CN104748439B - The dynamic co-feeding system of heat - Google Patents

The dynamic co-feeding system of heat Download PDF

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CN104748439B
CN104748439B CN201510043152.4A CN201510043152A CN104748439B CN 104748439 B CN104748439 B CN 104748439B CN 201510043152 A CN201510043152 A CN 201510043152A CN 104748439 B CN104748439 B CN 104748439B
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generator
absorber
connection
pipeline
solution
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CN104748439A (en
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李华玉
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李华玉
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00Climate change mitigation technologies for sector-wide applications
    • Y02P80/10Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
    • Y02P80/15On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

Abstract

The present invention provides heat dynamic co-feeding system, belongs to the dynamic alliance of heat and technical field of heat pumps.Engine is to generator, evaporator and the second generator provide steam discharge, engine also heat exchanger provides the second steam, second generator is connected through the second solution pump and solution heat exchanger with absorber, absorber is connected through solution heat exchanger with the second absorber, second absorber is connected through solution pump with generator, generator is connected through solution choke valve with the second generator, second generator provides refrigerant vapour to the second absorber, generator has refrigerant steam channel to be connected with condenser, condenser is connected through cryogen liquid pump with evaporator, evaporator has refrigerant steam channel to be connected with absorber, condenser and the second absorber have cooling medium pipeline and ft connection respectively, absorber and heat exchanger have heated medium pipeline and ft connection respectively, form the dynamic co-feeding system of heat.

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:
Made with vapor in the thermodynamic cycle device of circulatory mediator, to make engine (steam turbine) that there is higher inside heat Efficiency and its property safe and reliable to operation of increase, then require that the pressure and temperature of engine outlet steam discharge can not be too low;So in the winter Ji Shijie, environment temperature is relatively low, and engine outlet exhaust temperature is higher, then will have about 40 DEG C of even more highs therebetween The temperature difference can not be used;Furthermore, in the Steam Power Circulation system by representative of Thermal Power Station, although the grade of steam discharge is very It is low, but its thermic load also having is often very abundant, if being subject to effectively using then significant.
Be currently used for winter heating heat move alliance, also or have other heat supply purposes heat move alliance, corresponding technical side Case is generally comprised:(1) improve engine outlet steam discharge parameter and carry out heat supply;(2) drawn gas using engine intermediate extraction or segmentation Carry out heat supply;(3) it is the high temperature heat source of first-class absorption type heat pump come recovery section exhaust steam heat to use engine intermediate extraction Carry out heat supply.But, all cold environment is not made full use of in the dynamic jointly-supplying technology measure of these heat.
Using the second-kind absorption-type heat pump principle with regenerative cooling end, further make full use of engine steam discharge with it is cold The temperature difference between environment, and consider that following thermal energy step utilizes principle, and second-kind absorption-type heat pump heat supply and engine are drawn gas Heating is combined, with the rationalization for meeting the heat demand under different situations He realizing heat energy utilization --- and this can not only be realized Effective utilization of the temperature difference, and operation interval of the engine blade in wet-steam region can be reduced or eliminated, increase engine The internal thermal efficiency.
Due to being related to temperature difference size, cold ambient temperature between heat user thermal parameter and thermic load, steam discharge and cold environment Height, a variety of specific operating modes such as the thermic load that contains of steam discharge is how many, and consider the adaptation to existing heat power generating system, because This needs a variety of specific technical schemes.
The content of the invention:
Present invention is primarily intended to provide heat dynamic co-feeding system, specific content of the invention subitem is described below:
1. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine and working machine Constituted;Engine connects working machine, and engine has live steam passage and ft connection, also engine or exhaust passage and outside Connection, engine also have exhaust passage be sequentially communicated generator, evaporator and the second generator after the second generator have cold again Lime set pipeline and ft connection, the rear heat exchange that engine also has the second steam channel to be connected with heat exchanger have second cold again Lime set pipeline and ft connection;Second generator also has concentrated solution pipeline through the second solution pump and solution heat exchanger and absorber Connection, absorber also has weak solution pipeline to be connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution Pipeline is connected through solution pump with generator, and generator also has concentrated solution pipeline to be connected through solution choke valve with the second generator, the Two generators also have refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel to be connected with condenser, Condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel to connect with absorber Logical, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber also has heated medium pipeline With ft connection, heat exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, is in the heat described in the 1st moves co-feeding system, to cancel evaporator, engine is had into row The second generator has condensate liquid pipeline and ft connection again after vapour passage is sequentially communicated generator, evaporator and the second generator Be adjusted to engine have exhaust passage connected with generator and the second generator after the second generator have again condensate liquid pipeline with Ft connection, has refrigerant steam channel to be connected with absorber evaporator and is adjusted to engine and sets up exhaust passage and absorber Connection, has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and is adjusted to condenser and has 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, is in the heat described in the 1st moves co-feeding system, to have exhaust passage to connect successively in engine The second generator has condensate liquid pipeline and ft connection to be adjusted to engine again after logical generator, evaporator and the second generator Have exhaust passage connected with generator and the second generator after the second generator have condensate liquid pipeline and ft connection again, will be dynamic The rear heat exchange that power machine has the second steam channel to be connected with heat exchanger has the second condensate liquid pipeline to be adjusted with ft connection again The finisher for having the second steam channel to be connected with evaporator for engine has the second condensate liquid pipeline and ft connection, power again Machine sets up the rear heat exchange that the 3rd steam channel connects with heat exchanger the 3rd condensate liquid pipeline and ft connection again, is formed The dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, is in the heat described in the 3rd moves co-feeding system, to cancel evaporator, engine is had the The finisher that two steam channels are connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have refrigerant vapour again Passage is connected with absorber to be adjusted to engine and has the second steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid pipe Road is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat dynamic Co-feeding system.
5. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine and the second solution heat Exchanger is constituted;Engine connects working machine, and engine has live steam passage and ft connection, also engine or exhaust passage With ft connection, engine also has exhaust passage to have condensate liquid pipeline to connect with outside again with the second generator after the second generator It is logical, the finisher that engine also has the second steam channel to be sequentially communicated generator and evaporator have again the second condensate liquid pipeline with Ft connection, the rear heat exchange that engine also has the 3rd steam channel to be connected with heat exchanger have again the 3rd condensate liquid pipeline with Ft connection;Second generator also has concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, absorbs Device also has weak solution pipeline to be connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline through solution Pump and the second solution heat exchanger are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and second Generator is connected, and the second generator also has refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel Connected with condenser, condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, evaporator also has refrigerant vapour to lead to Road is connected with absorber, and condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber also has quilt Medium pipeline and ft connection are heated, 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, is in the heat described in the 5th moves co-feeding system, to cancel evaporator, engine is had the Two steam channels are sequentially communicated generator and the finisher of evaporator has the second condensate liquid pipeline to be adjusted to ft connection again Engine have the second steam channel connected with generator after generator have the second condensate liquid pipeline and ft connection again, will evaporate Device has refrigerant steam channel to connect with absorber to be adjusted to engine and set up the second steam channel to connect with absorber, by condenser There is cryogen liquid pipeline to connect with evaporator through cryogen liquid pump to be adjusted to condenser and there is cryogen liquid pipeline through cryogen liquid pump and outside to connect It is logical, form the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is that engine has the second steam channel successively in the heat described in the 5th moves co-feeding system The finisher of connection generator and evaporator has the second condensate liquid pipeline to be adjusted to engine with ft connection again the second steaming Generator has the second condensate liquid pipeline and ft connection again after vapour passage is connected with generator, has the 3rd steam to lead in engine The rear heat exchange that road is connected with heat exchanger has the 3rd condensate liquid pipeline to be adjusted to engine with ft connection again the 3rd steaming The finisher that vapour passage is connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, and engine sets up the 4th steam The rear heat exchange that passage is connected with heat exchanger has the 4th condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is in the heat described in the 7th moves co-feeding system, to cancel evaporator, engine is had the The finisher that three steam channels are connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have refrigerant vapour again Passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid pipe Road is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat dynamic Co-feeding system.
9. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine connects working machine, moves Power machine has live steam passage and ft connection, also engine or exhaust passage and a ft connection, engine also have exhaust passage according to The second generator has condensate liquid pipeline and outside again after the 3rd generator of secondary connection, generator, evaporator and the second generator Connection, the rear heat exchange that engine also has the second steam channel to be connected with heat exchanger has the second condensate liquid pipeline and outside again Connection;Second generator also has concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, and absorber is also There is weak solution pipeline to be connected through solution heat exchanger with the second absorber, the second absorber also have weak solution pipeline through solution pump with Generator is connected, and generator also has concentrated solution pipeline to be connected through solution choke valve with the second generator, and the second generator is also cold Agent steam channel is connected with the second absorber, and generator also has refrigerant steam channel to be connected with the 3rd absorber, the 3rd absorber Also weak solution pipeline is connected through the 3rd solution pump and the second solution heat exchanger with the 3rd generator, and the 3rd generator is also dense Solution line is connected through the second solution heat exchanger with the 3rd absorber, and the 3rd generator also has refrigerant steam channel and condenser Connection, condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel and absorption Device is connected, and condenser, the second absorber and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber also has Heated medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic alliance system of heat System.
10. the dynamic co-feeding system of heat, is in the heat described in the 9th moves co-feeding system, to cancel evaporator, engine is had into row The second generator has condensate line again after vapour passage is sequentially communicated the 3rd generator, generator, evaporator and the second generator Road and ft connection, which are adjusted to engine, has exhaust passage to be sequentially communicated after the 3rd generator, generator and the second generator the Two generators have condensate liquid pipeline and ft connection again, have refrigerant steam channel to be connected with absorber evaporator and are adjusted to power Machine is set up exhaust passage and connected with absorber, has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and is adjusted to cold Condenser has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
11. the dynamic co-feeding system of heat, is that in the heat described in the 9th moves co-feeding system, engine is had into exhaust passage successively The second generator has condensate liquid pipeline and outside to connect again after connecting the 3rd generator, generator, evaporator and the second generator It is logical be adjusted to engine have exhaust passage be sequentially communicated the 3rd generator, generator and the second generator after the second generator again There are condensate liquid pipeline and ft connection, the rear heat exchange that engine has the second steam channel to be connected with heat exchanger is had again The finisher that two condensate liquid pipelines are adjusted to engine with ft connection and have the second steam channel to be connected with evaporator has again Two condensate liquid pipelines and ft connection, engine sets up the rear heat exchange that the 3rd steam channel connects with heat exchanger again Three condensate liquid pipelines and ft connection, form the dynamic co-feeding system of heat.
12. the dynamic co-feeding system of heat, is in the heat described in the 11st moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the second steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, is formed The dynamic co-feeding system of heat.
13. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 are constituted;Engine connects work Make machine, engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine also has steam discharge The second generator has condensate liquid pipeline and ft connection, power again after passage is sequentially communicated the 3rd generator and the second generator Machine also has the second steam channel to be sequentially communicated generator and the finisher of evaporator has the second condensate liquid pipeline to connect with outside again Logical, the rear heat exchange that engine also has the 3rd steam channel to be connected with heat exchanger has the 3rd condensate liquid pipeline to connect with outside again It is logical;Second generator also has concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, and absorber also has Weak solution pipeline is connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline through solution pump and Two solution heat exchangers are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and the second generator Connection, the second generator also has refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel and the 3rd Absorber is connected, and the 3rd absorber also has weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and the 3rd generator Connection, the 3rd generator also has concentrated solution pipeline to be connected through the 3rd solution heat exchanger with the 3rd absorber, and the 3rd generator is also There is refrigerant steam channel to be connected with condenser, condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, evaporator Also refrigerant steam channel is connected with absorber, and condenser, the second absorber and the 3rd absorber also have cooling medium pipe respectively Road and ft connection, absorber also have heated medium pipeline and ft connection, heat exchanger also have heated medium pipeline with Ft connection, forms the dynamic co-feeding system of heat.
14. the dynamic co-feeding system of heat, is in the heat described in the 13rd moves co-feeding system, to cancel evaporator, engine is had Second steam channel is sequentially communicated generator and has the second condensate liquid pipeline to be adjusted with ft connection again with the finisher of evaporator It is whole for engine have the second steam channel connected with generator after generator have the second condensate liquid pipeline and ft connection again, general Evaporator has refrigerant steam channel to connect to be adjusted to engine setting up the second steam channel with absorber and connected with absorber, will Condenser have cryogen liquid pipeline connected through cryogen liquid pump with evaporator be adjusted to condenser have cryogen liquid pipeline through cryogen liquid pump with Ft connection, forms the dynamic co-feeding system of heat.
15. the dynamic co-feeding system of heat, is that in the heat described in the 13rd moves co-feeding system, engine is had into the second steam channel Being sequentially communicated generator and having the second condensate liquid pipeline to be adjusted to engine with ft connection again with the finisher of evaporator has Generator has the second condensate liquid pipeline and ft connection again after second steam channel is connected with generator, and engine is had into the 3rd The rear heat exchange that steam channel is connected with heat exchanger has the 3rd condensate liquid pipeline to be adjusted to engine with ft connection and had again The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, and engine sets up the 4th The rear heat exchange that steam channel is connected with heat exchanger has the 4th condensate liquid pipeline and ft connection again, forms the dynamic alliance system of heat System.
