communicated with the 3rd absorber (21) with absorber (2) respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 34. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump and the 3rd absorber, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16), solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, condenser (3) also has cryogen liquid pipeline the 3rd absorber (21) after the second cryogen liquid pump (19) is communicated with the 3rd absorber (21) to have refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 35. heat, move in co-feeding system in heat according to claim 34, cancel evaporimeter, the finisher (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) to be respectively adjusted to engine (10) in the lump has the second steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 36. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, the second cryogen liquid pump, the 3rd absorber, the 3rd cryogen liquid pump and a second solution choke valve, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the 3rd absorber (21) through the second solution choke valve (23), 3rd absorber (21) also has weak solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16), solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with absorber (2), condenser (3) also has cryogen liquid pipeline the 3rd absorber (21) after the second cryogen liquid pump (19) is communicated with the 3rd absorber (21) to have refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after the 3rd cryogen liquid pump (22) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with the 3rd absorber (21) again, condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 37. heat, move in co-feeding system in heat according to claim 36, cancel evaporimeter, the finisher (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump has the second steam channel to be communicated with absorber (2), had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 38. heat, move in co-feeding system in heat according to claim 36, cancel evaporimeter, the finisher (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with absorber (2) to be adjusted to engine (10) in the lump has the second steam channel to be communicated with absorber (2), had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after the 3rd cryogen liquid pump (22) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with the 3rd absorber (21) to be again adjusted to condenser (3) and have cryogen liquid pipeline through the 3rd cryogen liquid pump (22) and ft connection, engine (10) is set up exhaust passage and is communicated with the 3rd absorber (21), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, formed primarily of generation-evaporimeter, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger; Engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generation-evaporimeter (1), generation-evaporimeter (1) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be communicated with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection; steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16), solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generation-evaporimeter (1), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has weak solution pipeline through the 3rd solution pump (25), 3rd solution heat exchanger (26) is communicated with second point of steam chest (17) with generation-evaporimeter (1), second point of steam chest (17) also has concentrated solution pipeline to be communicated with the 4th absorber (24) through the 3rd solution heat exchanger (26), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively again, condenser (3) also has cryogen liquid pipeline the 3rd absorber (21) after the second cryogen liquid pump (19) is communicated with the 3rd absorber (21) to have refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 40. heat, move in co-feeding system in heat according to claim 39, had by condenser (3) cryogen liquid pipeline that-evaporimeter (1) occurs after cryogen liquid pump (5) is communicated with generation-evaporimeter (1) to have refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively to be again adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) is set up exhaust passage and is communicated with the 3rd absorber (21) with absorber (2) respectively, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporimeter, the second absorber, the second solution pump, the second solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with generator (12), generator (12) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, steam chest (8) is divided to have concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16), solution heat exchanger (6), solution choke valve (7) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has weak solution pipeline through the 3rd solution pump (25), 3rd solution heat exchanger (26) is communicated with second point of steam chest (17) with generator (12), second point of steam chest (17) also has concentrated solution pipeline to be communicated with the 4th absorber (24) through the 3rd solution heat exchanger (26), second point of steam chest (17) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, condenser (3) also has cryogen liquid pipeline the 3rd absorber (21) after the second cryogen liquid pump (19) is communicated with the 3rd absorber (21) to have refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 42. heat, move in co-feeding system in heat according to claim 41, cancel evaporimeter, the finisher (13) being had by engine (10) the second steam channel to be communicated with evaporimeter (13) has the second condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) to be respectively adjusted to engine (10) in the lump has the second steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 43. