CN104748439A - Heat and power combined supplying system - Google Patents

Heat and power combined supplying system Download PDF

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Publication number
CN104748439A
CN104748439A CN201510043152.4A CN201510043152A CN104748439A CN 104748439 A CN104748439 A CN 104748439A CN 201510043152 A CN201510043152 A CN 201510043152A CN 104748439 A CN104748439 A CN 104748439A
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China
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communicated
generator
absorber
evaporimeter
pipeline
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CN201510043152.4A
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CN104748439B (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
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00—Climate change mitigation technologies for sector-wide applications
    • Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
    • Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

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

Abstract

The invention provides a heat and power combined supplying system and belongs to the technical field of heat and power combined supplying and heating pumps. A power machine is used for providing exhaust steam for a generator, an evaporator and a second generator, and further used for providing second steam for a heat exchanger, the second generator is communicated with an absorber through a second solution pump and a solution heat exchanger, the absorber is further communicated with a second absorber through the solution heat exchanger, the second absorber is communicated with the generator through a solution pump, the generator is communicated with the second generator through a solution throttling valve, the second generator is used for providing refrigerant steam for the second absorber, the generator is provided with a refrigerant steam channel to be communicated with a condenser, the condenser is communicated with the evaporator through a refrigerant pump, the evaporator is provided with a refrigerant steam channel to be communicated with the absorber, the condenser and the second absorber are provided with cooling medium pipelines respectively to be communicated with the outside, the absorber and the heat exchanger are provided with heated medium pipelines respectively to be communicated with the outside, and thus the heat and power combined supplying system is formed.

Description

The dynamic co-feeding system of heat
Technical field:
The invention belongs to the dynamic alliance of heat and technical field of heat pumps.
Background technology:
Doing in the thermodynamic cycle device of circulatory mediator with steam, for making engine (steam turbine) have higher internal heat efficiency and increase its property safe and reliable to operation, then requiring that the pressure and temperature of engine outlet steam discharge can not be too low; In the time so in the winter time, environment temperature is lower, and engine outlet exhaust temperature is higher, then the temperature difference of 40 DEG C even higher of will having an appointment therebetween can not be used; Moreover be in the Steam Power Circulation system of representative with Thermal Power Station, although the grade of steam discharge is very low, its thermic load also had is often very abundant, if effectively utilize then significant in addition.
The existing heat for winter heating moves alliance, and also or have the heat of other heat supply purposes to move alliance, corresponding technical scheme generally comprises: (1) is improved engine outlet steam discharge parameter and carried out heat supply; (2) utilize engine intermediate extraction or segmentation to draw gas and carry out heat supply; (3) engine intermediate extraction is adopted to be that the high temperature heat source of first-class absorption type heat pump carrys out recovery section exhaust steam heat and carries out heat supply.But, making full use of all not to cold environment in the dynamic jointly-supplying technology measure of these heat.
Adopt the second-kind absorption-type heat pump principle with regenerative cooling end, make full use of the temperature difference between engine steam discharge and cold environment further, 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, steam discharge contain owing to relating to heat user thermal parameter and thermic load, between steam discharge 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine and working machine, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator, evaporimeter and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser 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.
2. the dynamic co-feeding system of heat, that heat described in the 1st is moved in co-feeding system, cancel evaporimeter, exhaust passage is had to be communicated with generator successively in engine, evaporimeter and the second generator after the second generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage and generator be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up exhaust passage to be communicated with absorber, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, that heat described in the 1st is moved in co-feeding system, exhaust passage is had to be communicated with generator successively in engine, evaporimeter and the second generator after the second generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage and generator be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection to be adjusted to engine again has the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, the rear heat exchange that the 3rd steam channel is communicated with heat exchanger set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, that heat described in the 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine and the second solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage and the second generator after the second generator have condensate liquid pipeline and ft connection again, the finisher that engine also has the second steam channel to be communicated with generator and evaporimeter successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange that engine also has the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator with the second solution heat exchanger through solution pump, generator also has concentrated 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 the second absorber, generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser 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, cancel evaporimeter, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with 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.
7. the dynamic co-feeding system of heat, that heat described in the 5th is moved in co-feeding system, engine have the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange that the 4th steam channel is communicated with heat exchanger set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, that heat described in the 7th 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.
9. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the 3rd generator, generator, evaporimeter and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator with the second solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the second solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser, second absorber and the 3rd 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, cancel evaporimeter, exhaust passage is had by engine to be communicated with the 3rd generator successively, generator, evaporimeter and the second generator after the second generator have condensate liquid pipeline and ft connection to be adjusted to engine again has exhaust passage to be communicated with the 3rd generator successively, after generator and the second generator, the second generator has condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up exhaust passage to be communicated with absorber, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, that heat described in the 9th is moved in co-feeding system, exhaust passage is had by engine to be communicated with the 3rd generator successively, generator, evaporimeter and the second generator after the second generator have condensate liquid pipeline and ft connection to be adjusted to engine again has exhaust passage to be communicated with the 3rd generator successively, after generator and the second generator, the second generator has condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection to be adjusted to engine again has the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, the rear heat exchange that the 3rd steam channel is communicated with heat exchanger set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, that heat described in the 11st 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 13. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the 3rd generator and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, the finisher that engine also has the second steam channel to be communicated with generator and evaporimeter successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange that engine also has the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator with the second solution heat exchanger through solution pump, generator also has concentrated 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 the second absorber, generator also has refrigerant steam channel to be communicated with the 3rd absorber, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser, second absorber and the 3rd 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, engine is had the second steam channel be communicated with successively generator and with the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel to be communicated with generator after steam generator have the second condensate liquid pipeline and ft connection again, there is by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to and engine is set up the second steam channel 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 15. heat, that heat described in the 13rd is moved in co-feeding system, engine is had the second steam channel be communicated with successively generator and with the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel to be communicated with generator after steam generator have the second condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange that the 4th steam channel is communicated with heat exchanger set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, that heat described in the 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator, generator, evaporimeter and the 3rd generator successively after the 3rd generator have condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection again, 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 generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd generator through solution choke valve, 3rd generator also has concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with the 3rd absorber, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser, second absorber and the 3rd 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, cancel evaporimeter, exhaust passage is had by engine to be communicated with the second generator successively, generator, evaporimeter and the 3rd generator after the 3rd generator have condensate liquid pipeline and ft connection to be adjusted to engine again has exhaust passage to be communicated with the second generator successively, after generator and the 3rd generator, the 3rd generator has condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up exhaust passage to be communicated with absorber, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, that heat described in the 17th is moved in co-feeding system, exhaust passage is had by engine to be communicated with the second generator successively, generator, evaporimeter and the 3rd generator after the 3rd generator have condensate liquid pipeline and ft connection to be adjusted to engine again has exhaust passage to be communicated with the second generator successively, after generator and the 3rd generator, the 3rd generator has condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection to be adjusted to engine again has the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, the rear heat exchange that the 3rd steam channel is communicated with heat exchanger set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, that heat described in the 19th 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 21. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator and the 3rd generator successively after the 3rd generator have condensate liquid pipeline and ft connection again, the finisher that engine also has the second steam channel to be communicated with generator and evaporimeter successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange that engine also has the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection again, 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 generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator through the 3rd solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd generator through solution choke valve, 3rd generator also has concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with the 3rd absorber, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser, second absorber and the 3rd 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 22. heat, that heat described in the 21st is moved in co-feeding system, cancel evaporimeter, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with 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 23. heat, that heat described in the 21st is moved in co-feeding system, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange that the 4th steam channel is communicated with heat exchanger set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, that heat described in the 23rd 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 25. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the 3rd generator after the 3rd generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with generator and the second generator successively 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, the rear heat exchange that engine also has the 4th steam channel to be communicated with heat exchanger has the 4th condensate liquid pipeline and ft connection again, 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 generator through solution heat exchanger, generator also has refrigerant steam channel to be communicated with the second absorber, second absorber also has weak solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the 3rd solution pump, second generator also has concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has concentrated solution pipeline to be communicated with the second absorber through the second solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with the 3rd absorber, second generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, condenser, second absorber and the 3rd 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 26. heat, that heat described in the 25th 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 27. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporimeter and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator, evaporimeter, the second evaporimeter and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the second solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, that heat described in the 27th is moved in co-feeding system, cancel evaporimeter, exhaust passage is had to be communicated with generator successively in engine, evaporimeter, second evaporimeter and the second generator after the second generator have condensate liquid pipeline and ft connection to be adjusted to engine again has exhaust passage to be communicated with generator successively, after second evaporimeter and the second generator, the second generator has condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up exhaust passage to be communicated with absorber, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid 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 27th is moved in co-feeding system, exhaust passage is had to be communicated with generator successively in engine, evaporimeter, second evaporimeter and the second generator after the second generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with generator and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, the rear heat exchange being had by engine the second steam channel to be communicated with heat exchanger have again the second condensate liquid pipeline and ft connection be adjusted to engine 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, the rear heat exchange that the 3rd steam channel is communicated with heat exchanger set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, that heat described in the 29th 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, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporimeter and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection again, 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, the rear heat exchange that engine also has the 4th steam channel to be communicated with heat exchanger has the 4th condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the second solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, that heat described in the 31st 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, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 33. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with generator, evaporimeter and the second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator with the second solution heat exchanger through solution pump, generator also has concentrated 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 the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 34. heat, that heat described in the 33rd is moved in co-feeding system, cancel evaporimeter, the second steam channel is had by engine to be communicated with generator successively, evaporimeter and the second evaporimeter after the second evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator and the second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up the second steam channel to be communicated with absorber, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid 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 33rd is moved in co-feeding system, the second steam channel is had by engine to be communicated with generator successively, evaporimeter and the second evaporimeter after the second evaporimeter have the second condensate liquid pipeline and ft connection to be adjusted to engine again and have the second steam channel to be communicated with generator after generator is communicated with successively to have the second condensate liquid pipeline and ft connection again, the rear heat exchange being had by engine the 3rd steam channel to be communicated with heat exchanger have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine have the 3rd steam channel be communicated with evaporimeter and the second steam successively after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange that the 4th steam channel is communicated with heat exchanger set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 36. heat, that heat described in the 35th is moved in co-feeding system, cancel evaporimeter, engine is had the 3rd steam channel be communicated with successively evaporimeter and the second evaporimeter after the second evaporimeter have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up the 3rd steam channel to be communicated with absorber, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 37. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, engine also have the 3rd steam channel be communicated with the second evaporimeter after the second evaporimeter have the 3rd condensate liquid pipeline and ft connection again, engine also has the finisher of the 4th steam channel and evaporimeter to have the 4th condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the 5th steam channel to be communicated with heat exchanger has the 5th condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator with the second solution heat exchanger through solution pump, generator also has concentrated 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 the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, evaporimeter also has refrigerant steam channel to be communicated with absorber, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 38. heat, that heat described in the 37th is moved in co-feeding system, cancel evaporimeter, the finisher being had by engine the 4th steam channel to be communicated with evaporimeter has the 4th 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 4th steam channel to be communicated with absorber, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with generator, evaporimeter and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through solution choke valve, second generator also has refrigerant steam channel to be communicated with the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the second solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber with absorber respectively, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 40. heat, that heat described in the 39th is moved in co-feeding system, cancel evaporimeter, exhaust passage is had to be communicated with generator successively in engine, evaporimeter and the second generator after the second generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with generator and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine to set up exhaust passage to be communicated with the 3rd absorber with absorber respectively, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, that heat described in the 39th is moved in co-feeding system, exhaust passage is had to be communicated with generator successively in engine, evaporimeter and the second generator after the second generator have again condensate liquid pipeline and ft connection be adjusted to engine have exhaust passage be communicated with generator and the second generator successively after the second generator have condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the second steam channel to be communicated with heat exchanger has the second condensate liquid pipeline and ft connection to be adjusted to engine again has the second steam channel to be communicated with evaporimeter has the second condensate liquid pipeline and ft connection again, the rear heat exchange that the 3rd steam channel is communicated with heat exchanger set up by engine the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 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 again, evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine in the lump has the second steam channel to be communicated with the 3rd absorber with absorber respectively, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 43. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, the finisher that engine also has the second steam channel to be communicated with generator and evaporimeter successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange that engine also has the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection again, second generator also has concentrated solution pipeline to be communicated with absorber with solution heat exchanger through the second 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 generator with the second solution heat exchanger through solution pump, generator also has concentrated 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 the second absorber, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, second cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the 3rd solution heat exchanger through the 3rd solution pump, 3rd absorber also has weak solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, and evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber with absorber respectively, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, and 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, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have second 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, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 45. heat, that heat described in the 43rd is moved in co-feeding system, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have second channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange that the 4th steam channel is communicated with heat exchanger set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 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 again, evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine has the 3rd 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, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 47. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, engine also have the second steam channel be communicated with generator, evaporimeter and the second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, the rear heat exchange that engine also has the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection again, 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 generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through the second cryogen liquid pump again, evaporimeter also has refrigerant steam channel to be communicated with absorber, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second absorber through the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through cryogen liquid pump, second evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, and heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, that heat described in the 47th is moved in co-feeding system, cancel evaporimeter, the second steam channel is had by engine to be communicated with generator successively, evaporimeter and the second evaporimeter after the second evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator and the second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to engine to set up the second steam channel to be communicated with absorber, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, that heat described in the 47th is moved in co-feeding system, the second steam channel is had by engine to be communicated with generator successively, evaporimeter and the second evaporimeter after the second evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator and the second evaporimeter successively after the second evaporimeter have the second condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange that the 4th steam channel is communicated with heat exchanger set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 50. heat, that heat described in the 49th 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, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 51. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine connects working machine, engine has live steam passage and ft connection, engine or in addition exhaust passage and ft connection, engine also have exhaust passage be communicated with the second generator after the second generator have condensate liquid pipeline and ft connection again, the finisher that engine also has the second steam channel to be communicated with generator and evaporimeter successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange that engine also has the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection again, 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 generator through solution heat exchanger, generator also have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump again, the second cryogen liquid pump also has cryogen liquid pipeline to be communicated with evaporimeter, second generator also has concentrated solution pipeline to be communicated with the 3rd absorber with the second solution heat exchanger through the second solution pump, 3rd absorber also has weak solution pipeline to be communicated with the second absorber through the second solution heat exchanger, second absorber also has weak solution pipeline to be communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, second generator also has refrigerant steam channel to be communicated with the second absorber, 3rd generator also has refrigerant steam channel to be communicated with condenser, condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with the 3rd absorber with absorber respectively, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, and heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 52. heat, that heat described in the 51st is moved in co-feeding system, cancel evaporimeter, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, had by evaporimeter refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine to set up the second steam channel to be communicated with the 3rd absorber with absorber respectively, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 53. heat, that heat described in the 51st is moved in co-feeding system, engine is had the second steam channel be communicated with successively generator and the finisher of evaporimeter have again the second condensate liquid pipeline and ft connection be adjusted to engine have the second steam channel be communicated with generator after generator have the second condensate liquid pipeline and ft connection again, the finisher that the rear heat exchange being had by engine the 3rd steam channel to be communicated with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again has the 3rd steam channel to be communicated with evaporimeter has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange that the 4th steam channel is communicated with heat exchanger set up by engine the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 54. heat, that heat described in the 53rd 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 again, evaporimeter has refrigerant steam channel to be communicated with the 3rd absorber with absorber to be respectively adjusted to engine has the 3rd steam channel to be communicated with the 3rd absorber with absorber respectively, being had by second cryogen liquid pump cryogen liquid pipeline to be communicated with evaporimeter to be adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, had by condenser cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump to be adjusted to condenser and to have cryogen liquid pipeline through cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 55. heat is the 1st, 3, 5, 7, 9, 11, 13, arbitrary heat described in 15 is moved in co-feeding system, increases newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution heat exchanger again, evaporimeter is set up refrigerant steam channel and is communicated with newly-increased absorber, cryogen liquid pipeline newly-increased absorber after newly-increased cryogen liquid pump is communicated with newly-increased absorber set up by condenser has refrigerant steam channel to be communicated with newly-increased second absorber again, newly-increased second absorber also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 56. heat, the 17th, 19, 21, 26, arbitrary heat described in 25 is moved in co-feeding system, increase newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with generator through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber has weak solution pipeline to be communicated with generator with solution heat exchanger through newly-increased solution heat exchanger again, evaporimeter is set up refrigerant steam channel and is communicated with newly-increased absorber, cryogen liquid pipeline newly-increased absorber after newly-increased cryogen liquid pump is communicated with newly-increased absorber set up by condenser has refrigerant steam channel to be communicated with newly-increased second absorber again, newly-increased second absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 57. heat is the 27th, 29, 31, 33, 35, 37, 39, 41, 43, 45, 47, 49, arbitrary heat described in 51 is moved in co-feeding system, increases newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, had by absorber weak solution pipeline to be communicated with the second absorber through solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased second absorber with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased second absorber has weak solution pipeline to be communicated with the second absorber with solution heat exchanger through newly-increased solution heat exchanger again, evaporimeter is set up refrigerant steam channel and is communicated with newly-increased absorber, generator is had refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with the second cryogen liquid pump to be again adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with newly-increased cryogen liquid pump with the second cryogen liquid pump respectively again, newly-increased cryogen liquid pump also have cryogen liquid pipeline be communicated with newly-increased absorber after increase absorber newly and have refrigerant steam channel to be communicated with newly-increased second absorber again, newly-increased second absorber also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 58. heat, is that the arbitrary heat described in 1-57 item is moved in co-feeding system, cancels heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger, forms the dynamic co-feeding system of heat.
Accompanying drawing illustrates:
Fig. 1 moves co-feeding system the 1st kind of principled thermal system figure according to heat provided by the present invention.
Fig. 2 moves co-feeding system the 2nd kind of principled thermal system figure according to heat provided by the present invention.
Fig. 3 moves co-feeding system the 3rd kind of principled thermal system figure according to heat provided by the present invention.
Fig. 4 moves co-feeding system the 4th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 5 moves co-feeding system the 5th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 6 moves co-feeding system the 6th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 7 moves co-feeding system the 7th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 8 moves co-feeding system the 8th kind of principled thermal system figure according to heat provided by the present invention.
Fig. 9 moves co-feeding system the 9th kind of principled thermal system figure according to heat provided by the present invention.
Figure 10 moves co-feeding system the 10th kind of principled thermal system figure according to heat provided by the present invention.
Figure 11 moves co-feeding system the 11st kind of principled thermal system figure according to heat provided by the present invention.
Figure 12 moves co-feeding system the 12nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 13 moves co-feeding system the 13rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 14 moves co-feeding system the 14th kind of principled thermal system figure according to heat provided by the present invention.
Figure 15 moves co-feeding system the 15th kind of principled thermal system figure according to heat provided by the present invention.
Figure 16 moves co-feeding system the 16th kind of principled thermal system figure according to heat provided by the present invention.
Figure 17 moves co-feeding system the 17th kind of principled thermal system figure according to heat provided by the present invention.
Figure 18 moves co-feeding system the 18th kind of principled thermal system figure according to heat provided by the present invention.
Figure 19 moves co-feeding system the 19th kind of principled thermal system figure according to heat provided by the present invention.
Figure 20 moves co-feeding system the 20th kind of principled thermal system figure according to heat provided by the present invention.
Figure 21 moves co-feeding system the 21st kind of principled thermal system figure according to heat provided by the present invention.
Figure 22 moves co-feeding system the 22nd kind of principled thermal system figure according to heat provided by the present invention.
Figure 23 moves co-feeding system the 23rd kind of principled thermal system figure according to heat provided by the present invention.
Figure 24 moves co-feeding system the 24th kind of principled thermal system figure according to heat provided by the present invention.
Figure 25 moves co-feeding system the 25th kind of principled thermal system figure according to heat provided by the present invention.
Figure 26 moves co-feeding system the 26th kind of principled thermal system figure according to heat provided by the present invention.
Figure 27 moves co-feeding system the 27th kind of principled thermal system figure according to heat provided by the present invention.
Figure 28 moves co-feeding system the 28th kind of principled thermal system figure according to heat provided by the present invention.