16. the dynamic co-feeding system of heat, is in the heat described in the 15th moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
17. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine connects working machine, moves Power machine has live steam passage and ft connection, also engine or exhaust passage and a ft connection, engine also have exhaust passage according to The 3rd generator has condensate liquid pipeline and outside again after the second generator of secondary connection, generator, evaporator and the 3rd generator Connection, the rear heat exchange that engine also has the second steam channel to be connected with heat exchanger has the second condensate liquid pipeline and outside again Connection;Generator also has concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, and absorber also has weak solution Pipeline is connected through solution heat exchanger with generator, and generator also has refrigerant steam channel to be connected with the second absorber, and second inhales Receiving device also has weak solution pipeline to be connected through the second solution pump and the second solution heat exchanger with the 3rd absorber, and the 3rd absorber is also There is weak solution pipeline to be connected through the 3rd solution pump with the second generator, the second generator also has concentrated solution pipeline through solution choke valve Connected with the 3rd generator, the 3rd generator also has concentrated solution pipeline to be connected through the second solution heat exchanger with the second absorber, 3rd generator also has refrigerant steam channel to be connected with the 3rd absorber, and the second generator also has refrigerant steam channel and condenser Connection, condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel and absorption Device is connected, and condenser, the second absorber and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber also has Heated medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic alliance system of heat System.
18. the dynamic co-feeding system of heat, is in the heat described in the 17th moves co-feeding system, to cancel evaporator, engine is had The 3rd generator has condensate liquid again after exhaust passage is sequentially communicated the second generator, generator, evaporator and the 3rd generator Pipeline is adjusted to engine with ft connection has exhaust passage to be sequentially communicated after the second generator, generator and the 3rd generator 3rd generator has condensate liquid pipeline and ft connection again, has refrigerant steam channel to be connected with absorber evaporator and is adjusted to dynamic Power machine is set up exhaust passage and connected with absorber, has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and is adjusted to Condenser has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
19. the dynamic co-feeding system of heat, is that in the heat described in the 17th moves co-feeding system, engine is had into exhaust passage successively The 3rd generator has condensate liquid pipeline and outside to connect again after connecting the second generator, generator, evaporator and the 3rd generator It is logical be adjusted to engine have exhaust passage be sequentially communicated the second generator, generator and the 3rd generator after the 3rd generator again There are condensate liquid pipeline and ft connection, the rear heat exchange that engine has the second steam channel to be connected with heat exchanger is had again The finisher that two condensate liquid pipelines are adjusted to engine with ft connection and have the second steam channel to be connected with evaporator has again Two condensate liquid pipelines and ft connection, engine sets up the rear heat exchange that the 3rd steam channel connects with heat exchanger again Three condensate liquid pipelines and ft connection, form the dynamic co-feeding system of heat.
20. the dynamic co-feeding system of heat, is in the heat described in the 19th moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the second steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
21. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Second solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine connects working machine, moves Power machine has live steam passage and ft connection, also engine or exhaust passage and a ft connection, engine also have exhaust passage according to The 3rd generator has condensate liquid pipeline and ft connection again after the second generator of secondary connection and the 3rd generator, and engine also has Second steam channel is sequentially communicated generator and the finisher of evaporator the second condensate liquid pipeline and ft connection, power again The rear heat exchange that machine also has the 3rd steam channel to be connected with heat exchanger has the 3rd condensate liquid pipeline and ft connection again;Occur Device also has concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, and absorber also has weak solution pipeline through molten Liquid heat exchanger is connected with generator, and generator also has refrigerant steam channel to be connected with the second absorber, and the second absorber also has Weak solution pipeline is connected through the second solution pump and the second solution heat exchanger with the 3rd absorber, and the 3rd absorber also has weak solution Pipeline is connected through the 3rd solution pump with the second generator, and the second generator also has concentrated solution pipeline through solution choke valve and the 3rd hair Raw device connection, the 3rd generator also has concentrated solution pipeline to be connected through the second solution heat exchanger with the second absorber, and the 3rd occurs Device also has refrigerant steam channel to be connected with the 3rd absorber, and the second generator also has refrigerant steam channel to be connected with condenser, cold Condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber, Condenser, the second absorber and the 3rd absorber also have cooling medium pipeline and ft connection respectively, and absorber also has heated Medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
22. the dynamic co-feeding system of heat, is in the heat described in the 21st moves co-feeding system, to cancel evaporator, engine is had Second steam channel is sequentially communicated generator and the finisher of evaporator has the second condensate liquid pipeline to be adjusted with ft connection again For engine have the second steam channel connected with generator after generator have the second condensate liquid pipeline and ft connection again, will steam Hair device has refrigerant steam channel to connect with absorber to be adjusted to engine and set up the second steam channel to connect with absorber, will condense Device have cryogen liquid pipeline connected through cryogen liquid pump with evaporator be adjusted to condenser have cryogen liquid pipeline through cryogen liquid pump with it is outside Connection, forms the dynamic co-feeding system of heat.
23. the dynamic co-feeding system of heat, is that in the heat described in the 21st moves co-feeding system, engine is had into the second steam channel Being sequentially communicated the finisher of generator and evaporator and having the second condensate liquid pipeline and ft connection to be adjusted to engine again has the Generator has the second condensate liquid pipeline and ft connection again after two steam channels are connected with generator, and engine is had into the 3rd steaming The rear heat exchange that vapour passage is connected with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again the The finisher that three steam channels are connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, and engine sets up the 4th steaming The rear heat exchange that vapour passage is connected with heat exchanger has the 4th condensate liquid pipeline and ft connection again, forms the dynamic alliance system of heat System.
24. the dynamic co-feeding system of heat, is in the heat described in the 23rd moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
25. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 are constituted;Engine connects work Make machine, engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine also has steam discharge The 3rd generator has condensate liquid pipeline and ft connection again after passage is connected with the 3rd generator, and engine also has the second steam The second generator has the second condensate liquid pipeline and ft connection, power again after passage is sequentially communicated generator and the second generator The finisher that machine also has the 3rd steam channel to be connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, and engine is also The rear heat exchange for having the 4th steam channel to be connected with heat exchanger has the 4th condensate liquid pipeline and ft connection again;Generator is also There is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorber also has weak solution pipeline to be handed over through solution heat Parallel operation is connected with generator, and generator also has refrigerant steam channel to be connected with the second absorber, and the second absorber also has weak solution Pipeline is connected through the second solution pump and the second solution heat exchanger with the 3rd absorber, and the 3rd absorber also has weak solution pipeline warp 3rd solution pump and the 3rd solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipeline molten through the 3rd Liquid heat exchanger is connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the second solution heat exchanger and second Absorber is connected, and the 3rd generator also has refrigerant steam channel to be connected with the 3rd absorber, and the second generator also has refrigerant vapour Passage is connected with condenser, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator also has cryogen steaming Vapour passage is connected with absorber, and condenser, the second absorber and the 3rd absorber also have cooling medium pipeline and outside to connect respectively Logical, absorber also has heated medium pipeline and ft connection, and heat exchanger also has heated medium pipeline and ft connection, shape Into the dynamic co-feeding system of heat.
26. the dynamic co-feeding system of heat, is in the heat described in the 25th moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
27. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 evaporator and the second cryogen liquid pump are constituted;Engine Working machine is connected, engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine is also Have exhaust passage be sequentially communicated generator, evaporator, the second evaporator and the second generator after the second generator have condensation again Liquid pipeline and ft connection, the rear heat exchange that engine also has the second steam channel to be connected with heat exchanger have the second condensation again Liquid pipeline and ft connection;Second generator also has concentrated solution pipeline to connect through the second solution pump and solution heat exchanger with absorber Logical, absorber also has weak solution pipeline to be connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution pipe Road is connected through solution pump with generator, and generator also has concentrated solution pipeline to be connected through solution choke valve with the second generator, and second Generator also has refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel to be connected with the 3rd generator The 3rd generator has cryogen liquid pipeline to be connected with the second cryogen liquid pump again afterwards, and the second cryogen liquid pump also has cryogen liquid pipeline and steaming Device connection is sent out, evaporator also has refrigerant steam channel to be connected with absorber;3rd generator also has concentrated solution pipeline molten through the 3rd Liquid pump and the second solution heat exchanger are connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline to be handed over through the second solution heat Parallel operation is connected with the 3rd generator, and the 3rd generator also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid Pipeline is connected through cryogen liquid pump with the second evaporator, and the second evaporator also has refrigerant steam channel to be connected with the 3rd absorber, cold Condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber and the 3rd absorber also have respectively to be added Heat medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
28. the dynamic co-feeding system of heat, is in the heat described in the 27th moves co-feeding system, to cancel evaporator, engine is had The second generator has condensate liquid again after exhaust passage is sequentially communicated generator, evaporator, the second evaporator and the second generator Pipeline is adjusted to engine with ft connection has exhaust passage to be sequentially communicated after generator, the second evaporator and the second generator Second generator has condensate liquid pipeline and ft connection again, has refrigerant steam channel to be connected with absorber evaporator and is adjusted to dynamic Power machine is set up exhaust passage and connected with absorber, has cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump and is adjusted to second Cryogen liquid pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
29. the dynamic co-feeding system of heat, is that in the heat described in the 27th moves co-feeding system, engine is had into exhaust passage successively The second generator has condensate liquid pipeline and outside to connect again after connection generator, evaporator, the second evaporator and the second generator It is logical be adjusted to engine have exhaust passage be sequentially communicated generator and the second generator after the second generator have condensate line again Road and ft connection, have the second condensate line again by the rear heat exchange that engine has the second steam channel to be connected with heat exchanger Road and ft connection, which are adjusted to engine, has the second steam channel to be sequentially communicated the second evaporation after evaporator and the second evaporator Device has the second condensate liquid pipeline and ft connection again, and engine sets up heat friendship after the 3rd steam channel is connected with heat exchanger Parallel operation has the 3rd condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
30. the dynamic co-feeding system of heat, is in the heat described in the 29th moves co-feeding system, to cancel evaporator, engine is had The second evaporator has the second condensate liquid pipeline and outside again after second steam channel is sequentially communicated evaporator and the second evaporator Connection be adjusted to engine have the second steam channel connected with the second evaporator after the second evaporator have the second condensate line again Road and ft connection, by evaporator have refrigerant steam channel connected with absorber be adjusted to engine set up the second steam channel with Absorber is connected, and is had cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump and is adjusted to the second cryogen liquid pump and has cryogen liquid pipe Road and ft connection, form the dynamic co-feeding system of heat.
31. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 evaporator and the second cryogen liquid pump are constituted;Engine Working machine is connected, engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine is also Have exhaust passage be sequentially communicated generator and the second generator after the second generator have condensate liquid pipeline and ft connection again, move Power machine also have the second steam channel connected with the second evaporator after the second evaporator there is the second condensate liquid pipeline to connect with outside again Logical, the finisher that engine also has the 3rd steam channel to be connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, The rear heat exchange that engine also has the 4th steam channel to be connected with heat exchanger has the 4th condensate liquid pipeline and ft connection again; Second generator also has concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, and absorber also has dilute molten Liquid pipeline is connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline through solution pump and generator Connection, generator also has concentrated solution pipeline to be connected through solution choke valve with the second generator, and the second generator also has refrigerant vapour Passage is connected with the second absorber, generator also have refrigerant steam channel connected with the 3rd generator after the 3rd generator have again Cryogen liquid pipeline is connected with the second cryogen liquid pump, and the second cryogen liquid pump also has cryogen liquid pipeline to be connected with evaporator, and evaporator is also There is refrigerant steam channel to be connected with absorber;3rd generator also has concentrated solution pipeline to be handed over through the 3rd solution pump and the second solution heat Parallel operation is connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline to connect through the second solution heat exchanger and the 3rd generator Logical, the 3rd generator also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and the Two evaporators are connected, and the second evaporator also has refrigerant steam channel to be connected with the 3rd absorber, and condenser and the second absorber are also There are cooling medium pipeline and ft connection respectively, absorber and the 3rd absorber also have heated medium pipeline to connect with outside respectively Logical, heat exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
32. the dynamic co-feeding system of heat, is in the heat described in the 31st moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and the second cryogen liquid pump is had Cryogen liquid pipeline is connected with evaporator to be adjusted to the second cryogen liquid pump and has cryogen liquid pipeline and a ft connection, forms the dynamic alliance system of heat System.
33. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 evaporator and the second cryogen Liquid pump is constituted;Engine connects working machine, and engine has live steam passage and a ft connection, engine or also exhaust passage with Ft connection, engine also have exhaust passage connected with the second generator after the second generator have again condensate liquid pipeline with it is outside Connection, engine also have the second steam channel be sequentially communicated generator, evaporator and the second evaporator after the second evaporator again There are the second condensate liquid pipeline and a ft connection, engine also has rear heat exchange that the 3rd steam channel connects with heat exchanger again There are the 3rd condensate liquid pipeline and ft connection;Second generator also has concentrated solution pipeline through the second solution pump and solution heat exchange Device is connected with absorber, and absorber also has weak solution pipeline to be connected through solution heat exchanger with the second absorber, the second absorber Also weak solution pipeline is connected through solution pump and the second solution heat exchanger with generator, and generator also has concentrated solution pipeline through Two solution heat exchangers are connected with the second generator, and the second generator also has refrigerant steam channel to be connected with the second absorber, hair Raw device also have refrigerant steam channel connected with the 3rd generator after the 3rd generator have cryogen liquid pipeline and the second cryogen liquid again Pump is connected, and the second cryogen liquid pump also has cryogen liquid pipeline to be connected with evaporator, and evaporator also has refrigerant steam channel and absorber Connection;3rd generator also has concentrated solution pipeline to be connected through the 3rd solution pump and the 3rd solution heat exchanger with the 3rd absorber, 3rd absorber also has weak solution pipeline to be connected through the 3rd solution heat exchanger with the 3rd generator, and the 3rd generator also has cryogen Steam channel is connected with condenser, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with the second evaporator, the second evaporation Device also has refrigerant steam channel to be connected with the 3rd absorber, and condenser and the second absorber also have cooling medium pipeline and outer respectively Portion is connected, 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.