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with the second generator (18), second generator (18) also has condensate liquid pipeline and ft connection, the finisher (13) that engine (10) also has the second steam channel to be communicated with generator (12) and evaporimeter (13) successively has the second condensate liquid pipeline and ft connection again, engine (10) also has the 3rd steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection, generator (12) also has concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline to be communicated with generator (12) with solution heat exchanger (6) through the second solution heat exchanger (16), generator (12) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has weak solution pipeline through the 3rd solution pump (25), 3rd solution heat exchanger (26) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have concentrated solution pipeline to be communicated with the 4th absorber (24) through the 3rd solution heat exchanger (26), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, condenser (3) also has cryogen liquid pipeline the 3rd absorber (21) after the second cryogen liquid pump (19) is communicated with the 3rd absorber (21) to have refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 44. heat, move in co-feeding system in heat according to claim 43, cancel evaporimeter, had by engine (10) the second steam channel to be communicated with successively finisher (13) that generator (12) is communicated with evaporimeter (13) have again the second condensate liquid pipeline and ft connection be adjusted to engine (10) have the second steam channel be communicated with generator (12) after generator (12) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (13) refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) to be respectively adjusted to engine (10) to set up the second steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 45. heat, formed primarily of absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, the second generator, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, engine (10) or in addition exhaust passage and ft connection, engine (10) also has exhaust passage to be communicated with the second generator (18), second generator (18) also has condensate liquid pipeline and ft connection, engine (10) also have the second steam channel be communicated with generator (12) after generator (12) have the second condensate liquid pipeline and ft connection again, the finisher (13) that engine (10) also has the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, engine (10) also has the 4th steam channel to be communicated with heat exchanger (9), heat exchanger (9) also has the 4th condensate liquid pipeline and ft connection, generator (12) also has concentrated solution pipeline to be communicated with absorber (2) with solution heat exchanger (6) through solution pump (4), absorber (2) also has weak solution pipeline to be communicated with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be communicated with the second absorber (14) with the second solution heat exchanger (16) through the second solution pump (15), second absorber (14) also has weak solution pipeline to be communicated with generator (12) with solution heat exchanger (6) through the second solution heat exchanger (16), generator (12) also has refrigerant steam channel to be communicated with the 4th absorber (24), 4th absorber (24) also has weak solution pipeline through the 3rd solution pump (25), 3rd solution heat exchanger (26) is communicated with a point steam chest (8) with generator (12), steam chest (8) is divided to also have concentrated solution pipeline to be communicated with the 4th absorber (24) through the 3rd solution heat exchanger (26), steam chest (8) is divided to also have refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5), evaporimeter (13) also has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, condenser (3) also has cryogen liquid pipeline the 3rd absorber (21) after the second cryogen liquid pump (19) is communicated with the 3rd absorber (21) to have refrigerant steam channel to be communicated with the second absorber (14) again, condenser (3) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 46. heat, move in co-feeding system in heat according to claim 45, cancel evaporimeter, the finisher (13) being had by engine (10) the 3rd steam channel to be communicated with evaporimeter (13) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with the 3rd absorber (21) with absorber (2) to be respectively adjusted to engine (10) in the lump has the 3rd steam channel to be communicated with the 3rd absorber (21) with absorber (2) respectively, had by condenser (3) cryogen liquid pipeline to be communicated with evaporimeter (13) through cryogen liquid pump (5) to be adjusted to condenser (3) and to have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 47. heat, that arbitrary heat described in claim 1-2,5-6,17-18,21-23,32-33,39-40 is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger (9), cancel the second steam channel be communicated with heat exchanger (9), cancel the second condensate liquid pipeline be communicated with heat exchanger (9), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, that arbitrary heat described in claim 3-4,7-12,19-20,24-27,30-31,34-38,41-44 is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger (9), cancel the 3rd steam channel be communicated with heat exchanger (9), cancel the 3rd condensate liquid pipeline be communicated with heat exchanger (9), form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, that arbitrary heat described in claim 13-16,28-29,45-46 is moved in co-feeding system, cancel heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger (9), cancel the 4th steam channel be communicated with heat exchanger (9), cancel the 4th condensate liquid pipeline be communicated with heat exchanger (9), form the dynamic co-feeding system of heat.
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