In figure, 1-generator, 2-second generator, 3-absorber, 4-second absorber, 5-condenser, 6-evaporimeter, 7-solution pump, 8-second solution pump, 9-cryogen liquid pump, 10-solution choke valve, 11-solution heat exchanger, 12-heat exchanger, 13-engine, 14-working machine, 15-second solution heat exchanger, 16-the 3rd generator, 17-the 3rd absorber, 18-the 3rd solution pump, 19-the 3rd solution heat exchanger, 20-second evaporimeter, 21-second cryogen liquid pump; A-increases absorber newly, and B-increases the second absorber newly, and C-increases solution pump newly, and D-increases cryogen liquid pump newly, and E-increases solution heat exchanger newly.
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 exit working media, as the low-pressure steam in steam turbine outlet moist steam.
(3) second steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of steam discharge.
(4) the 3rd steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the second steam.
(4) the 4th steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the 3rd steam.
(5) the 5th steam---that a certain position of engine is extracted out, pressure and temperature is all higher than the working media of the 4th steam.
(6) liquid that condensate liquid---steam discharge exothermic condensation is formed.
(7) second condensate liquids---the liquid that the second steam exothermic condensation is formed.
(8) the 3rd condensate liquids---the liquid that the 3rd steam exothermic condensation is formed.
(9) the 4th condensate liquids---the liquid that the 4th steam exothermic condensation is formed.
(10) the 5th condensate liquids---the liquid that the 5th steam exothermic condensation is formed.
(11) relevant with engine, but do not relate to operation principle of the present invention, parts unrelated to the invention (as dynamical system backheat heat exchanger components etc.) and flow process (recovery etc. as condensate liquid), not in express ranges of the present invention.
(12) 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.
(13) 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.
(14) effect of choke valve and solution choke valve---for fluid step-down, can be replaced by gravity pressure reduction or pipe resistance.
(15) for Figure 14, the circulation be made up of the 3rd generator 16, the 3rd absorber 17, the 3rd solution pump 18, second solution heat exchanger 15, condenser 5, cryogen liquid pump 9 and the second evaporimeter 20, when making working medium with ammonia-aqueous solution, 3rd generator is referred to as rectifying column by custom---and now as required, the 3rd generator 16 sets up cooling medium pipeline and ft connection.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, do not repeat in inessential situation; Apparent flow process is not stated.The present invention is described in detail below in conjunction with accompanying drawing and example.
Heat shown in Fig. 1 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine and working machine, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also has exhaust passage and ft connection, engine 13 also has exhaust passage to be communicated with the second generator 2 after generator 1, evaporimeter 6 and the second generator 2 successively and has condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through solution choke valve 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, absorber 3 also has heated medium pipeline and ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the second steam, the heat release in heat exchanger 12 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides steam discharge to generator 1, evaporimeter 6 and the second generator 2, steam discharge flows through generator 1, evaporimeter 6 and the second generator 2 and progressively heat release is discharged after becoming condensate liquid, and engine 13 also has steam discharge to discharge; The concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour and heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7, absorbing heat discharges refrigerant vapour and provide to condenser 5, and generator 1 concentrated solution enters the second generator 2 through solution choke valve 10 reducing pressure by regulating flow, heat absorption discharges refrigerant vapour and provides to the second absorber 4; The refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 2 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 1, exhaust passage is had to be communicated with generator 1 successively in engine 13, after evaporimeter 6 and the second generator 2 second generator 2 have again condensate liquid pipeline and ft connection be adjusted to engine 13 have exhaust passage and generator 1 be communicated with the second generator 2 after the second generator 2 have condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 3rd steam channel is communicated with heat exchanger 12 set up by engine 13 the 3rd condensate liquid pipeline and ft connection again, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine and the second solution heat exchanger, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage and the second generator 2 after the second generator 2 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with generator 1 and evaporimeter 6 successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 with the second solution heat exchanger 15 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 15, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, absorber 3 also has heated medium pipeline and ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 3rd steam, the heat release in heat exchanger 12 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with evaporimeter 6, heat release through generator 1, engine 13 provides steam discharge to the second generator 2, and steam discharge heat release in the second generator 2 is discharged after becoming condensate liquid, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7 and the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to condenser 5, generator 1 concentrated solution enters the second generator 2 through the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to the second absorber 4, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 4 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 3, engine 13 have the second steam channel be communicated with successively generator 1 and the finisher 6 of evaporimeter 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel be communicated with generator 1 after generator 1 have the second condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 4th steam channel is communicated with heat exchanger 12 set up by engine 13 the 4th condensate liquid pipeline and ft connection again, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also has exhaust passage to be communicated with the second generator 2 after the 3rd generator 16, generator 1, evaporimeter 6 and the second generator 2 successively and has condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through solution choke valve 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with the 3rd absorber 17, 3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 with the second solution heat exchanger 15 through the 3rd solution pump 18, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 through the second solution heat exchanger 15, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5, second absorber 4 and the 3rd absorber 17 also have cooling medium pipeline and ft connection respectively, absorber 3 also has heated medium pipeline and ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the second steam, the heat release in heat exchanger 12 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides steam discharge to the 3rd generator 16, generator 1, evaporimeter 6 and the second generator 2, and steam discharge flows through the 3rd generator 16, generator 1, evaporimeter 6 and the second generator 2 and progressively heat release is discharged after becoming condensate liquid; The concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour and heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7, absorbing heat discharges refrigerant vapour and provide to the 3rd absorber 17, and the concentrated solution of generator 1 enters the second generator 2 through solution choke valve 10, absorbing heat discharges refrigerant vapour and provide to the second absorber 4; The weak solution of the 3rd absorber 17 enters the 3rd generator 16, heat absorption release refrigerant vapour providing to condenser 5 through the 3rd solution pump 18 and the second solution heat exchanger 15, the concentrated solution of the 3rd generator 16 enters the 3rd absorber 17 through the second solution heat exchanger 15, absorb refrigerant vapour and heat release in cooling medium; The refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 6 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 5, exhaust passage is had by engine 13 to be communicated with the 3rd generator 16 successively, generator 1, evaporimeter 6 has condensate liquid pipeline and ft connection to be adjusted to engine 13 with the second generator 2 after the second generator 2 again has exhaust passage to be communicated with the 3rd generator 16 successively, generator 1 and the second generator 2 afterwards the second generator 2 have condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 3rd steam channel is communicated with heat exchanger 12 set up by engine 13 the 3rd condensate liquid pipeline and ft connection again, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the 3rd generator 16 and the second generator 2 successively after the second generator 2 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with generator 1 and evaporimeter 6 successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 with the second solution heat exchanger 15 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 15, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also has refrigerant steam channel to be communicated with the 3rd absorber 17, 3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 with the 3rd solution heat exchanger 19 through the 3rd solution pump 18, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 through the 3rd solution heat exchanger 19, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5, second absorber 4 and the 3rd absorber 17 also have cooling medium pipeline and ft connection respectively, absorber 3 also has heated medium pipeline and ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 3rd steam, the heat release in heat exchanger 12 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream is through generator 1 and evaporimeter 6, heat release is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 13 provides steam discharge to the 3rd generator 16 and the second generator 2, steam discharge flows through the 3rd generator 16 and the second generator 2, progressively heat release is discharged after becoming condensate liquid, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7 and the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to the 3rd absorber 17, the concentrated solution of generator 1 enters the second generator 2 through the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to the second absorber 4, the weak solution of the 3rd absorber 17 enters the 3rd generator 16, heat absorption release refrigerant vapour providing to condenser 5 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, the concentrated solution of the 3rd generator 16 enters the 3rd absorber 17 through the 3rd solution heat exchanger 19, absorb refrigerant vapour and heat release in cooling medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 8 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 7, engine 13 is had the second steam channel be communicated with successively generator 1 and with the finisher 6 of evaporimeter 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel to be communicated with generator 1 after steam generator 1 have the second condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 4th steam channel is communicated with heat exchanger 12 set up by engine 13 the 4th condensate liquid pipeline and ft connection again, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also has exhaust passage to be communicated with the 3rd generator 16 after the second generator 2, generator 1, evaporimeter 6 and the 3rd generator 16 successively and has condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection again, generator 1 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through solution pump 7, absorber 3 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 11, generator 1 also has refrigerant steam channel to be communicated with the second absorber 4, second absorber 4 also has weak solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the second solution pump 8, 3rd absorber 17 also has weak solution pipeline to be communicated with the second generator 2 through the 3rd solution pump 18, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd generator 16 through solution choke valve 10, 3rd generator 16 also has concentrated solution pipeline to be communicated with the second absorber 4 through the second solution heat exchanger 15, 3rd generator 16 also has refrigerant steam channel to be communicated with the 3rd absorber 17, second generator 2 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5, second absorber 4 and the 3rd absorber 17 also have cooling medium pipeline and ft connection respectively, absorber 3 also has heated medium pipeline and ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the second steam, the heat release in heat exchanger 12 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides steam discharge to the second generator 2, generator 1, evaporimeter 6 and the 3rd generator 16, and steam discharge flows through the second generator 2, generator 1, evaporimeter 6 and the 3rd generator 16 and progressively heat release is discharged after becoming condensate liquid, the concentrated solution of generator 1 enters absorber 3 through solution pump 7 and solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 enters generator 1, heat absorption release refrigerant vapour providing to the second absorber 4 through solution heat exchanger 11, the weak solution of the second absorber 4 enters the 3rd absorber 17 through the second solution pump 8 and the second solution heat exchanger 15, absorb refrigerant vapour heat release in cooling medium, the weak solution of the 3rd absorber 17 enters the second generator 2 through the 3rd solution pump 18, absorb release refrigerant vapour and provide to condenser 5, the concentrated solution of the second generator 2 enters the 3rd generator 16 through solution choke valve 10 throttling, heat absorption release refrigerant vapour also provides to the 3rd absorber 17, the concentrated solution of the 3rd generator 16 enters the second absorber 4 through the second solution heat exchanger 15, absorb refrigerant vapour heat release in cooling medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Figure 10 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Fig. 9, exhaust passage is had by engine 13 to be communicated with the second generator 2 successively, generator 1, evaporimeter 6 has condensate liquid pipeline and ft connection to be adjusted to engine 13 with the 3rd generator 16 after the 3rd generator 16 again has exhaust passage to be communicated with the second generator 2 successively, generator 1 and the 3rd generator 16 afterwards the 3rd generator 16 have condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 3rd steam channel is communicated with heat exchanger 12 set up by engine 13 the 3rd condensate liquid pipeline and ft connection again, form 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the second generator 2 and the 3rd generator 16 successively after the 3rd generator 16 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with generator 1 and evaporimeter 6 successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again, generator 1 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through solution pump 7, absorber 3 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 11, generator 1 also has refrigerant steam channel to be communicated with the second absorber 4, second absorber 4 also has weak solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the second solution pump 8, 3rd absorber 17 also has weak solution pipeline to be communicated with the second generator 2 through the 3rd solution pump 18, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd generator 16 through solution choke valve 10, 3rd generator 16 also has concentrated solution pipeline to be communicated with the second absorber 4 through the second solution heat exchanger 15, 3rd generator 16 also has refrigerant steam channel to be communicated with the 3rd absorber 17, second generator 2 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5, second absorber 4 and the 3rd absorber 17 also have cooling medium pipeline and ft connection respectively, absorber 3 also has heated medium pipeline and ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Figure 10, difference is: engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream becomes through the second condensate liquid pipeline discharge after condensate liquid with evaporimeter 6, progressively heat release through generator 1, and engine 13 provides steam discharge to the second generator 2 and the 3rd generator 16.