34. the dynamic co-feeding system of heat, is in the heat described in the 33rd moves co-feeding system, to cancel evaporator, engine is had The second evaporator has the second condensate liquid pipeline again after second steam channel is sequentially communicated generator, evaporator and the second evaporator Being adjusted to engine with ft connection has the second steam channel to be sequentially communicated the second evaporator after generator and the second evaporator There are the second condensate liquid pipeline and ft connection again, there is refrigerant steam channel to be connected with absorber evaporator and be adjusted to engine increasing If the second steam channel is connected with absorber, having cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump, to be adjusted to second cold Agent liquid pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
35. the dynamic co-feeding system of heat, is that in the heat described in the 33rd moves co-feeding system, engine is had into the second steam channel The second evaporator has the second condensate liquid pipeline and ft connection to adjust again after being sequentially communicated generator, evaporator and the second evaporator It is whole for engine have the second steam channel be sequentially communicated generator after generator connection have again the second condensate liquid pipeline with it is outside Connection, has the 3rd condensate liquid pipeline and outside again by the rear heat exchange that engine has the 3rd steam channel to be connected with heat exchanger Connection is adjusted to engine and has the 3rd steam channel to be sequentially communicated the second evaporator after evaporator and the second evaporator the again Three condensate liquid pipelines and ft connection, engine sets up the rear heat exchange that the 4th steam channel connects with heat exchanger again Four condensate liquid pipelines and ft connection, form the dynamic co-feeding system of heat.
36. the dynamic co-feeding system of heat, is in the heat described in the 35th moves co-feeding system, to cancel evaporator, engine is had The second evaporator has the 3rd condensate liquid pipeline and outside again after 3rd steam channel is sequentially communicated evaporator and the second evaporator Connection be adjusted to engine have the 3rd steam channel connected with the second evaporator after the second evaporator have the 3rd condensate line again Road and ft connection, by evaporator have refrigerant steam channel connected with absorber be adjusted to engine set up the 3rd steam channel with Absorber is connected, and is had cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump and is adjusted to the second cryogen liquid pump and has cryogen liquid pipe Road and ft connection, form the dynamic co-feeding system of heat.
37. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 evaporator and the second cryogen Liquid pump is constituted;Engine connects working machine, and engine has live steam passage and a ft connection, engine or also exhaust passage with Ft connection, engine also have exhaust passage connected with the second generator after the second generator have again condensate liquid pipeline with it is outside Connection, engine also have the second steam channel connected with generator after generator there is the second condensate liquid pipeline to connect with outside again It is logical, engine also have the 3rd steam channel connect with the second evaporator after the second evaporator have the 3rd condensate liquid pipeline and outside again Portion is connected, and engine also has the 4th steam channel and the finisher of evaporator 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 connected with heat exchanger has the 5th condensate liquid pipeline to connect with outside again It is logical;Second generator also has concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, and absorber also has Weak solution pipeline is connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline through solution pump and Two solution heat exchangers are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and the second generator Connection, the second generator also has refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel and the 3rd The 3rd generator has cryogen liquid pipeline to be connected with the second cryogen liquid pump again after generator connection, and the second cryogen liquid pump also has cryogen Liquid pipeline is connected with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber;3rd generator also has concentrated solution pipe The solution pumps of Lu Jing tri- and the 3rd solution heat exchanger are connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline through Three solution heat exchangers are connected with the 3rd generator, and the 3rd generator also has refrigerant steam channel to be connected with condenser, condenser Also cryogen liquid pipeline is connected through cryogen liquid pump with the second evaporator, and the second evaporator also has refrigerant steam channel and the 3rd absorption Device is connected, and condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber and the 3rd absorber are also There are heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, forms heat dynamic Co-feeding system.
38. the dynamic co-feeding system of heat, is in the heat described in the 37th moves co-feeding system, to cancel evaporator, engine is had The finisher that 4th steam channel is connected with evaporator has the 4th condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 4th steam channel to be connected with absorber in the lump, and the second cryogen liquid pump is had Cryogen liquid pipeline is connected with evaporator to be adjusted to the second cryogen liquid pump and has cryogen liquid pipeline and a ft connection, forms the dynamic alliance system of heat System.
39. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Second solution heat exchanger, the 3rd generator, the 3rd absorber, the 3rd solution pump and the second cryogen liquid pump are constituted;Engine Working machine is connected, engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine is also Have exhaust passage be sequentially communicated the second generator after generator, evaporator and the second generator have again condensate liquid pipeline with it is outside Connection, the rear heat exchange that engine also has the second steam channel to be connected with heat exchanger has the second condensate liquid pipeline and outside again Connection;Second generator also has concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, and absorber is also There is weak solution pipeline to be connected through solution heat exchanger with the second absorber, the second absorber also have weak solution pipeline through solution pump with Generator is connected, and generator also has concentrated solution pipeline to be connected through solution choke valve with the second generator, and the second generator is also cold Agent steam channel is connected with the second absorber, generator also have refrigerant steam channel connected with the 3rd generator after the 3rd generation Device has cryogen liquid pipeline to be connected with the second cryogen liquid pump again, and the second cryogen liquid pump also has cryogen liquid pipeline to be connected with evaporator;The Three generators also have concentrated solution pipeline to be connected through the 3rd solution pump and the second solution heat exchanger with the 3rd absorber, and the 3rd absorbs Device also has weak solution pipeline to be connected through the second solution heat exchanger with the 3rd generator, and the 3rd generator also has refrigerant steam channel Connected with condenser, condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, evaporator also has refrigerant vapour to lead to Road is connected with absorber and the 3rd absorber respectively, and condenser and the second absorber also have cooling medium pipeline to connect with outside respectively Logical, 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.
40. the dynamic co-feeding system of heat, is in the heat described in the 39th moves co-feeding system, to cancel evaporator, engine is had The second generator has condensate liquid pipeline and outside to connect again after exhaust passage is sequentially communicated generator, evaporator and the second generator It is logical be adjusted to engine have exhaust passage be sequentially communicated generator and the second generator after the second generator have condensate line again Road and ft connection, have refrigerant steam channel to be connected respectively with absorber and the 3rd absorber evaporator and are adjusted to engine increasing If exhaust passage is connected with absorber and the 3rd absorber respectively, there is cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump Being adjusted to the second cryogen liquid pump has cryogen liquid pipeline and ft connection, and condenser is had into cryogen liquid pipeline through cryogen liquid pump and evaporation Device connection, which is adjusted to condenser, has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
41. the dynamic co-feeding system of heat, is that in the heat described in the 39th moves co-feeding system, engine is had into exhaust passage successively The second generator has condensate liquid pipeline and ft connection to be adjusted to power again after connection generator, evaporator and the second generator Machine have exhaust passage be sequentially communicated generator and the second generator after the second generator have condensate liquid pipeline and ft connection again, The rear heat exchange that engine has the second steam channel to be connected with heat exchanger there are into the second condensate liquid pipeline and ft connection again The finisher that being adjusted to engine has the second steam channel to be connected with evaporator has the second condensate liquid pipeline and ft connection again, Engine sets up the rear heat exchange that the 3rd steam channel connects with heat exchanger the 3rd condensate liquid pipeline and ft connection again, Form the dynamic co-feeding system of heat.
42. the dynamic co-feeding system of heat, is in the heat described in the 41st moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage connected respectively with absorber and the 3rd absorber be adjusted in the lump engine have the second steam channel respectively with absorber Connected with the 3rd absorber, there is cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump and be adjusted to the second cryogen liquid pump and have cold Agent liquid pipeline and ft connection, have cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and are adjusted to condenser and have cold Agent liquid pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump and ft connection.
43. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 are constituted; Engine connects working machine, and engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, moves Power machine also have exhaust passage connected with the second generator after the second generator have condensate liquid pipeline and ft connection, engine again Also the second steam channel is sequentially communicated generator and the finisher of evaporator the second condensate liquid pipeline and ft connection again, The rear heat exchange that engine also has the 3rd steam channel to be connected with heat exchanger has the 3rd condensate liquid pipeline and ft connection again; Second generator also has concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, and absorber also has dilute molten Liquid pipeline is connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline molten through solution pump and second Liquid heat exchanger is connected with generator, and generator also has concentrated solution pipeline to connect through the second solution heat exchanger and the second generator Logical, the second generator also has refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel and the 3rd hair The 3rd generator has cryogen liquid pipeline to be connected with the second cryogen liquid pump again after raw device connection, and the second cryogen liquid pump also has cryogen liquid Pipeline is connected with evaporator;3rd generator also has concentrated solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and the 3rd Absorber is connected, and the 3rd absorber also has weak solution pipeline to be connected through the 3rd solution heat exchanger with the 3rd generator, the 3rd hair Raw device also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, Evaporator also has refrigerant steam channel to be connected respectively with absorber and the 3rd absorber;Condenser and the second absorber also have respectively Cooling medium pipeline and ft connection, absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, heat Exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
44. the dynamic co-feeding system of heat, is in the heat described in the 43rd moves co-feeding system, to cancel evaporator, engine is had Second steam channel is sequentially communicated generator and the finisher of evaporator has the second condensate liquid pipeline to be adjusted with ft connection again For engine have second channel connected with generator after generator have the second condensate liquid pipeline and ft connection again, by evaporator Have refrigerant steam channel connected respectively with absorber and the 3rd absorber be adjusted to engine set up the second steam channel respectively with Absorber and the connection of the 3rd absorber, have cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and are adjusted to condenser There is cryogen liquid pipeline through cryogen liquid pump and ft connection, there is cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump and be adjusted to Second cryogen liquid pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
45. the dynamic co-feeding system of heat, is that in the heat described in the 43rd moves co-feeding system, engine is had into the second steam channel Being sequentially communicated the finisher of generator and evaporator and having the second condensate liquid pipeline and ft connection to be adjusted to engine again has the Generator has the second condensate liquid pipeline and ft connection again after two passages are connected with generator, has the 3rd steam to lead in engine The rear heat exchange that road is connected with heat exchanger has the 3rd condensate liquid pipeline to be adjusted to engine with ft connection again the 3rd steaming The finisher that vapour passage is connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, and engine is set up the 4th steam and led to The rear heat exchange that road is connected with heat exchanger has the 4th condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
46. the dynamic co-feeding system of heat, is in the heat described in the 45th moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage connected respectively with absorber and the 3rd absorber be adjusted to engine have the 3rd steam channel respectively with absorber and Three absorbers are connected, and are had cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and are adjusted to condenser and have cryogen liquid pipe Road has cryogen liquid pipeline to connect with evaporator to be adjusted to the second cryogen liquid through cryogen liquid pump and ft connection, by the second cryogen liquid pump Pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
47. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 evaporator and the second cryogen Liquid pump is constituted;Engine connects working machine, and engine has live steam passage and a ft connection, engine or also exhaust passage with Ft connection, engine also have exhaust passage connected with the second generator after the second generator have again condensate liquid pipeline with it is outside Connection, engine also have the second steam channel be sequentially communicated generator, evaporator and the second evaporator after the second evaporator again There are the second condensate liquid pipeline and a ft connection, engine also has rear heat exchange that the 3rd steam channel connects with heat exchanger again There are the 3rd condensate liquid pipeline and ft connection;Generator also has concentrated solution pipeline through solution pump and solution heat exchanger and absorber Connection, absorber also has weak solution pipeline to be connected through solution heat exchanger with generator, generator also have refrigerant steam channel and The 3rd generator has cryogen liquid pipeline to be connected through the second cryogen liquid pump with evaporator again after the connection of 3rd generator, and evaporator is also There is refrigerant steam channel to be connected with absorber;Second generator also has concentrated solution pipeline to be handed over through the second solution pump and the second solution heat Parallel operation is connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline to connect through the second solution heat exchanger and the second absorber Logical, the second absorber also has weak solution pipeline to be connected through the 3rd solution pump and the 3rd solution heat exchanger with the 3rd generator, the Three generators also have concentrated solution pipeline to be connected through the 3rd solution heat exchanger with the second generator, and the second generator also has cryogen steaming Vapour passage is connected with the second absorber, and the 3rd generator also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen Liquid pipeline is connected through cryogen liquid pump with the second evaporator, and the second evaporator also has refrigerant steam channel to be connected with the 3rd absorber; Condenser and the second absorber also have cooling medium pipeline and a ft connection respectively, absorber and the 3rd absorber also have respectively by Medium pipeline and ft connection are heated, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
48. the dynamic co-feeding system of heat, is in the heat described in the 47th moves co-feeding system, to cancel evaporator, engine is had The second evaporator has the second condensate liquid pipeline again after second steam channel is sequentially communicated generator, evaporator and the second evaporator Being adjusted to engine with ft connection has the second steam channel to be sequentially communicated the second evaporator after generator and the second evaporator There are the second condensate liquid pipeline and ft connection again, there is refrigerant steam channel to be connected with absorber evaporator and be adjusted to engine increasing If the second steam channel is connected with absorber, having cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump, to be adjusted to second cold Agent liquid pump has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
49. the dynamic co-feeding system of heat, is that in the heat described in the 47th moves co-feeding system, engine is had into the second steam channel The second evaporator has the second condensate liquid pipeline and ft connection to adjust again after being sequentially communicated generator, evaporator and the second evaporator It is whole for engine have the second steam channel be sequentially communicated generator and the second evaporator after the second evaporator have the second condensation again Liquid pipeline and ft connection, have the 3rd condensation again by the rear heat exchange that engine has the 3rd steam channel to be connected with heat exchanger The finisher that liquid pipeline is adjusted to engine with ft connection and has the 3rd steam channel to be connected with evaporator has the 3rd condensation again Liquid pipeline and ft connection, engine sets up the rear heat exchange that the 4th steam channel connects with heat exchanger the 4th condensation again Liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
50. the dynamic co-feeding system of heat, is in the heat described in the 49th moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and the second cryogen liquid pump is had Cryogen liquid pipeline is connected with evaporator to be adjusted to the second cryogen liquid pump and has cryogen liquid pipeline and a ft connection, forms the dynamic alliance system of heat System.
51. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, 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 are constituted; Engine connects working machine, and engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, moves Power machine also have exhaust passage connected with the second generator after the second generator have condensate liquid pipeline and ft connection, engine again Also the second steam channel is sequentially communicated generator and the finisher of evaporator the second condensate liquid pipeline and ft connection again, The rear heat exchange that engine also has the 3rd steam channel to be connected with heat exchanger has the 3rd condensate liquid pipeline and ft connection again; Generator also has concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, and absorber also has weak solution pipeline warp Solution heat exchanger is connected with generator, generator also have refrigerant steam channel connected with the 3rd generator after the 3rd generator There is cryogen liquid pipeline to be connected with the second cryogen liquid pump again, the second cryogen liquid pump also has cryogen liquid pipeline to be connected with evaporator;Second Generator also has concentrated solution pipeline to be connected through the second solution pump and the second solution heat exchanger with the 3rd absorber, the 3rd absorber Also weak solution pipeline is connected through the second solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline through Three solution pumps and the 3rd solution heat exchanger are connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the 3rd solution Heat exchanger is connected with the second generator, and the second generator also has refrigerant steam channel to be connected with the second absorber, and the 3rd occurs Device also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, steams Hair device also has refrigerant steam channel to be connected respectively with absorber and the 3rd absorber;Condenser and the second absorber also have cold respectively But medium pipeline and ft connection, absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, and heat is handed over Parallel operation also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
52. the dynamic co-feeding system of heat, is in the heat described in the 51st moves co-feeding system, to cancel evaporator, engine is had Second steam channel is sequentially communicated generator and the finisher of evaporator has the second condensate liquid pipeline to be adjusted with ft connection again For engine have the second steam channel connected with generator after generator have the second condensate liquid pipeline and ft connection again, will steam Hair device have refrigerant steam channel connect respectively with absorber and the 3rd absorber be adjusted to engine set up the second steam channel divide Do not connected with absorber and the 3rd absorber, having cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump, to be adjusted to second cold Agent liquid pump has cryogen liquid pipeline and ft connection, has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and is adjusted to Condenser has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
53. the dynamic co-feeding system of heat, is that in the heat described in the 51st moves co-feeding system, engine is had into the second steam channel Being sequentially communicated the finisher of generator and evaporator and having the second condensate liquid pipeline and ft connection to be adjusted to engine again has the Generator has the second condensate liquid pipeline and ft connection again after two steam channels are connected with generator, and engine is had into the 3rd steaming The rear heat exchange that vapour passage is connected with heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to engine again the The finisher that three steam channels are connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, and engine sets up the 4th steaming The rear heat exchange that vapour passage is connected with heat exchanger has the 4th condensate liquid pipeline and ft connection again, forms the dynamic alliance system of heat System.
54. the dynamic co-feeding system of heat, is in the heat described in the 53rd moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage connected respectively with absorber and the 3rd absorber be adjusted to engine have the 3rd steam channel respectively with absorber and Three absorbers are connected, and are had cryogen liquid pipeline to be connected with evaporator the second cryogen liquid pump and are adjusted to the second cryogen liquid pump and have cryogen liquid Pipeline and ft connection, have cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and are adjusted to condenser and have cryogen liquid Pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump and ft connection.
55. the dynamic co-feeding system of heat, it is that any hot the 1st, described in 3,5,7,9,11,13,15 is moved in co-feeding system, increases Plus newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, it will absorb Device has weak solution pipeline to connect with the second absorber through solution heat exchanger to be adjusted to absorber and have weak solution pipeline and newly-increased suction Device connection is received, newly-increased absorber also has weak solution pipeline to be absorbed through newly-increased solution pump and newly-increased solution heat exchanger with newly-increased second Device is connected, and newly-increased second absorber has weak solution pipeline to be absorbed through newly-increased solution heat exchanger and solution heat exchanger and second again Device is connected, and evaporator is set up refrigerant steam channel and connected with newly-increased absorber, and condenser sets up cryogen liquid pipeline through newly-increased cryogen Liquid pump increases absorber newly after being connected with newly-increased absorber has refrigerant steam channel to be connected with newly-increased second absorber again, and newly-increased the Two absorbers also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
56. it is that any hot the 17th, described in 19,21,25,26 is moved in co-feeding system, increase is new the dynamic co-feeding system of heat Increase absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, absorber is had Weak solution pipeline is connected through solution heat exchanger with generator to be adjusted to absorber and has weak solution pipeline to be connected with newly-increased absorber, Newly-increased absorber also has weak solution pipeline to be connected through newly-increased solution pump and newly-increased solution heat exchanger with newly-increased second absorber, newly Increase the second absorber has weak solution pipeline to be connected through newly-increased solution heat exchanger and solution heat exchanger with generator again, evaporator Set up refrigerant steam channel to connect with newly-increased absorber, condenser sets up cryogen liquid pipeline through newly-increased cryogen liquid pump and newly-increased absorption Increase absorber after device connection newly has refrigerant steam channel to be connected with newly-increased second absorber again, and newly-increased second absorber also has quilt Medium pipeline and ft connection are heated, the dynamic co-feeding system of heat is formed.
57. it is the dynamic connection of any hot the 27th, described in 29,31,33,35,37,39,41,43,45 the dynamic co-feeding system of heat For in system, the newly-increased absorber of increase, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and new solubilization liquid heat are handed over Parallel operation, has weak solution pipeline to be connected through solution heat exchanger with the second absorber absorber and is adjusted to absorber and has weak solution pipe Road is connected with newly-increased absorber, and newly-increased absorber also has the newly-increased solution pump of weak solution pipeline warp and newly-increased solution heat exchanger and new Increase the connection of the second absorber, newly-increased second absorber has weak solution pipeline through newly-increased solution heat exchanger and solution heat exchanger again Connected with the second absorber, evaporator is set up refrigerant steam channel and connected with newly-increased absorber, has refrigerant vapour to lead in generator The 3rd generator has cryogen liquid pipeline to connect with the second cryogen liquid pump to be adjusted to generator again after road is connected with the 3rd generator Have refrigerant steam channel connected with the 3rd generator after the 3rd generator have again cryogen liquid pipeline respectively with the second cryogen liquid pump Connected with newly-increased cryogen liquid pump, newly-increased cryogen liquid pump also has cryogen liquid pipeline to increase absorber newly again after being connected with newly-increased absorber There is refrigerant steam channel to be connected with newly-increased second absorber, newly-increased second absorber also has heated medium pipeline to connect with outside It is logical, form the dynamic co-feeding system of heat.
58. the dynamic co-feeding system of heat, is in any hot described in 1-57 moves co-feeding system, to cancel heat exchanger, take Disappear the heated medium pipeline connected with heat exchanger, forms the dynamic co-feeding system of heat.
Brief description of the drawings:
Fig. 1 is according to 1st kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 2 is according to 2nd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 3 is according to 3rd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 4 is according to 4th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 5 is according to 5th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 6 is according to 6th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 7 is according to 7th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 8 is according to 8th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 9 is according to 9th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 10 is according to 10th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 11 is according to 11st kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 12 is according to 12nd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 13 is according to 13rd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 14 is according to 14th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 15 is according to 15th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 16 is according to 16th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 17 is according to 17th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 18 is according to 18th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 19 is according to 19th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 20 is according to 20th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 21 is according to 21st kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 22 is according to 22nd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 23 is according to 23rd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 24 is according to 24th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 25 is according to 25th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 26 is according to 26th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 27 is according to 27th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 28 is according to 28th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
In figure, 1- generators, the generators of 2- second, 3- absorbers, the absorbers of 4- second, 5- condensers, 6- evaporators, 7- Solution pump, the solution pumps of 8- second, 9- cryogen liquid pumps, 10- solution choke valves, 11- solution heat exchangers, 12- heat exchangers, 13- Engine, 14- working machines, the solution heat exchangers of 15- second, the generators of 16- the 3rd, the absorbers of 17- the 3rd, the solution of 18- the 3rd Pump, the solution heat exchangers of 19- the 3rd, the evaporators of 20- second, 21- the second cryogen liquid pumps;A- increases absorber, B- newly-increased second newly Absorber, C- increases solution pump newly, and D- increases cryogen liquid pump newly, and E- increases solution heat exchanger newly.
Here following explanation is also provided:
(1) live steam --- refer to converted for hot merit, pressure and temperature is above the engine working media that draws gas.
(2) steam discharge --- refer to the low-pressure steam in engine exit working media, such as steam turbine outlet moist steam.
(3) second steam --- a certain position of engine is extracted out, pressure and temperature is above the working media of steam discharge.
(4) the 3rd steam --- the work that a certain position of engine is extracted out, pressure and temperature is above the second steam is situated between Matter.
(4) the 4th steam --- the work that a certain position of engine is extracted out, pressure and temperature is above the 3rd steam is situated between Matter.
(5) the 5th steam --- the work that a certain position of engine is extracted out, pressure and temperature is above the 4th steam is situated between Matter.
(6) condensate liquid --- the liquid of steam discharge exothermic condensation formation.
(7) second condensate liquids --- the liquid of the second steam exothermic condensation formation.
(8) the 3rd condensate liquids --- the liquid of the 3rd steam exothermic condensation formation.
(9) the 4th condensate liquids --- the liquid of the 4th steam exothermic condensation formation.
(10) the 5th condensate liquids --- the liquid of the 5th steam exothermic condensation formation.
(11) it is relevant with engine, but be not related to operation principle of the present invention, part (such as dynamical system unrelated to the invention Backheat heat exchanger components etc.) and flow (recovery of such as condensate liquid), not in express ranges of the present invention.
(12) the refrigerant vapour exothermic condensation formation cryogen liquid of cryogen liquid and condensate liquid --- generator solution release, power The working steam exothermic condensation formation condensate liquid of machine;Claim cryogen liquid when refrigerant vapour and working steam is same materials.
(13) engine exports the utilization of steam discharge --- for the dynamic co-feeding system of specific heat, the profit of exhaust steam heat load With being 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 not by Utilize.Therefore, summarizing steam discharge utilization power using " engine 1 or also exhaust passage and ft connection " such statement.
(14) effect of choke valve and solution choke valve --- for fluid decompression, it can be taken by gravity pressure difference or pipe resistance Generation.
(15) by taking Figure 14 as an example, handed over by the 3rd generator 16, the 3rd absorber 17, the 3rd solution pump 18, the second solution heat Parallel operation 15, condenser 5, the circulation of the evaporator 20 of cryogen liquid pump 9 and second composition, when making working medium with ammonia-water solution, the 3rd occurs Device is referred to as rectifying column by custom --- and now as needed, the 3rd generator 16 sets up cooling medium pipeline and ft connection.
Embodiment:
First it is noted that in the statement of structure and flow, it is inessential in the case of do not repeat;To apparent Flow do not state.The present invention is described in detail with example below in conjunction with the accompanying drawings.
Heat shown in Fig. 1 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine and working machine institute Composition;Engine 13 connects working machine 14, and engine 13 has live steam passage and a ft connection, engine 13 also have exhaust passage with Ft connection, engine 13 also has exhaust passage to be sequentially communicated the second generation after generator 1, the generator 2 of evaporator 6 and second Device 2 has condensate liquid pipeline and ft connection again, and engine 13 also has the second steam channel is warm after being connected with heat exchanger 12 to hand over Parallel operation 12 has the second condensate liquid pipeline and ft connection again;Second generator 2 also has concentrated solution pipeline through the second solution pump 8 and molten Liquid heat exchanger 11 is connected with absorber 3, and absorber 3 also has weak solution pipeline through the absorber 4 of solution heat exchanger 11 and second Connection, the second absorber 4 also has weak solution pipeline to be connected through solution pump 7 with generator 1, and generator 1 also has concentrated solution pipeline warp Solution choke valve 10 is connected with the second generator 2, and the second generator 2 also has refrigerant steam channel to be connected with the second absorber 4, is sent out Raw device 1 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipeline through cryogen liquid pump 9 and evaporator 6 Connection, evaporator 6 also has refrigerant steam channel to be connected with absorber 3, and the absorber 4 of condenser 5 and second also has cooling to be situated between respectively Matter pipeline and ft connection, absorber 3 also have heated medium pipeline and ft connection, and heat exchanger 12 also has heated medium Pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the second steam, Second steam in heat exchanger 12 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 13 provide steam discharge to generator 1, the generator 2 of evaporator 6 and second, and steam discharge flows through generator 1, the generator 2 of evaporator 6 and second And progressively heat release is into discharge after condensate liquid, engine 13 also has steam discharge discharge;The concentrated solution of second generator 2 is through the second solution Pump 8 and solution heat exchanger 11 enter absorber 3, absorb refrigerant vapour and heat release is in heated medium, the weak solution of absorber 3 Enter the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour and heat release in cooling medium, the second absorber 4 it is dilute Solution enters generator 1, heat absorption release refrigerant vapour through solution pump 7 and provided to condenser 5, and the concentrated solution of generator 1 is through solution The reducing pressure by regulating flow of choke valve 10 enters the second generator 2, heat absorption release refrigerant vapour and provided to the second absorber 4;Condenser 5 Refrigerant vapour heat release is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 5 enters evaporator 6, heat absorption through the pressurization of cryogen liquid pump 9 There is provided into refrigerant vapour and to absorber 3, form the dynamic co-feeding system of heat.