Heat shown in Figure 12 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 11, engine 13 is had the second steam channel be communicated with successively generator 1 and the finisher 6 of evaporimeter 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel be communicated with generator 1 after generator 1 have the second condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 4th steam channel is communicated with heat exchanger 12 set up by engine 13 the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
Heat shown in Figure 13 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the 3rd generator 16 after the 3rd generator 16 have condensate liquid pipeline and ft connection again, engine 13 also have the second steam channel be communicated with generator 1 and the second generator 2 successively after the second generator 2 have the second condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that engine 13 also has the 4th steam channel to be communicated with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again, generator 1 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through solution pump 7, absorber 3 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 11, generator 1 also has refrigerant steam channel to be communicated with the second absorber 4, second absorber 4 also has weak solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the second solution pump 8, 3rd absorber 17 also has weak solution pipeline to be communicated with the second generator 2 with the 3rd solution heat exchanger 19 through the 3rd solution pump 18, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd generator 16 through the 3rd solution heat exchanger 19, 3rd generator 16 also has concentrated solution pipeline to be communicated with the second absorber 4 through the second solution heat exchanger 15, 3rd generator 16 also has refrigerant steam channel to be communicated with the 3rd absorber 17, second generator 2 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, condenser 5, second absorber 4 and the 3rd absorber 17 also have cooling medium pipeline and ft connection respectively, absorber 3 also has heated medium pipeline and ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 4th steam, the heat release in heat exchanger 12 of 4th steam is discharged through the 4th condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides the 3rd steam to evaporimeter 6, the heat release in evaporimeter 6 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, engine 13 provides the second steam to generator 1 and the second generator 2, second vapor stream is through generator 1 and the second generator 2, progressively heat release is discharged through the second condensate liquid pipeline after becoming condensate liquid, engine 13 provides steam discharge to the 3rd generator 16, steam discharge heat release in the 3rd generator 16 is discharged after becoming condensate liquid, the concentrated solution of generator 1 enters absorber 3 through solution pump 7 and solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 enters generator 1, heat absorption release refrigerant vapour providing to the second absorber 4 through solution heat exchanger 11, the weak solution of the second absorber 4 enters the 3rd absorber 17 through the second solution pump 8 and the second solution heat exchanger 15, absorb refrigerant vapour heat release in cooling medium, the weak solution of the 3rd absorber 17 enters the second generator 2 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, absorb release refrigerant vapour and provide to condenser 5, the concentrated solution of the second generator 2 enters the 3rd generator 16 through the 3rd solution heat exchanger 19, heat absorption release refrigerant vapour also provides to the 3rd absorber 17, the concentrated solution of the 3rd generator 16 enters the second absorber 4 through the second solution heat exchanger 15, absorb refrigerant vapour heat release in cooling medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Figure 14 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also has exhaust passage to be communicated with the second generator 2 after generator 1, evaporimeter 6, second evaporimeter 20 and the second generator 2 successively and has condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through solution choke valve 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 21 again, second cryogen liquid pump 21 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the 3rd solution pump 18, 3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 through the second solution heat exchanger 15, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 20 through cryogen liquid pump 9, second evaporimeter 20 also has refrigerant steam channel to be communicated with the 3rd absorber 17, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the second steam, the heat release in heat exchanger 12 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides steam discharge to generator 1, evaporimeter 6, second evaporimeter 20 and the second generator 2, and steam discharge flows through generator 1, evaporimeter 6, second evaporimeter 20 and the second generator 2 and progressively heat release is discharged after becoming condensate liquid, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour and heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7, absorbs heat to discharge refrigerant vapour and be supplied to the 3rd generator 16 and do to drive thermal medium, and the concentrated solution of generator 1 enters the second generator 2 through solution choke valve 10 throttling, absorbing heat discharges refrigerant vapour and provide to the second absorber 4, the concentrated solution of the 3rd generator 16 enters the 3rd absorber 17 through the 3rd solution pump 18 and the second solution heat exchanger 15, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 17 enters the 3rd generator 16 through the second solution heat exchanger 15, refrigerant vapour flows through the 3rd generator 16, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters the second evaporimeter 20 through cryogen liquid pump 9 pressurization, absorb heat into refrigerant vapour and provide to the 3rd absorber 17, evaporimeter 6 is entered through the second cryogen liquid pump 21 pressurization after the refrigerant vapour heat release flowing through the 3rd generator 16 becomes cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 3, form the dynamic co-feeding system of heat.
Heat shown in Figure 15 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 14, exhaust passage is had to be communicated with generator 1 successively in engine 13, evaporimeter 6, after second evaporimeter 20 and the second generator 2 second generator 2 have again condensate liquid pipeline and ft connection be adjusted to engine 13 have exhaust passage be communicated with successively generator 1 and the second generator 2 afterwards the second generator 2 have condensate liquid pipeline and ft connection again, the rear heat exchange 12 being had by engine 13 second steam channel to be communicated with heat exchanger 12 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel be communicated with evaporimeter 6 and the second evaporimeter 20 successively after the second evaporimeter 20 have the second condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 3rd steam channel is communicated with heat exchanger 12 set up by engine 13 the 3rd condensate liquid pipeline and ft connection again, 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with generator 1 and the second generator 2 successively after the second generator 2 have condensate liquid pipeline and ft connection again, engine 13 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 6 that engine 13 also has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that engine 13 also has the 4th steam channel to be communicated with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through solution choke valve 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 21 again, second cryogen liquid pump 21 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the 3rd solution pump 18, 3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 through the second solution heat exchanger 15, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 20 through cryogen liquid pump 9, second evaporimeter 20 also has refrigerant steam channel to be communicated with the 3rd absorber 17, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Figure 15, difference is: engine 13 heat exchanger 12 provides the 4th steam, the heat release in heat exchanger 12 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, engine 13 provides the 3rd steam to evaporimeter 6, the heat release in evaporimeter 6 of 3rd steam is discharged through the 3rd condensate liquid pipeline after becoming condensate liquid, and engine 13 provides the second steam to the second evaporimeter 20.
Heat shown in Figure 17 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the second generator 2 after the second generator 2 have condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second evaporimeter 20 after generator 1, evaporimeter 6 and the second evaporimeter 20 successively and has the second condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 with the second solution heat exchanger 15 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 15, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 21 again, second cryogen liquid pump 21 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the 3rd solution heat exchanger 19 through the 3rd solution pump 18, 3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 through the 3rd solution heat exchanger 19, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 20 through cryogen liquid pump 9, second evaporimeter 20 also has refrigerant steam channel to be communicated with the 3rd absorber 17, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 3rd steam, the heat release in heat exchanger 12 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 is to generator 1, evaporimeter 6 and the second evaporimeter 20 provide the second steam, second vapor stream is through generator 1, evaporimeter 6 and the second evaporimeter 20 and progressively heat release discharge through the second condensate liquid pipeline after becoming condensate liquid, engine 13 provides steam discharge to the second generator 2, steam discharge heat release in the second generator 2 is discharged after becoming condensate liquid, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7 and the second solution heat exchanger 15, heat absorption release refrigerant vapour is also supplied to the 3rd generator 16 do driving thermal medium, generator 1 concentrated solution enters the second generator 2 through the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the 3rd generator 16 enters the 3rd absorber 17 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 17 enters the 3rd generator 16 through the 3rd solution heat exchanger 19, refrigerant vapour flows through the 3rd generator 16, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters the second evaporimeter 20 through cryogen liquid pump 9 pressurization, absorb heat into refrigerant vapour and provide to the 3rd absorber 17, evaporimeter 6 is entered through the second cryogen liquid pump 21 pressurization after the refrigerant vapour heat release flowing through the 3rd generator 16 becomes cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 3, form the dynamic co-feeding system of heat.
Heat shown in Figure 18 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 17, the second steam channel is had to be communicated with generator 1 successively in engine 13, after evaporimeter 6 and the second evaporimeter 20, the second evaporimeter 20 has the second condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the second steam channel to be communicated with generator 1 after generator 1 is communicated with successively to have the second condensate liquid pipeline and ft connection again, the rear heat exchange 12 being had by engine 13 the 3rd steam channel to be communicated with heat exchanger 12 have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine 13 have the 3rd steam channel be communicated with evaporimeter 6 and the second steam 20 successively after the second evaporimeter 20 have the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 4th steam channel is communicated with heat exchanger 12 set up by engine 13 the 4th condensate liquid pipeline and ft connection again, 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the second generator 2 after the second generator 2 have condensate liquid pipeline and ft connection again, engine 13 also have the second steam channel be communicated with generator 1 after generator 1 have the second condensate liquid pipeline and ft connection again, engine 13 also have the 3rd steam channel be communicated with the second evaporimeter 20 after the second evaporimeter 20 have the 3rd condensate liquid pipeline and ft connection again, engine 13 also has the finisher 6 of the 4th steam channel and evaporimeter 6 to have the 4th condensate liquid pipeline and ft connection again, the rear heat exchange 12 that engine 13 also has the 5th steam channel to be communicated with heat exchanger 12 has the 5th condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 with the second solution heat exchanger 15 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 15, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 21 again, second cryogen liquid pump 21 also has cryogen liquid pipeline to be communicated with evaporimeter 6, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the 3rd solution heat exchanger 19 through the 3rd solution pump 18, 3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 through the 3rd solution heat exchanger 19, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 20 through cryogen liquid pump 9, second evaporimeter 20 also has refrigerant steam channel to be communicated with the 3rd absorber 17, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, compared with the dynamic co-feeding system of heat shown in Figure 18, difference is: engine 13 heat exchanger 12 provides the 5th steam, the heat release in heat exchanger 12 of 5th steam is discharged through the 5th condensate liquid pipeline after becoming condensate liquid, engine 13 provides the 4th steam to evaporimeter 6, the heat release in evaporimeter 6 of 4th steam is discharged through the 4th condensate liquid pipeline after becoming condensate liquid, and engine 13 provides the 3rd steam to the second evaporimeter 20.