Heat shown in Fig. 2 moves what co-feeding system was realized in:
In the heat shown in Fig. 1 moves co-feeding system, there is exhaust passage to be sequentially communicated generator 1, evaporator 6 in engine 13 Having condensate liquid pipeline to be adjusted to engine 13 with ft connection again with the second generator 2 after the second generator 2 has exhaust passage Second generator 2 has condensate liquid pipeline and ft connection again after being connected with the generator 2 of generator 1 and second, by engine 13 The rear heat exchange 12 for having the second steam channel to be connected with heat exchanger 12 has the second condensate liquid pipeline to be adjusted with ft connection again The finisher 6 for having the second steam channel to be connected with evaporator 6 for engine 13 has the second condensate liquid pipeline and ft connection again, Engine 13 set up the rear heat exchange 12 that the 3rd steam channel connects with heat exchanger 12 have again the 3rd condensate liquid pipeline with it is outer Portion is connected, and forms the dynamic co-feeding system of heat.
Heat shown in Fig. 3 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine and the second solution heat are handed over Parallel operation is constituted;Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has steam discharge Second generator 2 has condensate liquid pipeline and ft connection again after passage and the second generator 2, and engine 13 also has the second steam Passage is sequentially communicated generator 1 and the finisher 6 of evaporator 6 the second condensate liquid pipeline and ft connection, engine 13 again The rear heat exchange 12 that also the 3rd steam channel is connected with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again;The Two generators 2 also have concentrated solution pipeline to be connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, and absorber 3 also has Weak solution pipeline is connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution pump 7 and second solution heat exchanger 15 connected with generator 1, generator 1 also have concentrated solution pipeline through the second solution heat exchanger 15 Connected with the second generator 2, the second generator 2 also has refrigerant steam channel to be connected with the second absorber 4, and generator 1 is also cold Agent steam channel is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected through cryogen liquid pump 9 with evaporator 6, evaporator 6 Also refrigerant steam channel is connected with absorber 3, and the absorber 4 of condenser 5 and second also has cooling medium pipeline and outside respectively Connection, absorber 3 also has heated medium pipeline and ft connection, and heat exchanger 12 also has heated medium pipeline to connect with outside It is logical.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 3rd steam, 3rd steam in heat exchanger 12 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provide the second steam to generator 1 and evaporator 6, the second steam flow through generator 1 and evaporator 6, heat release into condensate liquid it Discharged by the second condensate liquid pipeline, engine 13 provides steam discharge, steam discharge heat release in the second generator 2 to the second generator 2 Discharged after into condensate liquid;The concentrated solution of second generator 2 through the second solution pump 8 and solution heat exchanger 11 enter absorber 3, Absorb refrigerant vapour and heat release is in heated medium, the weak solution of absorber 3 enters the second absorber through solution heat exchanger 11 4th, absorb refrigerant vapour and heat release is in cooling medium, the weak solution of the second absorber 4 is through the solution heat exchanger of solution pump 7 and second 15 enter generator 1, heat absorption release refrigerant vapour and are provided to condenser 5, and the concentrated solution of generator 1 is through the second solution heat exchanger 15 enter the second generator 2, heat absorption release refrigerant vapour and are provided to the second absorber 4;The refrigerant vapour heat release of condenser 5 in Cooling medium into cryogen liquid, the cryogen liquid of condenser 5 enter evaporator 6 through the pressurization of cryogen liquid pump 9, absorb heat into refrigerant vapour and to Absorber 3 is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Fig. 4 moves what co-feeding system was realized in:
In the heat shown in Fig. 3 moves co-feeding system, engine 13 has the second steam channel to be sequentially communicated generator 1 and evaporation The finisher 6 of device 6 has the second condensate liquid pipeline to be adjusted to engine 13 with ft connection again the second steam channel and generation Generator 1 has the second condensate liquid pipeline and ft connection again after device 1 is connected, and has the 3rd steam channel to be handed over heat in engine 13 The rear heat exchange 12 of the connection of parallel operation 12 has the 3rd condensate liquid pipeline to be adjusted to engine 13 with ft connection again the 3rd steam The finisher 6 that passage is connected with evaporator 6 has the 3rd condensate liquid pipeline and ft connection again, and engine 13 sets up the 4th steam The rear heat exchange 12 that passage is connected with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again, forms the dynamic alliance system of heat System.
Heat shown in Fig. 5 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Two solution heat exchangers, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine 13 connects working machine 14, Engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage to be sequentially communicated the 3rd generator 16, generator 1st, second generator 2 has condensate liquid pipeline and a ft connection again after the generator 2 of evaporator 6 and second, and engine 13 also has the The rear heat exchange 12 that two steam channels are connected with heat exchanger 12 has the second condensate liquid pipeline and ft connection again;Second occurs Device 2 also has concentrated solution pipeline to be connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution Pipeline is connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution pump 7 and hair Raw device 1 is connected, and generator 1 also has concentrated solution pipeline to be connected through solution choke valve 10 with the second generator 2, and the second generator 2 is also There is refrigerant steam channel to be connected with the second absorber 4, generator 1 also has refrigerant steam channel to be connected with the 3rd absorber 17, the Three absorbers 17 also have weak solution pipeline to be connected through the 3rd solution pump 18 and the second solution heat exchanger 15 with the 3rd generator 16, 3rd generator 16 also has concentrated solution pipeline to be connected through the second solution heat exchanger 15 with the 3rd absorber 17, the 3rd generator 16 Also refrigerant steam channel is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected through cryogen liquid pump 9 with evaporator 6, Evaporator 6 also has refrigerant steam channel to be connected with absorber 3, and condenser 5, the second absorber 4 and the 3rd absorber 17 are also distinguished There are cooling medium pipeline and ft connection, absorber 3 also has heated medium pipeline and ft connection, and heat exchanger 12 also has quilt Heat medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the second steam, Second steam in heat exchanger 12 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 13 provide steam discharge to the 3rd generator 16, generator 1, the generator 2 of evaporator 6 and second, and steam discharge flows through the 3rd generator 16, hair Raw device 1, evaporator 6 with the second generator 2 and progressively heat release into discharge after condensate liquid;The concentrated solution of second generator 2 is through Two solution pumps 8 and solution heat exchanger 11 enter absorber 3, absorb refrigerant vapour and heat release is in heated medium, absorber 3 Weak solution enters the second absorber 4 through solution heat exchanger 11, absorbs refrigerant vapour and heat release is in cooling medium, the second absorber 4 weak solution enters generator 1, heat absorption release refrigerant vapour through solution pump 7 and provided to the 3rd absorber 17, generator 1 Concentrated solution enters the second generator 2, heat absorption release refrigerant vapour through solution choke valve 10 and provided to the second absorber 4;3rd The weak solution of absorber 17 enters the 3rd generator 16, heat absorption through the 3rd solution pump 18 and the second solution heat exchanger 15 and discharges cold Agent steam is simultaneously provided to condenser 5, and the concentrated solution of the 3rd generator 16 enters the 3rd absorber through the second solution heat exchanger 15 17th, absorb refrigerant vapour and heat release is in cooling medium;The refrigerant vapour heat release of condenser 5, into cryogen liquid, is condensed in cooling medium The cryogen liquid of device 5 enters evaporator 6 through the pressurization of cryogen liquid pump 9, absorbs heat into refrigerant vapour and provided to absorber 3, forms heat dynamic Co-feeding system.
Heat shown in Fig. 6 moves what co-feeding system was realized in:
In the heat shown in Fig. 5 moves co-feeding system, there is exhaust passage to be sequentially communicated the 3rd generator 16, hair in engine 13 Second generator 2 has condensate liquid pipeline and ft connection to be adjusted to power again after raw device 1, the generator 2 of evaporator 6 and second Machine 13 has exhaust passage to be sequentially communicated the 3rd generator 16, the generator 2 of generator 1 and second, and the second generator 2 has cold again afterwards Lime set pipeline and ft connection, the rear heat exchange 12 that engine 13 has the second steam channel to be connected with heat exchanger 12 is had again Second condensate liquid pipeline is adjusted to the finisher 6 that engine 13 has the second steam channel to be connected with evaporator 6 with ft connection There are the second condensate liquid pipeline and ft connection again, engine 13 sets up heat friendship after the 3rd steam channel is connected with heat exchanger 12 Parallel operation 12 has the 3rd condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 7 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Engine 13 connects work Machine 14, engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage to be sequentially communicated the He of the 3rd generator 16 Second generator 2 has condensate liquid pipeline and a ft connection again after second generator 2, engine 13 also have the second steam channel according to The finisher 6 of secondary connection generator 1 and evaporator 6 has the second condensate liquid pipeline and a ft connection again, and engine 13 also has the The rear heat exchange 12 that three steam channels are connected with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again;Second occurs Device 2 also has concentrated solution pipeline to be connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution Pipeline is connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution pump 7 and the Two solution heat exchangers 15 are connected with generator 1, and generator 1 also has concentrated solution pipeline through the second solution heat exchanger 15 and second Generator 2 is connected, and the second generator 2 also has refrigerant steam channel to be connected with the second absorber 4, and generator 1 also has refrigerant vapour Passage is connected with the 3rd absorber 17, and the 3rd absorber 17 also has weak solution pipeline to be handed over through the 3rd solution pump 18 and the 3rd solution heat Parallel operation 19 is connected with the 3rd generator 16, and the 3rd generator 16 also has concentrated solution pipeline through the 3rd solution heat exchanger 19 and the 3rd Absorber 17 is connected, and the 3rd generator 16 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipeline Connected through cryogen liquid pump 9 with evaporator 6, evaporator 6 also has refrigerant steam channel to be connected with absorber 3, condenser 5, second is inhaled Receive the absorber 17 of device 4 and the 3rd also has cooling medium pipeline and a ft connection respectively, absorber 3 also have heated medium pipeline with Ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 3rd steam, 3rd steam in heat exchanger 12 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provide the second steam to generator 1 and evaporator 6, the second steam flow through generator 1 and evaporator 6, heat release into condensate liquid it Discharged by the second condensate liquid pipeline, engine 13 provides steam discharge to the 3rd generator 16 and the second generator 2, steam discharge flows through the Three generators 16 with the second generator 2, progressively heat release discharged into after condensate liquid;The concentrated solution of second generator 2 is molten through second Liquid pump 8 and solution heat exchanger 11 enter absorber 3, absorb refrigerant vapour and heat release is in heated medium, absorber 3 it is dilute molten Liquid enters the second absorber 4 through solution heat exchanger 11, absorbs refrigerant vapour and heat release is in cooling medium, the second absorber 4 Weak solution enters generator 1, heat absorption release refrigerant vapour and to the 3rd absorber through the solution heat exchanger 15 of solution pump 7 and second 17 provide, and the concentrated solution of generator 1 enters the second generator 2, heat absorption release refrigerant vapour simultaneously through the second solution heat exchanger 15 There is provided to the second absorber 4;The weak solution of 3rd absorber 17 enters through the 3rd solution pump 18 and the 3rd solution heat exchanger 19 3rd generator 16, heat absorption release refrigerant vapour are simultaneously provided to condenser 5, and the concentrated solution of the 3rd generator 16 is through the 3rd solution heat Exchanger 19 enters the 3rd absorber 17, absorbs refrigerant vapour and heat release is in cooling medium;The refrigerant vapour heat release of condenser 5 in Cooling medium into cryogen liquid, the cryogen liquid of condenser 5 enter evaporator 6 through the pressurization of cryogen liquid pump 9, absorb heat into refrigerant vapour and to Absorber 3 is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Fig. 8 moves what co-feeding system was realized in:
Shown in Fig. 7 heat move co-feeding system in, by engine 13 have the second steam channel be sequentially communicated generator 1 and with The finisher 6 of evaporator 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel with Generator 1 connect after generator 1 have the second condensate liquid pipeline and ft connection again, by engine 13 have the 3rd steam channel with The rear heat exchange 12 of the connection of heat exchanger 12 has the 3rd condensate liquid pipeline to be adjusted to engine 13 with ft connection again the 3rd The finisher 6 that steam channel is connected with evaporator 6 has the 3rd condensate liquid pipeline and ft connection again, and engine 13 sets up the 4th The rear heat exchange 12 that steam channel is connected with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again, forms the dynamic connection of heat For system.
Heat shown in Fig. 9 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Two solution heat exchangers, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine 13 connects working machine 14, Engine 13 has live steam passage and a ft connection, engine 13 also have exhaust passage be sequentially communicated the second generator 2, generator 1, The 3rd generator 16 has condensate liquid pipeline and a ft connection again after the generator 16 of evaporator 6 and the 3rd, and engine 13 also has the The rear heat exchange 12 that two steam channels are connected with heat exchanger 12 has the second condensate liquid pipeline and ft connection again;Generator 1 Also concentrated solution pipeline is connected through solution pump 7 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipeline warp Solution heat exchanger 11 is connected with generator 1, and generator 1 also has refrigerant steam channel to be connected with the second absorber 4, and second absorbs Device 4 also has weak solution pipeline to be connected through the second solution pump 8 and the second solution heat exchanger 15 with the 3rd absorber 17, and the 3rd absorbs Device 17 also has weak solution pipeline to be connected through the 3rd solution pump 18 with the second generator 2, and the second generator 2 also has concentrated solution pipeline warp Solution choke valve 10 is connected with the 3rd generator 16, and the 3rd generator 16 also has concentrated solution pipeline through the second solution heat exchanger 15 Connected with the second absorber 4, the 3rd generator 16 also has refrigerant steam channel to be connected with the 3rd absorber 17, the second generator 2 Also refrigerant steam channel is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected through cryogen liquid pump 9 with evaporator 6, Evaporator 6 also has refrigerant steam channel to be connected with absorber 3, and condenser 5, the second absorber 4 and the 3rd absorber 17 are also distinguished There are cooling medium pipeline and ft connection, absorber 3 also has heated medium pipeline and ft connection, and heat exchanger 12 also has quilt Heat medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the second steam, Second steam in heat exchanger 12 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 13 provide steam discharge to the second generator 2, generator 1, the generator 16 of evaporator 6 and the 3rd, and steam discharge flows through the second generator 2, hair Raw device 1, evaporator 6 with the 3rd generator 16 and progressively heat release into discharge after condensate liquid;The concentrated solution of generator 1 is through solution pump 7 and solution heat exchanger 11 enter absorber 3, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 3 is passed through Solution heat exchanger 11 enters generator 1, heat absorption release refrigerant vapour and provided to the second absorber 4;Second absorber 4 it is dilute Solution enters the 3rd absorber 17 through the second solution pump 8 and the second solution heat exchanger 15, absorbs refrigerant vapour and heat release is in cold But medium, the weak solution of the 3rd absorber 17 enter the second generator 2 through the 3rd solution pump 18, absorb release refrigerant vapour and to Condenser 5 is provided, and the concentrated solution of the second generator 2 is cold into the 3rd generator 16, heat absorption release through the throttling of solution choke valve 10 Agent steam is simultaneously provided to the 3rd absorber 17, and the concentrated solution of the 3rd generator 16 enters second through the second solution heat exchanger 15 and inhaled Device 4 is received, refrigerant vapour is absorbed and heat release is in cooling medium;The refrigerant vapour heat release of condenser 5 in cooling medium into cryogen liquid, it is cold The cryogen liquid of condenser 5 enters evaporator 6 through the pressurization of cryogen liquid pump 9, absorbs heat into refrigerant vapour and provided to absorber 3, forms heat Dynamic co-feeding system.
Heat shown in Figure 10 moves what co-feeding system was realized in:
In the heat shown in Fig. 9 moves co-feeding system, there is exhaust passage to be sequentially communicated the second generator 2, hair in engine 13 The 3rd generator 16 has condensate liquid pipeline and ft connection to be adjusted to power again after raw device 1, the generator 16 of evaporator 6 and the 3rd Machine 13 has exhaust passage to be sequentially communicated the second generator 2, the generator 16 of generator 1 and the 3rd, and the 3rd generator 16 has cold again afterwards Lime set pipeline and ft connection, the rear heat exchange 12 that engine 13 has the second steam channel to be connected with heat exchanger 12 is had again Second condensate liquid pipeline is adjusted to the finisher 6 that engine 13 has the second steam channel to be connected with evaporator 6 with ft connection There are the second condensate liquid pipeline and ft connection again, engine 13 sets up heat friendship after the 3rd steam channel is connected with heat exchanger 12 Parallel operation 12 has the 3rd condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
Heat shown in Figure 11 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Two solution heat exchangers, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine 13 connects working machine 14, Engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage to be sequentially communicated the second generator 2 and the 3rd hair The 3rd generator 16 has condensate liquid pipeline and ft connection again after raw device 16, and engine 13 also has the second steam channel to connect successively The finisher 6 of logical generator 1 and evaporator 6 has the second condensate liquid pipeline and ft connection again, and engine 13 also has the 3rd to steam The rear heat exchange 12 that vapour passage is connected with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again;Generator 1 also has Concentrated solution pipeline is connected through solution pump 7 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipeline through solution Heat exchanger 11 is connected with generator 1, and generator 1 also has refrigerant steam channel to be connected with the second absorber 4, the second absorber 4 Also weak solution pipeline is connected through the second solution pump 8 and the second solution heat exchanger 15 with the 3rd absorber 17, the 3rd absorber 17 also have weak solution pipeline to be connected through the 3rd solution pump 18 with the second generator 2, and the second generator 2 also has concentrated solution pipeline through molten Liquid choke valve 10 is connected with the 3rd generator 16, the 3rd generator 16 also have concentrated solution pipeline through the second solution heat exchanger 15 with Second absorber 4 is connected, and the 3rd generator 16 also has refrigerant steam channel to be connected with the 3rd absorber 17, and the second generator 2 is also There is refrigerant steam channel to be connected with condenser 5, condenser 5 also has cryogen liquid pipeline to be connected through cryogen liquid pump 9 with evaporator 6, steam Hair device 6 also has refrigerant steam channel to be connected with absorber 3, and condenser 5, the second absorber 4 and the 3rd absorber 17 also have respectively Cooling medium pipeline and ft connection, absorber 3 also have heated medium pipeline and ft connection, and heat exchanger 12, which also has, to be added Heat medium pipeline and ft connection.
(2) in flow, compared with the dynamic co-feeding system of heat shown in Figure 10, difference is:Engine 13 is to the He of generator 1 Evaporator 6 provides the second steam, and the second steam flows through generator 1 with evaporator 6, progressively heat release is into cold through second after condensate liquid Lime set pipeline is discharged, and engine 13 provides steam discharge to the second generator 2 and the 3rd generator 16.
Heat shown in Figure 12 moves what co-feeding system was realized in:
In the heat shown in Figure 11 moves co-feeding system, there is the second steam channel to be sequentially communicated the He of generator 1 in engine 13 The finisher 6 of evaporator 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel with Generator 1 connect after generator 1 have the second condensate liquid pipeline and ft connection again, by engine 13 have the 3rd steam channel with The rear heat exchange 12 of the connection of heat exchanger 12 has the 3rd condensate liquid pipeline to be adjusted to engine 13 with ft connection again the 3rd The finisher 6 that steam channel is connected with evaporator 6 has the 3rd condensate liquid pipeline and ft connection again, and engine 13 sets up the 4th The rear heat exchange 12 that steam channel is connected with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again, forms the dynamic connection of heat For system.
Heat shown in Figure 13 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat are handed over Parallel operation, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Engine 13 connects work Make machine 14, engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage to connect it with the 3rd generator 16 The 3rd generator 16 has condensate liquid pipeline and ft connection again afterwards, and engine 13 also has the second steam channel to be sequentially communicated generator 1 and second second generator 2 after generator 2 have the second condensate liquid pipeline and ft connection again, engine 13 also has the 3rd to steam The finisher 6 that vapour passage is connected with evaporator 6 has the 3rd condensate liquid pipeline and ft connection again, and engine 13 also has the 4th to steam The rear heat exchange 12 that vapour passage is connected with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again;Generator 1 also has Concentrated solution pipeline is connected through solution pump 7 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipeline through solution Heat exchanger 11 is connected with generator 1, and generator 1 also has refrigerant steam channel to be connected with the second absorber 4, the second absorber 4 Also weak solution pipeline is connected through the second solution pump 8 and the second solution heat exchanger 15 with the 3rd absorber 17, the 3rd absorber 17 also have weak solution pipeline to be connected through the 3rd solution pump 18 and the 3rd solution heat exchanger 19 with the second generator 2, and second occurs Device 2 also has concentrated solution pipeline to be connected through the 3rd solution heat exchanger 19 with the 3rd generator 16, and the 3rd generator 16 also has dense molten Liquid pipeline is connected through the second solution heat exchanger 15 with the second absorber 4, and the 3rd generator 16 also has refrigerant steam channel and the Three absorbers 17 are connected, and the second generator 2 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipeline Connected through cryogen liquid pump 9 with evaporator 6, evaporator 6 also has refrigerant steam channel to be connected with absorber 3, condenser 5, second is inhaled Receive the absorber 17 of device 4 and the 3rd also has cooling medium pipeline and a ft connection respectively, absorber 3 also have heated medium pipeline with Ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 4th steam, 4th steam in heat exchanger 12 heat release in heated medium into being discharged through the 4th condensate liquid pipeline after condensate liquid, engine 13 provide the 3rd steam to evaporator 6, the 3rd steam in evaporator 6 heat release into after condensate liquid through the 3rd condensate liquid tubes rows Go out, engine 13 provides the second steam to the generator 2 of generator 1 and second, the second steam flows through the generator of generator 1 and second 2nd, progressively heat release through the second condensate liquid pipeline into discharging after condensate liquid, and engine 13 provides steam discharge, row to the 3rd generator 16 Vapour heat release in the 3rd generator 16 is discharged into after condensate liquid;The concentrated solution of generator 1 is through solution pump 7 and solution heat exchanger 11 enter absorber 3, absorbing refrigerant vapour, simultaneously heat release is in heated medium, and the weak solution of absorber 3 is through solution heat exchanger 11 There is provided into generator 1, heat absorption release refrigerant vapour and to the second absorber 4;The weak solution of second absorber 4 is through the second solution The solution heat exchanger 15 of pump 8 and second enters the 3rd absorber 17, absorbs refrigerant vapour and heat release absorbs in cooling medium, the 3rd The weak solution of device 17 enters the second generator 2 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, absorbs release cryogen steaming Vapour is simultaneously provided to condenser 5, and the concentrated solution of the second generator 2 enters the 3rd generator 16 through the 3rd solution heat exchanger 19, inhaled Heat release refrigerant vapour is simultaneously provided to the 3rd absorber 17, and the concentrated solution of the 3rd generator 16 is entered through the second solution heat exchanger 15 Enter the second absorber 4, absorb refrigerant vapour and heat release is in cooling medium;The refrigerant vapour heat release of condenser 5 in cooling medium into Cryogen liquid, the cryogen liquid of condenser 5 enters evaporator 6 through the pressurization of cryogen liquid pump 9, absorbs heat into refrigerant vapour and carried to absorber 3 For forming the dynamic co-feeding system of heat.