Heat shown in Figure 20 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also has exhaust passage to be communicated with the second generator 2 after generator 1, evaporimeter 6 and the second generator 2 successively and has condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through solution choke valve 10, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 21 again, second cryogen liquid pump 21 also has cryogen liquid pipeline to be communicated with evaporimeter 6, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the 3rd solution pump 18, 3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 through the second solution heat exchanger 15, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 17 with absorber 3 respectively, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the second steam, the heat release in heat exchanger 12 of second steam is discharged through the second condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides steam discharge to generator 1, evaporimeter 6 and the second generator 2, and steam discharge flows through generator 1, evaporimeter 6 and the second generator 2 and progressively heat release is discharged after becoming condensate liquid, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7, heat absorption release refrigerant vapour is also supplied to the 3rd generator 16 do driving thermal medium, generator 1 concentrated solution enters the second generator 2 through solution choke valve 10 reducing pressure by regulating flow, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the 3rd generator 16 enters the 3rd absorber 17 through the 3rd solution pump 18 and the second solution heat exchanger 15, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 17 enters the 3rd generator 16 through the second solution heat exchanger 15, refrigerant vapour flows through the 3rd generator 16, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, evaporimeter 6 is entered through the second cryogen liquid pump 21 pressurization after the refrigerant vapour heat release flowing through the 3rd generator 16 becomes cryogen liquid, the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour and provides respectively to absorber 3 and the 3rd absorber 17, form the dynamic co-feeding system of heat.
Heat shown in Figure 21 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 20, exhaust passage is had to be communicated with generator 1 successively in engine 13, after evaporimeter 6 and the second generator 2 second generator 2 have again condensate liquid pipeline and ft connection be adjusted to engine 13 have exhaust passage be communicated with successively generator 1 and the second generator 2 afterwards the second generator 2 have condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 second steam channel to be communicated with heat exchanger 12 has the second condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the second steam channel to be communicated with evaporimeter 6 has the second condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 3rd steam channel is communicated with heat exchanger 12 set up by engine 13 the 3rd condensate liquid pipeline and ft connection again, 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 generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the second generator 2 after the second generator 2 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with generator 1 and evaporimeter 6 successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again, second generator 2 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through the second solution pump 8, absorber 3 also has weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11, second absorber 4 also has weak solution pipeline to be communicated with generator 1 with the second solution heat exchanger 15 through solution pump 7, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 15, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 21 again, second cryogen liquid pump 21 also has cryogen liquid pipeline to be communicated with evaporimeter 6, 3rd generator 16 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the 3rd solution heat exchanger 19 through the 3rd solution pump 18,3rd absorber 17 also has weak solution pipeline to be communicated with the 3rd generator 16 through the 3rd solution heat exchanger 19,3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, and evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 17 with absorber 3 respectively, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, and absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, and heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 3rd steam, the heat release in heat exchanger 12 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with evaporimeter 6, heat release through generator 1, engine 13 provides steam discharge to the second generator 2, and steam discharge heat release in the second generator 2 is discharged after becoming condensate liquid, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7 and the second solution heat exchanger 15, heat absorption release refrigerant vapour is also supplied to the 3rd generator 16 do driving thermal medium, generator 1 concentrated solution enters the second generator 2 through the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to the second absorber 4, the concentrated solution of the 3rd generator 16 enters the 3rd absorber 17 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 17 enters the 3rd generator 16 through the 3rd solution heat exchanger 19, refrigerant vapour flows through the 3rd generator 16, heating enters the solution release in it and provides refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, evaporimeter 6 is entered through the second cryogen liquid pump 21 pressurization after the refrigerant vapour heat release flowing through the 3rd generator 16 becomes cryogen liquid, the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour and provides respectively to absorber 3 and the 3rd absorber 17, form the dynamic co-feeding system of heat.
Heat shown in Figure 23 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 22, engine 13 is had the second steam channel be communicated with successively generator 1 and the finisher 6 of evaporimeter 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have second channel be communicated with generator 1 after generator 1 have the second condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 4th steam channel is communicated with heat exchanger 12 set up by engine 13 the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
Heat shown in Figure 24 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the second generator 2 after the second generator 2 have condensate liquid pipeline and ft connection again, engine 13 also has the second steam channel to be communicated with the second evaporimeter 20 after generator 1, evaporimeter 6 and the second evaporimeter 20 successively and has the second condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again, generator 1 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through solution pump 7, absorber 3 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 11, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with evaporimeter 6 through the second cryogen liquid pump 21 again, evaporimeter 6 also has refrigerant steam channel to be communicated with absorber 3, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the second solution pump 8, 3rd absorber 17 also has weak solution pipeline to be communicated with the second absorber 4 through the second solution heat exchanger 15, second absorber 4 also has weak solution pipeline to be communicated with the 3rd generator 16 with the 3rd solution heat exchanger 19 through the 3rd solution pump 18, 3rd generator 16 also has concentrated solution pipeline to be communicated with the second generator 2 through the 3rd solution heat exchanger 19, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 20 through cryogen liquid pump 9, second evaporimeter 20 also has refrigerant steam channel to be communicated with the 3rd absorber 17, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, and absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, and heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 3rd steam, the heat release in heat exchanger 12 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 is to generator 1, evaporimeter 6 and the second evaporimeter 20 provide the second steam, second vapor stream is through generator 1, evaporimeter 6 and the second evaporimeter 20 and progressively heat release discharge through the second condensate liquid pipeline after becoming condensate liquid, engine 13 provides steam discharge to the second generator 2, steam discharge heat release in the second generator 2 is discharged after becoming condensate liquid, the concentrated solution of generator 1 enters absorber 3 through solution pump 7 and solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 enters generator 1, heat absorption release refrigerant vapour be supplied to the 3rd generator 16 and do to drive thermal medium through solution heat exchanger 11, the concentrated solution of the second generator 2 enters the 3rd absorber 17 through the second solution pump 8 and the second solution heat exchanger 15, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 17 enters the second absorber 4 through the second solution heat exchanger 15, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters the 3rd generator 16 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, refrigerant vapour flows through the 3rd generator 16, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 3rd generator 16 enters the second generator 2 through the 3rd solution heat exchanger 19, heat absorption release refrigerant vapour also provides to the second absorber 4, the cryogen liquid of condenser 5 enters the second evaporimeter 20 through cryogen liquid pump 9 pressurization, absorb heat into refrigerant vapour and provide to the 3rd absorber 17, evaporimeter 6 is entered through the second cryogen liquid pump 21 pressurization after the refrigerant vapour heat release flowing through the 3rd generator 16 becomes cryogen liquid, absorb heat into refrigerant vapour and provide to absorber 3, form the dynamic co-feeding system of heat.
Heat shown in Figure 25 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 24, the second steam channel is had to be communicated with generator 1 successively in engine 13, after evaporimeter 6 and the second evaporimeter 20 second evaporimeter 20 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel be communicated with successively generator 1 and the second evaporimeter 20 afterwards the second evaporimeter 20 have the second condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 4th steam channel is communicated with heat exchanger 12 set up by engine 13 the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
Heat shown in Figure 26 is moved co-feeding system and is achieved in that
(1), in structure, it formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine 13 connects working machine 14, engine 13 has live steam passage and ft connection, engine 13 also have exhaust passage be communicated with the second generator 2 after the second generator 2 have condensate liquid pipeline and ft connection again, the finisher 6 that engine 13 also has the second steam channel to be communicated with generator 1 and evaporimeter 6 successively has the second condensate liquid pipeline and ft connection again, and the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again, generator 1 also has concentrated solution pipeline to be communicated with absorber 3 with solution heat exchanger 11 through solution pump 7, absorber 3 also has weak solution pipeline to be communicated with generator 1 through solution heat exchanger 11, generator 1 also have refrigerant steam channel be communicated with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline to be communicated with the second cryogen liquid pump 21 again, the second cryogen liquid pump 21 also has cryogen liquid pipeline to be communicated with evaporimeter 6, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd absorber 17 with the second solution heat exchanger 15 through the second solution pump 8, 3rd absorber 17 also has weak solution pipeline to be communicated with the second absorber 4 through the second solution heat exchanger 15, second absorber 4 also has weak solution pipeline to be communicated with the 3rd generator 16 with the 3rd solution heat exchanger 19 through the 3rd solution pump 18, 3rd generator 16 also has concentrated solution pipeline to be communicated with the second generator 2 through the 3rd solution heat exchanger 19, second generator 2 also has refrigerant steam channel to be communicated with the second absorber 4, 3rd generator 16 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 6 through cryogen liquid pump 9, evaporimeter 6 also has refrigerant steam channel to be communicated with the 3rd absorber 17 with absorber 3 respectively, condenser 5 and the second absorber 4 also have cooling medium pipeline and ft connection respectively, and absorber 3 and the 3rd absorber 17 also have heated medium pipeline and ft connection respectively, and heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 3rd steam, the heat release in heat exchanger 12 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with evaporimeter 6, progressively heat release through generator 1, engine 13 provides steam discharge to the second generator 2, and steam discharge heat release in the second generator 2 is discharged after becoming condensate liquid, the concentrated solution of generator 1 enters absorber 3 through solution pump 7 and solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 enters generator 1, heat absorption release refrigerant vapour be supplied to the 3rd generator 16 and do to drive thermal medium through solution heat exchanger 11, the concentrated solution of the second generator 2 enters the 3rd absorber 17 through the second solution pump 8 and the second solution heat exchanger 15, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 17 enters the second absorber 4 through the second solution heat exchanger 15, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters the 3rd generator 16 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, refrigerant vapour flows through the 3rd generator 16, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 3rd generator 16 enters the second generator 2 through the 3rd solution heat exchanger 19, heat absorption release refrigerant vapour also provides to the second absorber 4, the cryogen liquid of condenser 5 enters evaporimeter 6 through cryogen liquid pump 9 pressurization, evaporimeter 6 is entered through the second cryogen liquid pump 21 pressurization after the refrigerant vapour heat release flowing through the 3rd generator 16 becomes cryogen liquid, the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour and provides respectively to absorber 3 and the 3rd absorber 17, form the dynamic co-feeding system of heat.