Heat shown in Figure 14 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporator and the second cryogen liquid pump are constituted;Engine 13 connects Connect working machine 14, engine 13 has live steam passage and a ft connection, engine 13 also have exhaust passage be sequentially communicated generator 1, Second generator 2 has condensate liquid pipeline and ft connection, power again after evaporator 6, the second evaporator 20 and the second generator 2 The rear heat exchange 12 that machine 13 also has the second steam channel to be connected with heat exchanger 12 has the second condensate liquid pipeline to connect with outside again It is logical;Second generator 2 also has concentrated solution pipeline to be connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, absorber 3 also have weak solution pipeline to be connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline warp Solution pump 7 is connected with generator 1, and generator 1 also has concentrated solution pipeline to be connected through solution choke valve 10 with the second generator 2, the Two generators 2 also have refrigerant steam channel to be connected with the second absorber 4, and generator 1 also has refrigerant steam channel to occur with the 3rd The 3rd generator 16 has cryogen liquid pipeline to be connected with the second cryogen liquid pump 21 again after device 16 is connected, and the second cryogen liquid pump 21 also has Cryogen liquid pipeline is connected with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3;3rd generator 16 also has Concentrated solution pipeline is connected through the 3rd solution pump 18 and the second solution heat exchanger 15 with the 3rd absorber 17, and the 3rd absorber 17 is also There is weak solution pipeline to be connected through the second solution heat exchanger 15 with the 3rd generator 16, the 3rd generator 16 also has refrigerant vapour to lead to Road is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected through cryogen liquid pump 9 with the second evaporator 20, the second evaporator 20 also have refrigerant steam channel to be connected with the 3rd absorber 17, and the absorber 4 of condenser 5 and second also has cooling medium pipeline respectively With ft connection, the absorber 17 of absorber 3 and the 3rd also has heated medium pipeline and ft connection respectively, and heat exchanger 12 is also There are heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the second steam, Second steam in heat exchanger 12 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 13 provide steam discharge to generator 1, evaporator 6, the second evaporator 20 and the second generator 2, and steam discharge flows through generator 1, evaporator 6th, the second evaporator 20 with the second generator 2 and progressively heat release into discharging after condensate liquid;The concentrated solution of second generator 2 is through Two solution pumps 8 and solution heat exchanger 11 enter absorber 3, absorb refrigerant vapour and heat release is in heated medium, absorber 3 Weak solution enters the second absorber 4 through solution heat exchanger 11, absorbs refrigerant vapour and heat release is in cooling medium, the second absorber 4 weak solution enters generator 1, heat absorption release refrigerant vapour through solution pump 7 and is supplied to the 3rd generator 16 to make to drive heat to be situated between Matter, the concentrated solution of generator 1 is through the throttling of solution choke valve 10 into the second generator 2, heat absorption release refrigerant vapour and to second Absorber 4 is provided;The concentrated solution of 3rd generator 16 enters the 3rd through the 3rd solution pump 18 and the second solution heat exchanger 15 and inhaled Device 17 is received, refrigerant vapour is absorbed and heat release is in heated medium, the weak solution of the 3rd absorber 17 is through the second solution heat exchanger 15 enter the 3rd generators 16, and refrigerant vapour flows through the solution release that the 3rd generator 16, heating enter in it and to condenser 5 Refrigerant vapour is provided, the refrigerant vapour heat release of condenser 5 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 5 is through cryogen liquid The pressurization of pump 9 enters the second evaporator 20, absorbs heat into refrigerant vapour and provided to the 3rd absorber 17, flows through the 3rd generator 16 Refrigerant vapour heat release into entering evaporator 6 through the pressurization of the second cryogen liquid pump 21 after cryogen liquid, absorb heat into refrigerant vapour and to absorption Device 3 is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 15 moves what co-feeding system was realized in:
In the heat shown in Figure 14 moves co-feeding system, there is exhaust passage to be sequentially communicated generator 1, evaporator in engine 13 6th, the second generator 2 has condensate liquid pipeline and ft connection to be adjusted to power again afterwards for the second evaporator 20 and the second generator 2 Machine 13 has exhaust passage to be sequentially communicated the generator 2 of generator 1 and second, and the second generator 2 has condensate liquid pipeline and outside again afterwards Connection, has the second condensate liquid pipeline again by the rear heat exchange 12 that engine 13 has the second steam channel to be connected with heat exchanger 12 Being adjusted to engine 13 with ft connection has the second steam channel to be sequentially communicated second steaming afterwards of evaporator 20 of evaporator 6 and second Hair device 20 has the second condensate liquid pipeline and ft connection again, and engine 13 sets up the 3rd steam channel and connects it with heat exchanger 12 Rear heat exchange 12 has the 3rd condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
Heat shown in Figure 16 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat are handed over Parallel operation, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporator and the second cryogen liquid pump are constituted;Engine 13 Working machine 14 is connected, engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage to be sequentially communicated generator 1 There are condensate liquid pipeline and ft connection again with the second generator 2 after the second generator 2, engine 13 also has the second steam channel Second evaporator 20 has the second condensate liquid pipeline and a ft connection again after being connected with the second evaporator 20, and engine 13 also has the The finisher 6 that three steam channels are connected with evaporator 6 has the 3rd condensate liquid pipeline and a ft connection again, and engine 13 also has the The rear heat exchange 12 that four steam channels are connected with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again;Second occurs Device 2 also has concentrated solution pipeline to be connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution Pipeline is connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution pump 7 and hair Raw device 1 is connected, and generator 1 also has concentrated solution pipeline to be connected through solution choke valve 10 with the second generator 2, and the second generator 2 is also There is refrigerant steam channel to be connected with the second absorber 4, generator 1 also has after refrigerant steam channel connects with the 3rd generator 16 3rd generator 16 has cryogen liquid pipeline to be connected with the second cryogen liquid pump 21 again, the second cryogen liquid pump 21 also have cryogen liquid pipeline with Evaporator 6 is connected, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3;3rd generator 16 also has concentrated solution pipeline warp 3rd solution pump 18 and the second solution heat exchanger 15 are connected with the 3rd absorber 17, and the 3rd absorber 17 also has weak solution pipeline Connected through the second solution heat exchanger 15 with the 3rd generator 16, the 3rd generator 16 also has refrigerant steam channel and condenser 5 Connection, condenser 5 also has cryogen liquid pipeline to be connected through cryogen liquid pump 9 with the second evaporator 20, and the second evaporator 20 also has cryogen Steam channel is connected with the 3rd absorber 17, and the absorber 4 of condenser 5 and second also has cooling medium pipeline to connect with outside respectively Logical, the absorber 17 of absorber 3 and the 3rd also has heated medium pipeline and ft connection respectively, and heat exchanger 12, which also has, to be heated Medium pipeline and ft connection.
(2) in flow, compared with the dynamic co-feeding system of heat shown in Figure 15, difference is:The heat exchanger of engine 13 12 provide the 4th steam, and the heat release in heat exchanger 12 of the 4th steam, into being discharged through the 4th condensate liquid pipeline after condensate liquid, is moved Power machine 13 provides the 3rd steam to evaporator 6, the 3rd steam in evaporator 6 heat release into after condensate liquid through the 3rd condensate line Road is discharged, and engine 13 provides the second steam to the second evaporator 20.
Heat shown in Figure 17 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator and the second cryogen liquid pump Constituted;Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage Second generator 2 has condensate liquid pipeline and ft connection again after being connected with the second generator 2, and engine 13 also has the second steam Passage be sequentially communicated the second evaporator 20 after generator 1, the evaporator 20 of evaporator 6 and second have again the second condensate liquid pipeline with Ft connection, the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be connected with heat exchanger 12 has the 3rd condensate liquid again Pipeline and ft connection;Second generator 2 also has concentrated solution pipeline through the second solution pump 8 and solution heat exchanger 11 and absorber 3 connections, absorber 3 also has weak solution pipeline to be connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has Weak solution pipeline is connected through the solution heat exchanger 15 of solution pump 7 and second with generator 1, and generator 1 also has concentrated solution pipeline warp Second solution heat exchanger 15 is connected with the second generator 2, and the second generator 2 also has refrigerant steam channel and the second absorber 4 Connection, generator 1 also have refrigerant steam channel connected with the 3rd generator 16 after the 3rd generator 16 have cryogen liquid pipeline again Connected with the second cryogen liquid pump 21, the second cryogen liquid pump 21 also has cryogen liquid pipeline to be connected with evaporator 6, and evaporator 6 is also cold Agent steam channel is connected with absorber 3;3rd generator 16 also has concentrated solution pipeline through the 3rd solution pump 18 and the 3rd solution heat Exchanger 19 is connected with the 3rd absorber 17, and the 3rd absorber 17 also has weak solution pipeline through the 3rd solution heat exchanger 19 and the Three generators 16 are connected, and the 3rd generator 16 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipe Road is connected through cryogen liquid pump 9 with the second evaporator 20, and the second evaporator 20 also has refrigerant steam channel to connect with the 3rd absorber 17 Logical, the absorber 4 of condenser 5 and second also has cooling medium pipeline and ft connection respectively, and the absorber 17 of absorber 3 and the 3rd is also There are heated medium pipeline and ft connection respectively, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 3rd steam, 3rd steam in heat exchanger 12 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provide the second steam to generator 1, the evaporator 20 of evaporator 6 and second, and the second steam flows through generator 1, evaporator 6 and the Two evaporators 20 and progressively heat release through the second condensate liquid pipeline into being discharged after condensate liquid, and engine 13 is carried to the second generator 2 Supply and discharge vapour, steam discharge heat release in the second generator 2 is discharged into after condensate liquid;The concentrated solution of second generator 2 is through the second solution Pump 8 and solution heat exchanger 11 enter absorber 3, absorb refrigerant vapour and heat release is in heated medium, the weak solution of absorber 3 Enter the second absorber 4 through solution heat exchanger 11, absorb refrigerant vapour and heat release in cooling medium, the second absorber 4 it is dilute Solution enters generator 1, heat absorption release refrigerant vapour through the solution heat exchanger 15 of solution pump 7 and second and is supplied to the 3rd generation Device 16 makees driving thermal medium, and the concentrated solution of generator 1 enters the second generator 2, heat absorption through the second solution heat exchanger 15 and discharges cold Agent steam is simultaneously provided to the second absorber 4;The concentrated solution of 3rd generator 16 is through the 3rd solution pump 18 and the 3rd solution heat exchange Device 19 enters the 3rd absorber 17, absorbs refrigerant vapour and heat release in heated medium, and the weak solution of the 3rd absorber 17 is through the Three solution heat exchangers 19 enter the 3rd generator 16, the solution that refrigerant vapour flows through the 3rd generator 16, heating enters in it Discharge and to condenser 5 provide refrigerant vapour, the refrigerant vapour heat release of condenser 5 in cooling medium into cryogen liquid, condenser 5 Cryogen liquid enters the second evaporator 20 through the pressurization of cryogen liquid pump 9, absorbs heat into refrigerant vapour and provided to the 3rd absorber 17, flows through The refrigerant vapour heat release of 3rd generator 16 into after cryogen liquid through the pressurization of the second cryogen liquid pump 21 enter evaporator 6, absorb heat into it is cold Agent steam is simultaneously provided to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Figure 18 moves what co-feeding system was realized in:
In the heat shown in Figure 17 moves co-feeding system, there is the second steam channel to be sequentially communicated generator 1, steaming in engine 13 Second evaporator 20 has the second condensate liquid pipeline to be adjusted to engine 13 with ft connection again after the evaporator 20 of hair device 6 and second Have the second steam channel to be sequentially communicated generator 1 after generator 1 is connected has the second condensate liquid pipeline and ft connection again, will be dynamic The rear heat exchange 12 that power machine 13 has the 3rd steam channel to be connected with heat exchanger 12 has the 3rd condensate liquid pipeline to connect with outside again It is logical be adjusted to engine 13 have the 3rd steam channel be sequentially communicated the evaporator 20 of evaporator 6 and second after the second evaporator 20 again There are the 3rd condensate liquid pipeline and ft connection, engine 13 sets up heat exchange after the 4th steam channel is connected with heat exchanger 12 Device 12 has the 4th condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
Heat shown in Figure 19 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator and the second cryogen liquid pump Constituted;Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage Second generator 2 has condensate liquid pipeline and ft connection again after being connected with the second generator 2, and engine 13 also has the second steam Generator 1 has the second condensate liquid pipeline and ft connection again after passage is connected with generator 1, and engine 13 also has the 3rd steam Second evaporator 20 has the 3rd condensate liquid pipeline and ft connection again after passage is connected with the second evaporator 20, and engine 13 is also The finisher 6 for having the 4th steam channel and evaporator 6 has the 4th condensate liquid pipeline and a ft connection again, and engine 13 also has the The rear heat exchange 12 that five steam channels are connected with heat exchanger 12 has the 5th condensate liquid pipeline and ft connection again;Second occurs Device 2 also has concentrated solution pipeline to be connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, and absorber 3 also has dilute molten Liquid pipeline is connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through the He of solution pump 7 Second solution heat exchanger 15 is connected with generator 1, and generator 1 also has concentrated solution pipeline through the second solution heat exchanger 15 and the Two generators 2 are connected, and the second generator 2 also has refrigerant steam channel to be connected with the second absorber 4, and generator 1 also has cryogen to steam The 3rd generator 16 has cryogen liquid pipeline to be connected with the second cryogen liquid pump 21 again after vapour passage is connected with the 3rd generator 16, the Two cryogen liquid pumps 21 also have cryogen liquid pipeline to be connected with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3; 3rd generator 16 also has concentrated solution pipeline to connect through the 3rd solution pump 18 and the 3rd solution heat exchanger 19 with the 3rd absorber 17 Logical, the 3rd absorber 17 also has weak solution pipeline to be connected through the 3rd solution heat exchanger 19 with the 3rd generator 16, and the 3rd occurs Device 16 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be evaporated through cryogen liquid pump 9 and second Device 20 is connected, and the second evaporator 20 also has refrigerant steam channel to be connected with the 3rd absorber 17, the absorber 4 of condenser 5 and second Also have cooling medium pipeline and ft connection respectively, the absorber 17 of absorber 3 and the 3rd also have respectively heated medium pipeline with Ft connection, heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow, compared with the dynamic co-feeding system of heat shown in Figure 18, difference is:The heat exchanger of engine 13 12 provide the 5th steam, and the heat release in heat exchanger 12 of the 5th steam, into being discharged through the 5th condensate liquid pipeline after condensate liquid, is moved Power machine 13 provides the 4th steam to evaporator 6, the 4th steam in evaporator 6 heat release into after condensate liquid through the 4th condensate line Road is discharged, and engine 13 provides the 3rd steam to the second evaporator 20.