Heat shown in Figure 27 is moved co-feeding system and is achieved in that
Move in co-feeding system in the heat shown in Figure 26, engine 13 is had the second steam channel be communicated with successively generator 1 and the finisher 6 of evaporimeter 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel be communicated with generator 1 after generator 1 have the second condensate liquid pipeline and ft connection again, the finisher 6 that the rear heat exchange 12 being had by engine 13 the 3rd steam channel to be communicated with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine 13 again has the 3rd steam channel to be communicated with evaporimeter 6 has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange 12 that the 4th steam channel is communicated with heat exchanger 12 set up by engine 13 the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
Heat shown in Figure 28 is moved co-feeding system and is achieved in that
(1) in structure, move in co-feeding system in the heat shown in Fig. 3, increase newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, had by absorber 3 weak solution pipeline to be communicated with the second absorber 4 through solution heat exchanger 11 to be adjusted to absorber 3 and to have weak solution pipeline to be communicated with newly-increased absorber A, newly-increased absorber A also has weak solution pipeline to be communicated with newly-increased second absorber B with newly-increased solution heat exchanger E through newly-increased solution pump C, newly-increased second absorber B has weak solution pipeline to be communicated with the second absorber 4 with solution heat exchanger 11 through newly-increased solution heat exchanger E again, evaporimeter 6 is set up refrigerant steam channel and is communicated with newly-increased absorber A, cryogen liquid pipeline newly-increased absorber A after newly-increased cryogen liquid pump D is communicated with newly-increased absorber A set up by condenser 5 has refrigerant steam channel to be communicated with newly-increased second absorber B again, newly-increased second absorber B also has heated medium pipeline and ft connection.
(2) in flow process, live steam enters engine 13 step-down work done, engine 13 heat exchanger 12 provides the 3rd steam, the heat release in heat exchanger 12 of 3rd steam is discharged through the 3rd condensate liquid pipeline after heated medium becomes condensate liquid, engine 13 provides the second steam to generator 1 and evaporimeter 6, second vapor stream becomes after condensate liquid through the second condensate liquid pipeline discharge with evaporimeter 6, progressively heat release through generator 1, engine 13 provides steam discharge to the second generator 2, and steam discharge heat release in the second generator 2 is discharged after becoming condensate liquid, the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 8 and solution heat exchanger 11, absorb refrigerant vapour heat release in heated medium, the weak solution of absorber 3 enters newly-increased absorber A, absorb refrigerant vapour heat release in cryogen liquid, the weak solution of newly-increased absorber A enters newly-increased second absorber B through newly-increased solution pump C and newly-increased solution heat exchanger E, absorb refrigerant vapour heat release in heated medium, the weak solution of newly-increased second absorber B enters the second absorber 4 through newly-increased solution heat exchanger E and solution heat exchanger 11, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 4 enters generator 1 through solution pump 7 and the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to condenser 5, generator 1 concentrated solution enters the second generator 2 through the second solution heat exchanger 15, heat absorption release refrigerant vapour also provides to the second absorber 4, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in cooling medium, the cryogen liquid of condenser 5 is divided into two-way---and the first via enters evaporimeter 6 through cryogen liquid pump 9 pressurization, absorbs heat into refrigerant vapour and provide respectively to absorber 3 and newly-increased absorber A, second tunnel flows through newly-increased absorber A, absorbs heat into refrigerant vapour and provide to newly-increased second absorber B after newly-increased cryogen liquid pump D pressurizes, and forms the dynamic co-feeding system of heat.
The effect that the technology of the present invention can realize---heat proposed by the invention is moved co-feeding system and is had following effect and advantage:
(1) temperature difference between engine 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) adopt backheat cooling process, the temperature difference between steam discharge and cold environment can be made full use of further, improve value and the technology flexibility of low grade heat energy.
(4) provide multiple concrete technical scheme, numerous different actual state can be tackled, have the wider scope of application.
(5) during variable working condition, can preferentially adopt second-kind absorption-type heat pump for thermal flow process, heat exchanger thermic load has adjustment space, which ensure that the efficient and flexible of system.
(6) 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.
(7) there is the double dominant of extraction for heat supply and condensing heat supply, avoid the impact of heating demand change on work done (generating) largely.
(8) enriched the type of hot dynamic co-feeding system, extended the range of application of 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 (58)

1. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine and working machine; Engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also has exhaust passage to be communicated with the second generator (2) after generator (1), evaporimeter (6) and the second generator (2) successively and has condensate liquid pipeline and ft connection again, and engine (13) rear heat exchange (12) that the second steam channel is communicated with heat exchanger (12) in addition has the second condensate liquid pipeline and ft connection again; second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through solution choke valve (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 1, cancel evaporimeter, exhaust passage is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second generator (2) the second generator (2) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage and generator (1) be communicated with the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up exhaust passage to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 1, exhaust passage is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second generator (2) the second generator (2) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage and generator (1) be communicated with the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the second steam channel to be communicated with heat exchanger (12) has the second condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 3rd steam channel is communicated with heat exchanger (12) set up by engine (13) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 3, cancel evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the second steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine and the second solution heat exchanger, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with generator (1) and evaporimeter (6) successively has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) with the second solution heat exchanger (15) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (15), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 5, cancel evaporimeter, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 5, engine (13) have the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 4th steam channel is communicated with heat exchanger (12) set up by engine (13) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 7, cancel evaporimeter, the finisher (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the 3rd steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also has exhaust passage to be communicated with the 3rd generator (16) successively, generator (1), evaporimeter (6) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the second steam channel to be communicated with heat exchanger (12) has the second condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through solution choke valve (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with the 3rd absorber (17), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) with the second solution heat exchanger (15) through the 3rd solution pump (18), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) through the second solution heat exchanger (15), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5), second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, move in co-feeding system in heat according to claim 9, cancel evaporimeter, exhaust passage is had by engine (13) to be communicated with the 3rd generator (16) successively, generator (1), evaporimeter (6) has condensate liquid pipeline and ft connection to be adjusted to engine (13) with the second generator (2) after the second generator (2) again has exhaust passage to be communicated with the 3rd generator (16) successively, generator (1) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up exhaust passage to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, move in co-feeding system in heat according to claim 9, exhaust passage is had by engine (13) to be communicated with the 3rd generator (16) successively, generator (1), evaporimeter (6) has condensate liquid pipeline and ft connection to be adjusted to engine (13) with the second generator (2) after the second generator (2) again has exhaust passage to be communicated with the 3rd generator (16) successively, generator (1) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the second steam channel to be communicated with heat exchanger (12) has the second condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 3rd steam channel is communicated with heat exchanger (12) set up by engine (13) the 3rd condensate liquid pipeline and ft connection again, 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, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the second steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with successively the 3rd generator (16) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with generator (1) and evaporimeter (6) successively has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) with the second solution heat exchanger (15) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (15), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also has refrigerant steam channel to be communicated with the 3rd absorber (17), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) with the 3rd solution heat exchanger (19) through the 3rd solution pump (18), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) through the 3rd solution heat exchanger (19), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5), second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, move in co-feeding system in heat according to claim 13, cancel evaporimeter, engine (13) is had the second steam channel be communicated with successively generator (1) and with the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel to be communicated with powder producer (1) after steam generator (1) have the second condensate liquid pipeline and ft connection again, there is by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to and engine (13) is set up the second steam channel be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, move in co-feeding system in heat according to claim 13, engine (13) is had the second steam channel be communicated with successively generator (1) and with the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel to be communicated with generator (1) after steam generator (1) have the second condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 4th steam channel is communicated with heat exchanger (12) set up by engine (13) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, move in co-feeding system in heat according to claim 15, cancel evaporimeter, the finisher (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the 3rd steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also has exhaust passage to be communicated with the second generator (2) successively, generator (1), evaporimeter (6) and the 3rd generator (16) afterwards the 3rd generator (16) have condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the second steam channel to be communicated with heat exchanger (12) has the second condensate liquid pipeline and ft connection again, generator (1) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through solution pump (7), absorber (3) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (11), generator (1) also has refrigerant steam channel to be communicated with the second absorber (4), second absorber (4) also has weak solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the second solution pump (8), 3rd absorber (17) also has weak solution pipeline to be communicated with the second generator (2) through the 3rd solution pump (18), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd generator (16) through solution choke valve (10), 3rd generator (16) also has concentrated solution pipeline to be communicated with the second absorber (4) through the second solution heat exchanger (15), 3rd generator (16) also has refrigerant steam channel to be communicated with the 3rd absorber (17), second generator (2) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5), second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 18. heat, move in co-feeding system in heat according to claim 17, cancel evaporimeter, exhaust passage is had to be communicated with the second generator (2) successively in engine (13), generator (1), evaporimeter (6) has condensate liquid pipeline and ft connection to be adjusted to engine (13) with the 3rd generator (16) after the 3rd generator (16) again has exhaust passage to be communicated with the second generator (2) successively, generator (1) and the 3rd generator (16) afterwards the 3rd generator (16) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up exhaust passage to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, move in co-feeding system in heat according to claim 17, exhaust passage is had to be communicated with the second generator (2) successively in engine (13), generator (1), evaporimeter (6) has condensate liquid pipeline and ft connection to be adjusted to engine (13) with the 3rd generator (16) after the 3rd generator (16) again has exhaust passage to be communicated with the second generator (2) successively, generator (1) and the 3rd generator (16) afterwards the 3rd generator (16) have condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the second steam channel to be communicated with heat exchanger (12) has the second condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 3rd steam channel is communicated with heat exchanger (12) set up by engine (13) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, move in co-feeding system in heat according to claim 19, cancel evaporimeter, the finisher (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the second steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with successively the second generator (2) and the 3rd generator (16) afterwards the 3rd generator (16) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with generator (1) and evaporimeter (6) successively has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, generator (1) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through solution pump (7), absorber (3) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (11), generator (1) also has refrigerant steam channel to be communicated with the second absorber (4), second absorber (4) also has weak solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the second solution pump (8), 3rd absorber (17) also has weak solution pipeline to be communicated with the second generator (2) through the 3rd solution pump (18), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd generator (16) through solution choke valve (10), 3rd generator (16) also has concentrated solution pipeline to be communicated with the second absorber (4) through the second solution heat exchanger (15), 3rd generator (16) also has refrigerant steam channel to be communicated with the 3rd absorber (17), second generator (2) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5), second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 22. heat, move in co-feeding system in heat according to claim 21, cancel evaporimeter, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. heat, move in co-feeding system in heat according to claim 21, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 4th steam channel is communicated with heat exchanger (12) set up by engine (13) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, move in co-feeding system in heat according to claim 23, cancel evaporimeter, the finisher (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the 3rd steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 25. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the 3rd generator (16) after the 3rd generator (16) have condensate liquid pipeline and ft connection again, engine (13) also have the second steam channel be communicated with successively generator (1) and the second generator (2) afterwards the second generator (2) have the second condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 4th steam channel to be communicated with heat exchanger (12) has the 4th condensate liquid pipeline and ft connection again, generator (1) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through solution pump (7), absorber (3) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (11), generator (1) also has refrigerant steam channel to be communicated with the second absorber (4), second absorber (4) also has weak solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the second solution pump (8), 3rd absorber (17) also has weak solution pipeline to be communicated with the second generator (2) with the 3rd solution heat exchanger (19) through the 3rd solution pump (18), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd generator (16) through the 3rd solution heat exchanger (19), 3rd generator (16) also has concentrated solution pipeline to be communicated with the second absorber (4) through the second solution heat exchanger (15), 3rd generator (16) also has refrigerant steam channel to be communicated with the 3rd absorber (17), second generator (2) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), condenser (5), second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, move in co-feeding system in heat according to claim 25, cancel evaporimeter, the finisher (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the 3rd steam channel to be communicated with absorber (3), had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also has exhaust passage to be communicated with generator (1) successively, evaporimeter (6), second evaporimeter (20) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the second steam channel to be communicated with heat exchanger (12) has the second condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through solution choke valve (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) again, second cryogen liquid pump (21) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the 3rd solution pump (18), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) through the second solution heat exchanger (15), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (20) through cryogen liquid pump (9), second evaporimeter (20) also has refrigerant steam channel to be communicated with the 3rd absorber (17), condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, move in co-feeding system in heat according to claim 27, cancel evaporimeter, exhaust passage is had to be communicated with generator (1) successively in engine (13), evaporimeter (6), second evaporimeter (20) has condensate liquid pipeline and ft connection to be adjusted to engine (13) with the second generator (2) after the second generator (2) again has exhaust passage to be communicated with generator (1) successively, second evaporimeter (20) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up exhaust passage to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid 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 27, exhaust passage is had to be communicated with generator (1) successively in engine (13), evaporimeter (6), after second evaporimeter (20) and the second generator (2) the second generator (2) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with successively generator (1) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, the rear heat exchange (12) being had by engine (13) the second steam channel to be communicated with heat exchanger (12) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with evaporimeter (6) and the second evaporimeter (20) successively after the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 3rd steam channel is communicated with heat exchanger (12) set up by engine (13) the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, move in co-feeding system in heat according to claim 29, cancel evaporimeter, engine (13) is had the second steam channel be communicated with evaporimeter (6) 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 (13) 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 (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with successively generator (1) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, engine (13) 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 (6) that engine (13) also has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 4th steam channel to be communicated with heat exchanger (12) has the 4th condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through solution choke valve (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) again, second cryogen liquid pump (21) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the 3rd solution pump (18), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) through the second solution heat exchanger (15), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (20) through cryogen liquid pump (9), second evaporimeter (20) also has refrigerant steam channel to be communicated with the 3rd absorber (17), condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, move in co-feeding system in heat according to claim 31, cancel evaporimeter, the finisher (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the 3rd steam channel to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 33. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with generator (1) successively, evaporimeter (6) and the second evaporimeter (20) afterwards the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) with the second solution heat exchanger (15) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (15), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) again, second cryogen liquid pump (21) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the 3rd solution heat exchanger (19) through the 3rd solution pump (18), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) through the 3rd solution heat exchanger (19), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (20) through cryogen liquid pump (9), second evaporimeter (20) also has refrigerant steam channel to be communicated with the 3rd absorber (17), condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 34. heat, move in co-feeding system in heat according to claim 33, cancel evaporimeter, the second steam channel is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second evaporimeter (20) the second evaporimeter (20) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with successively generator (1) and the second evaporimeter (20) afterwards the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid 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 33, the second steam channel is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second evaporimeter (20), the second evaporimeter (20) has the second condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the second steam channel to be communicated with generator (1) after generator (1) is communicated with successively to have the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) being had by engine (13) the 3rd steam channel to be communicated with heat exchanger (12) have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine (13) have the 3rd steam channel be communicated with evaporimeter (6) and the second steam (20) successively after the second evaporimeter (20) have the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 4th steam channel is communicated with heat exchanger (12) set up by engine (13) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 36. heat, move in co-feeding system in heat according to claim 35, cancel evaporimeter, engine (13) is had the 3rd steam channel be communicated with evaporimeter (6) and the second evaporimeter (20) successively after the second evaporimeter (20) have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine (13) have the 3rd steam channel be communicated with the second evaporimeter (20) after the second evaporimeter (20) have the 3rd condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (3) to set up the 3rd steam channel to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 37. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, engine (13) also have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, engine (13) also have the 3rd steam channel be communicated with the second evaporimeter (20) after the second evaporimeter (20) have the 3rd condensate liquid pipeline and ft connection again, engine (13) also has the finisher (6) of the 4th steam channel and evaporimeter (6) to have the 4th condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 5th steam channel to be communicated with heat exchanger (12) has the 5th condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) with the second solution heat exchanger (15) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (15), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) again, second cryogen liquid pump (21) also has cryogen liquid pipeline to be communicated with evaporimeter (6), evaporimeter (6) also has refrigerant steam channel to be communicated with absorber (3), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the 3rd solution heat exchanger (19) through the 3rd solution pump (18), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) through the 3rd solution heat exchanger (19), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (20) through cryogen liquid pump (9), second evaporimeter (20) also has refrigerant steam channel to be communicated with the 3rd absorber (17), condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 38. heat, move in co-feeding system in heat according to claim 37, cancel evaporimeter, the finisher (6) being had by engine (13) the 4th steam channel to be communicated with evaporimeter (6) has the 4th condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the 4th steam channel to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 39. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also has exhaust passage to be communicated with the second generator (2) after generator (1), evaporimeter (6) and the second generator (2) successively and has condensate liquid pipeline and ft connection again, and engine (13) rear heat exchange (12) that the second steam channel is communicated with heat exchanger (12) in addition has the second condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through solution choke valve (10), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) again, second cryogen liquid pump (21) also has cryogen liquid pipeline to be communicated with evaporimeter (6), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the 3rd solution pump (18), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) through the second solution heat exchanger (15), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 40. heat, move in co-feeding system in heat according to claim 39, cancel evaporimeter, exhaust passage is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second generator (2) the second generator (2) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with successively generator (1) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) to be respectively adjusted to engine (13) to set up exhaust passage to be communicated with the 3rd absorber (17) with absorber (3) respectively, being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 41. heat, move in co-feeding system in heat according to claim 39, exhaust passage is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second generator (2) the second generator (2) have again condensate liquid pipeline and ft connection be adjusted to engine (13) have exhaust passage be communicated with successively generator (1) and the second generator (2) afterwards the second generator (2) have condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the second steam channel to be communicated with heat exchanger (12) has the second condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 3rd steam channel is communicated with heat exchanger (12) set up by engine (13) the 3rd condensate liquid pipeline and ft connection again, 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 (6) being had by engine (13) the second steam channel to be communicated with evaporimeter (6) has the second condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) to be respectively adjusted to engine (13) in the lump has the second steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 43. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with generator (1) and evaporimeter (6) successively has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, second generator (2) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through the second solution pump (8), absorber (3) also has weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11), second absorber (4) also has weak solution pipeline to be communicated with generator (1) with the second solution heat exchanger (15) through solution pump (7), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (15), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) again, second cryogen liquid pump (21) also has cryogen liquid pipeline to be communicated with evaporimeter (6), 3rd generator (16) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the 3rd solution heat exchanger (19) through the 3rd solution pump (18), 3rd absorber (17) also has weak solution pipeline to be communicated with the 3rd generator (16) through the 3rd solution heat exchanger (19), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, forms 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, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have second channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) to be respectively adjusted to engine (13) to set up the second steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 45. heat, move in co-feeding system in heat according to claim 43, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have second channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 4th steam channel is communicated with heat exchanger (12) set up by engine (13) the 4th condensate liquid pipeline and ft connection again, 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 (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) to be respectively adjusted to engine (13) has the 3rd steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 47. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporimeter and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be communicated with generator (1) successively, evaporimeter (6) and the second evaporimeter (20) afterwards the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, generator (1) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through solution pump (7), absorber (3) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (11), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with evaporimeter (6) through the second cryogen liquid pump (21) again, evaporimeter (6) in addition refrigerant steam channel is communicated with absorber (3), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the second solution pump (8), 3rd absorber (17) also has weak solution pipeline to be communicated with the second absorber (4) through the second solution heat exchanger (15), second absorber (4) also has weak solution pipeline to be communicated with the 3rd generator (16) with the 3rd solution heat exchanger (19) through the 3rd solution pump (18), 3rd generator (16) also has concentrated solution pipeline to be communicated with the second generator (2) through the 3rd solution heat exchanger (19), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (20) through cryogen liquid pump (9), second evaporimeter (20) also has refrigerant steam channel to be communicated with the 3rd absorber (17), condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 48. heat, move in co-feeding system in heat according to claim 47, cancel evaporimeter, the second steam channel is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second evaporimeter (20) the second evaporimeter (20) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with successively generator (1) and the second evaporimeter (20) afterwards the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) to set up the second steam channel to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 49. heat, move in co-feeding system in heat according to claim 47, the second steam channel is had to be communicated with generator (1) successively in engine (13), after evaporimeter (6) and the second evaporimeter (20) the second evaporimeter (20) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with successively generator (1) and the second evaporimeter (20) afterwards the second evaporimeter (20) have the second condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 4th steam channel is communicated with heat exchanger (12) set up by engine (13) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 50. heat, move in co-feeding system in heat according to claim 49, cancel evaporimeter, the finisher (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (6) has refrigerant steam channel to be communicated with absorber (3) to be adjusted to engine (13) in the lump has the 3rd steam channel to be communicated with absorber (3), being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 51. heat, formed primarily of generator, the second generator, absorber, the second absorber, condenser, evaporimeter, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump, engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, engine (13) or in addition exhaust passage and ft connection, engine (13) also have exhaust passage be communicated with the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, the finisher (6) that engine (13) also has the second steam channel to be communicated with generator (1) and evaporimeter (6) successively has the second condensate liquid pipeline and ft connection again, the rear heat exchange (12) that engine (13) also has the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, generator (1) also has concentrated solution pipeline to be communicated with absorber (3) with solution heat exchanger (11) through solution pump (7), absorber (3) also has weak solution pipeline to be communicated with generator (1) through solution heat exchanger (11), generator (1) also have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) again, the second cryogen liquid pump (21) in addition cryogen liquid pipeline is communicated with evaporimeter (6), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd absorber (17) with the second solution heat exchanger (15) through the second solution pump (8), 3rd absorber (17) also has weak solution pipeline to be communicated with the second absorber (4) through the second solution heat exchanger (15), second absorber (4) also has weak solution pipeline to be communicated with the 3rd generator (16) with the 3rd solution heat exchanger (19) through the 3rd solution pump (18), 3rd generator (16) also has concentrated solution pipeline to be communicated with the second generator (2) through the 3rd solution heat exchanger (19), second generator (2) also has refrigerant steam channel to be communicated with the second absorber (4), 3rd generator (16) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9), evaporimeter (6) also has refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 52. heat, that heat described in claim 51 is moved in co-feeding system, cancel evaporimeter, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, had by evaporimeter (6) refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) to be respectively adjusted to engine (13) to set up the second steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 53. heat, that heat described in claim 51 is moved in co-feeding system, engine (13) is had the second steam channel be communicated with successively generator (1) and the finisher (6) of evaporimeter (6) have again the second condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel be communicated with generator (1) after generator (1) have the second condensate liquid pipeline and ft connection again, the finisher (6) that the rear heat exchange (12) being had by engine (13) the 3rd steam channel to be communicated with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine (13) again has the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, the rear heat exchange (12) that the 4th steam channel is communicated with heat exchanger (12) set up by engine (13) the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 54. heat, that heat described in claim 53 is moved in co-feeding system, cancel evaporimeter, the finisher (6) being had by engine (13) the 3rd steam channel to be communicated with evaporimeter (6) has the 3rd condensate liquid pipeline and ft connection again, evaporimeter (13) has refrigerant steam channel to be communicated with the 3rd absorber (17) with absorber (3) to be respectively adjusted to engine (13) has the 3rd steam channel to be communicated with the 3rd absorber (17) with absorber (3) respectively, being had by second cryogen liquid pump (21) cryogen liquid pipeline to be communicated with evaporimeter (6) to be adjusted to the second cryogen liquid pump (21) has cryogen liquid pipeline and ft connection, had by condenser (5) cryogen liquid pipeline to be communicated with evaporimeter (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and to have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 55. heat, in claim 1, 3, 5, 7, 9, 11, 13, arbitrary heat described in 15 is moved in co-feeding system, increase newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (A), newly-increased absorber (A) also has weak solution pipeline to be communicated with newly-increased second absorber (B) with newly-increased solution heat exchanger (E) through newly-increased solution pump (C), newly-increased second absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (11) through newly-increased solution heat exchanger (E) again, evaporimeter (6) is set up refrigerant steam channel and is communicated with newly-increased absorber (A), cryogen liquid pipeline newly-increased absorber (A) after newly-increased cryogen liquid pump (D) is communicated with newly-increased absorber (A) set up by condenser (5) has refrigerant steam channel to be communicated with newly-increased second absorber (B) again, newly-increased second absorber (B) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 56. heat, in claim 17, 19, 21, 26, arbitrary heat described in 25 is moved in co-feeding system, increase newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with generator (1) through solution heat exchanger (11) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (A), newly-increased absorber (A) also has weak solution pipeline to be communicated with newly-increased second absorber (B) with newly-increased solution heat exchanger (E) through newly-increased solution pump (C), newly-increased second absorber (B) has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (11) through newly-increased solution heat exchanger (E) again, evaporimeter (6) is set up refrigerant steam channel and is communicated with newly-increased absorber (A), cryogen liquid pipeline newly-increased absorber (A) after newly-increased cryogen liquid pump (D) is communicated with newly-increased absorber (A) set up by condenser (5) has refrigerant steam channel to be communicated with newly-increased second absorber (B) again, newly-increased second absorber (B) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 57. heat, in claim 27, 29, 31, 33, 35, 37, 39, 41, 43, 45, 47, 49, arbitrary heat described in 51 is moved in co-feeding system, increase newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, had by absorber (3) weak solution pipeline to be communicated with the second absorber (4) through solution heat exchanger (11) to be adjusted to absorber (3) and to have weak solution pipeline to be communicated with newly-increased absorber (A), newly-increased absorber (A) also has weak solution pipeline to be communicated with newly-increased second absorber (B) with newly-increased solution heat exchanger (E) through newly-increased solution pump (C), newly-increased second absorber (B) has weak solution pipeline to be communicated with the second absorber (4) with solution heat exchanger (11) through newly-increased solution heat exchanger (E) again, evaporimeter (6) is set up refrigerant steam channel and is communicated with newly-increased absorber (A), generator (1) is had refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with the second cryogen liquid pump (21) to be again adjusted to generator (1) have refrigerant steam channel be communicated with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline to be communicated with newly-increased cryogen liquid pump (D) with the second cryogen liquid pump (21) respectively again, newly-increased cryogen liquid pump (D) also have cryogen liquid pipeline be communicated with newly-increased absorber (A) after increase absorber (A) newly and have refrigerant steam channel to be communicated with newly-increased second absorber (B) again, newly-increased second absorber (B) also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 58. heat, is move in co-feeding system in the arbitrary heat described in claim 1-57, cancels heat exchanger, cancel the heated medium pipeline be communicated with heat exchanger (12), forms the dynamic co-feeding system of heat.
CN201510043152.4A 2014-01-27 2015-01-23 The dynamic co-feeding system of heat Active CN104748439B (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106322832A (en) * 2016-05-30 2017-01-11 李华玉 Heat and power co-supply system
CN106352591A (en) * 2016-05-30 2017-01-25 李华玉 Combined heating and power system
CN106403351A (en) * 2016-06-15 2017-02-15 李华玉 Combined heating and power system
CN106440470A (en) * 2016-06-15 2017-02-22 李华玉 Combined heating and power system
CN106440469A (en) * 2016-05-30 2017-02-22 李华玉 Combined heating and power system
CN106482380A (en) * 2016-06-15 2017-03-08 李华玉 Heat moves co-feeding system
CN106524561A (en) * 2016-06-15 2017-03-22 李华玉 Combined heat and power supply system

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11304274A (en) * 1998-04-20 1999-11-05 Kawasaki Thermal Eng Co Ltd Waste heat utilized absorption type water cooling/ heating machine refrigerating machine
JP2000065436A (en) * 1998-08-18 2000-03-03 Kawasaki Thermal Engineering Co Ltd Waste heat utilizing absorption type water heater/cooler refrigerating machine with load variation controlling function
JP2001066010A (en) * 1999-08-24 2001-03-16 Tokyo Gas Co Ltd Absorption chller and heater
CN2615346Y (en) * 2002-11-28 2004-05-12 江苏双良空调设备股份有限公司 Heating, electric and cooling triple combined supply system with steam type bromine cooling machine and thermal pump as cold and heat sources
CN1811303A (en) * 2006-02-18 2006-08-02 李华玉 Single-effect heat pump/double-effect cooling absorption set and combined heat, electricity and cold supply system
CN202381129U (en) * 2011-11-01 2012-08-15 北京科技大学 Power supplying system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11304274A (en) * 1998-04-20 1999-11-05 Kawasaki Thermal Eng Co Ltd Waste heat utilized absorption type water cooling/ heating machine refrigerating machine
JP2000065436A (en) * 1998-08-18 2000-03-03 Kawasaki Thermal Engineering Co Ltd Waste heat utilizing absorption type water heater/cooler refrigerating machine with load variation controlling function
JP2001066010A (en) * 1999-08-24 2001-03-16 Tokyo Gas Co Ltd Absorption chller and heater
CN2615346Y (en) * 2002-11-28 2004-05-12 江苏双良空调设备股份有限公司 Heating, electric and cooling triple combined supply system with steam type bromine cooling machine and thermal pump as cold and heat sources
CN1811303A (en) * 2006-02-18 2006-08-02 李华玉 Single-effect heat pump/double-effect cooling absorption set and combined heat, electricity and cold supply system
CN202381129U (en) * 2011-11-01 2012-08-15 北京科技大学 Power supplying system

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106322832A (en) * 2016-05-30 2017-01-11 李华玉 Heat and power co-supply system
CN106352591A (en) * 2016-05-30 2017-01-25 李华玉 Combined heating and power system
CN106440469A (en) * 2016-05-30 2017-02-22 李华玉 Combined heating and power system
CN106440469B (en) * 2016-05-30 2020-01-31 李华玉 Combined heat and power system
CN106403351A (en) * 2016-06-15 2017-02-15 李华玉 Combined heating and power system
CN106440470A (en) * 2016-06-15 2017-02-22 李华玉 Combined heating and power system
CN106482380A (en) * 2016-06-15 2017-03-08 李华玉 Heat moves co-feeding system
CN106524561A (en) * 2016-06-15 2017-03-22 李华玉 Combined heat and power supply system
CN106403351B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system
CN106482380B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system
CN106524561B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system
CN106440470B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system

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