Heat shown in Figure 20 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Two solution heat exchangers, the 3rd generator, the 3rd absorber, the 3rd solution pump and the second cryogen liquid pump are constituted;Engine 13 Working machine 14 is connected, engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage to be sequentially communicated generator 1st, second generator 2 has condensate liquid pipeline and a ft connection again after the generator 2 of evaporator 6 and second, and engine 13 also has the The rear heat exchange 12 that two steam channels are connected with heat exchanger 12 has the second condensate liquid pipeline and ft connection again;Second occurs Device 2 also has concentrated solution pipeline to be connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution Pipeline is connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution pump 7 and hair Raw device 1 is connected, and generator 1 also has concentrated solution pipeline to be connected through solution choke valve 10 with the second generator 2, and the second generator 2 is also There is refrigerant steam channel to be connected with the second absorber 4, generator 1 also has after refrigerant steam channel connects with the 3rd generator 16 3rd generator 16 has cryogen liquid pipeline to be connected with the second cryogen liquid pump 21 again, the second cryogen liquid pump 21 also have cryogen liquid pipeline with Evaporator 6 is connected;3rd generator 16 also has concentrated solution pipeline through the 3rd solution pump 18 and the second solution heat exchanger 15 and the Three absorbers 17 are connected, and the 3rd absorber 17 also has weak solution pipeline to connect through the second solution heat exchanger 15 and the 3rd generator 16 Logical, the 3rd generator 16 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipeline through cryogen liquid pump 9 Connected with evaporator 6, evaporator 6 also has refrigerant steam channel to be connected respectively with the absorber 17 of absorber 3 and the 3rd, condenser 5 Also there are cooling medium pipeline and ft connection respectively with the second absorber 4, the absorber 17 of absorber 3 and the 3rd also has respectively to be added Heat medium pipeline and ft connection, heat exchanger 12 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the second steam, Second steam in heat exchanger 12 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 13 provide steam discharge to generator 1, the generator 2 of evaporator 6 and second, and steam discharge flows through generator 1, the generator 2 of evaporator 6 and second And progressively heat release is discharged into after condensate liquid;The concentrated solution of second generator 2 is through the second solution pump 8 and solution heat exchanger 11 Into absorber 3, absorbing refrigerant vapour, simultaneously heat release is in heated medium, and the weak solution of absorber 3 is entered through solution heat exchanger 11 Enter the second absorber 4, absorb refrigerant vapour and heat release is in cooling medium, the weak solution of the second absorber 4 enters through solution pump 7 to be sent out Raw device 1, heat absorption release refrigerant vapour are simultaneously supplied to the 3rd generator 16 to make driving thermal medium, and the concentrated solution of generator 1 is through solution section Stream valve 10 reducing pressure by regulating flow enters the second generator 2, heat absorption release refrigerant vapour and provided to the second absorber 4;3rd generator 16 concentrated solution enters the 3rd absorber 17 through the 3rd solution pump 18 and the second solution heat exchanger 15, absorbs refrigerant vapour and puts Heat enters the 3rd generator 16, cryogen in heated medium, the weak solution of the 3rd absorber 17 through the second solution heat exchanger 15 The solution that steam flows through the 3rd generator 16, heating enters in it discharges and provides refrigerant vapour to condenser 5, condenser 5 Refrigerant vapour heat release is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 5 enters evaporator 6 through the pressurization of cryogen liquid pump 9, flowed through The refrigerant vapour heat release of 3rd generator 16 into entering evaporator 6 through the pressurization of the second cryogen liquid pump 21 after cryogen liquid, evaporator 6 Cryogen liquid absorbs heat into refrigerant vapour and provided respectively to the absorber 17 of absorber 3 and the 3rd, forms the dynamic co-feeding system of heat.
Heat shown in Figure 21 moves what co-feeding system was realized in:
In the heat shown in Figure 20 moves co-feeding system, there is exhaust passage to be sequentially communicated generator 1, evaporator in engine 13 6 and second second generator 2 after generator 2 there is condensate liquid pipeline to be adjusted to engine 13 with ft connection again to have exhaust passage Second generator 2 has condensate liquid pipeline and ft connection again after being sequentially communicated the generator 2 of generator 1 and second, by engine 13 rear heat exchanges 12 for having the second steam channel to be connected with heat exchanger 12 have the second condensate liquid pipeline to be adjusted with ft connection again It is whole to there is the second condensate liquid pipeline to connect with outside again for the finisher 6 that engine 13 has the second steam channel to be connected with evaporator 6 It is logical, engine 13 set up the rear heat exchange 12 that the 3rd steam channel connects with heat exchanger 12 have again the 3rd condensate liquid pipeline and Ft connection, forms the dynamic co-feeding system of heat.
Heat shown in Figure 22 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump are constituted;Power Machine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage and second to occur The second generator 2 has condensate liquid pipeline and ft connection again after device 2 is connected, and engine 13 also has the second steam channel to connect successively The finisher 6 of logical generator 1 and evaporator 6 has the second condensate liquid pipeline and ft connection again, and engine 13 also has the 3rd to steam The rear heat exchange 12 that vapour passage is connected with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again;Second generator 2 Also concentrated solution pipeline is connected through the second solution pump 8 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipe Road is connected through solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution pump 7 and second Solution heat exchanger 15 is connected with generator 1, and generator 1 also has concentrated solution pipeline through the second solution heat exchanger 15 and the second hair Raw device 2 is connected, and the second generator 2 also has refrigerant steam channel to be connected with the second absorber 4, and generator 1 also has refrigerant vapour to lead to The 3rd generator 16 has cryogen liquid pipeline to be connected with the second cryogen liquid pump 21 again after road is connected with the 3rd generator 16, and second is cold Agent liquid pump 21 also has cryogen liquid pipeline to be connected with evaporator 6;3rd generator 16 also has concentrated solution pipeline through the 3rd solution pump 18 Connected with the 3rd solution heat exchanger 19 with the 3rd absorber 17, the 3rd absorber 17 also has weak solution pipeline through the 3rd solution heat Exchanger 19 is connected with the 3rd generator 16, and the 3rd generator 16 also has refrigerant steam channel to be connected with condenser 5, condenser 5 Also cryogen liquid pipeline is connected through cryogen liquid pump 9 with evaporator 6, evaporator 6 also have refrigerant steam channel respectively with absorber 3 and 3rd absorber 17 is connected;The absorber 4 of condenser 5 and second also has cooling medium pipeline and ft connection, the He of absorber 3 respectively 3rd absorber 17 also has heated medium pipeline and ft connection respectively, and heat exchanger 12 also has heated medium pipeline and outer Portion is connected.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 3rd steam, 3rd steam in heat exchanger 12 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provide the second steam to generator 1 and evaporator 6, the second steam flow through generator 1 and evaporator 6, heat release into condensate liquid it Discharged by the second condensate liquid pipeline, engine 13 provides steam discharge, steam discharge heat release in the second generator 2 to the second generator 2 Discharged after into condensate liquid;The concentrated solution of second generator 2 through the second solution pump 8 and solution heat exchanger 11 enter absorber 3, Absorb refrigerant vapour and heat release is in heated medium, the weak solution of absorber 3 enters the second absorber through solution heat exchanger 11 4th, absorb refrigerant vapour and heat release is in cooling medium, the weak solution of the second absorber 4 is through the solution heat exchanger of solution pump 7 and second 15 enter generator 1, heat absorption release refrigerant vapour and are supplied to the 3rd generator 16 to make driving thermal medium, the concentrated solution of generator 1 Enter the second generator 2, heat absorption release refrigerant vapour through the second solution heat exchanger 15 and provided to the second absorber 4;3rd The concentrated solution of generator 16 enters the 3rd absorber 17 through the 3rd solution pump 18 and the 3rd solution heat exchanger 19, absorbs cryogen steaming Simultaneously heat release is in heated medium for vapour, and the weak solution of the 3rd absorber 17 enters the 3rd generator through the 3rd solution heat exchanger 19 16, the solution that refrigerant vapour flows through the 3rd generator 16, heating enters in it discharges and provides refrigerant vapour to condenser 5, cold The refrigerant vapour heat release of condenser 5 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 5 enters evaporation through the pressurization of cryogen liquid pump 9 Device 6, flows through the refrigerant vapour heat release of the 3rd generator 16 into entering evaporator 6 through the pressurization of the second cryogen liquid pump 21 after cryogen liquid, The cryogen liquid of evaporator 6 absorbs heat into refrigerant vapour and provided respectively to the absorber 17 of absorber 3 and the 3rd, forms the dynamic alliance system of heat System.
Heat shown in Figure 23 moves what co-feeding system was realized in:
In the heat shown in Figure 22 moves co-feeding system, there is the second steam channel to be sequentially communicated the He of generator 1 in engine 13 The finisher 6 of evaporator 6 has the second condensate liquid pipeline to be adjusted to engine 13 with ft connection again second channel and generation Generator 1 has the second condensate liquid pipeline and ft connection again after device 1 is connected, and has the 3rd steam channel to be handed over heat in engine 13 The rear heat exchange 12 of the connection of parallel operation 12 has the 3rd condensate liquid pipeline to be adjusted to engine 13 with ft connection again the 3rd steam The finisher 6 that passage is connected with evaporator 6 has the 3rd condensate liquid pipeline and ft connection again, and engine 13 sets up the 4th steam The rear heat exchange 12 that passage is connected with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again, forms the dynamic alliance system of heat System.
Heat shown in Figure 24 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator and the second cryogen liquid pump Constituted;Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage Second generator 2 has condensate liquid pipeline and ft connection again after being connected with the second generator 2, and engine 13 also has the second steam Passage be sequentially communicated the second evaporator 20 after generator 1, the evaporator 20 of evaporator 6 and second have again the second condensate liquid pipeline with Ft connection, the rear heat exchange 12 that engine 13 also has the 3rd steam channel to be connected with heat exchanger 12 has the 3rd condensate liquid again Pipeline and ft connection;Generator 1 also has concentrated solution pipeline to be connected through solution pump 7 and solution heat exchanger 11 with absorber 3, inhales Receiving device 3 also has weak solution pipeline to be connected through solution heat exchanger 11 with generator 1, and generator 1 also has refrigerant steam channel and the The 3rd generator 16 has cryogen liquid pipeline to be connected through the second cryogen liquid pump 21 with evaporator 6 again after the connection of three generators 16, steams Hair device 6 also has refrigerant steam channel to be connected with absorber 3;Second generator 2 also has concentrated solution pipeline through the second solution pump 8 and the Two solution heat exchangers 15 are connected with the 3rd absorber 17, and the 3rd absorber 17 also has weak solution pipeline through the second solution heat exchange Device 15 is connected with the second absorber 4, and the second absorber 4 also has weak solution pipeline through the 3rd solution pump 18 and the 3rd solution heat exchange Device 19 is connected with the 3rd generator 16, and the 3rd generator 16 also has concentrated solution pipeline through the 3rd solution heat exchanger 19 and second Generator 2 is connected, and the second generator 2 also has refrigerant steam channel to be connected with the second absorber 4, and the 3rd generator 16 also has cryogen Steam channel is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected through cryogen liquid pump 9 with the second evaporator 20, and second Evaporator 20 also has refrigerant steam channel to be connected with the 3rd absorber 17;The absorber 4 of condenser 5 and second also has cooling to be situated between respectively Matter pipeline and ft connection, the absorber 17 of absorber 3 and the 3rd also have heated medium pipeline and ft connection, heat exchange respectively Device 12 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 3rd steam, 3rd steam in heat exchanger 12 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provide the second steam to generator 1, the evaporator 20 of evaporator 6 and second, and the second steam flows through generator 1, evaporator 6 and the Two evaporators 20 and progressively heat release through the second condensate liquid pipeline into being discharged after condensate liquid, and engine 13 is carried to the second generator 2 Supply and discharge vapour, steam discharge heat release in the second generator 2 is discharged into after condensate liquid;The concentrated solution of generator 1 is through solution pump 7 and solution Heat exchanger 11 enters absorber 3, absorbs refrigerant vapour and heat release is in heated medium, and the weak solution of absorber 3 is through solution heat Exchanger 11 enters generator 1, heat absorption release refrigerant vapour and is supplied to the 3rd generator 16 to make driving thermal medium;Second occurs The concentrated solution of device 2 enters the 3rd absorber 17 through the second solution pump 8 and the second solution heat exchanger 15, absorbs refrigerant vapour and puts Heat enters the second absorber 4 through the second solution heat exchanger 15, absorbs cold in heated medium, the weak solution of the 3rd absorber 17 Simultaneously heat release is in cooling medium for agent steam, and the weak solution of the second absorber 4 is through the 3rd solution pump 18 and the 3rd solution heat exchanger 19 Into the 3rd generator 16, refrigerant vapour flow through the 3rd generator 16, heating enter its in solution release refrigerant vapour and to Condenser 5 is provided, and the concentrated solution of the 3rd generator 16 enters the second generator 2, heat absorption through the 3rd solution heat exchanger 19 and discharged Refrigerant vapour is simultaneously provided to the second absorber 4, and the cryogen liquid of condenser 5 enters the second evaporator 20 through the pressurization of cryogen liquid pump 9, inhaled Heat is provided into refrigerant vapour and to the 3rd absorber 17, flow through the refrigerant vapour heat release of the 3rd generator 16 into after cryogen liquid through the The pressurization of two cryogen liquid pumps 21 enters evaporator 6, absorbs heat into refrigerant vapour and provided to absorber 3, forms the dynamic co-feeding system of heat.
Heat shown in Figure 25 moves what co-feeding system was realized in:
In the heat shown in Figure 24 moves co-feeding system, there is the second steam channel to be sequentially communicated generator 1, steaming in engine 13 Second evaporator 20 has the second condensate liquid pipeline to be adjusted to engine 13 with ft connection again after the evaporator 20 of hair device 6 and second Having the second steam channel to be sequentially communicated the evaporator 20 of generator 1 and second, the second evaporator 20 has the second condensate liquid pipeline again afterwards With ft connection, the rear heat exchange 12 that engine 13 has the 3rd steam channel to be connected with heat exchanger 12 there is into the 3rd condensation again The finisher 6 that liquid pipeline is adjusted to engine 13 with ft connection and has the 3rd steam channel to be connected with evaporator 6 has the 3rd again Condensate liquid pipeline and ft connection, engine 13 set up rear heat exchange 12 that the 4th steam channel connects with heat exchanger 12 again There are the 4th condensate liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
Heat shown in Figure 26 moves what co-feeding system was realized in:
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump are constituted;Power Machine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage and second to occur The second generator 2 has condensate liquid pipeline and ft connection again after device 2 is connected, and engine 13 also has the second steam channel to connect successively The finisher 6 of logical generator 1 and evaporator 6 has the second condensate liquid pipeline and ft connection again, and engine 13 also has the 3rd to steam The rear heat exchange 12 that vapour passage is connected with heat exchanger 12 has the 3rd condensate liquid pipeline and ft connection again;Generator 1 also has Concentrated solution pipeline is connected through solution pump 7 and solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipeline through solution Heat exchanger 11 is connected with generator 1, and the 3rd occurs after the also refrigerant steam channel of generator 1 is connected with the 3rd generator 16 Device 16 has cryogen liquid pipeline to be connected with the second cryogen liquid pump 21 again, and the second cryogen liquid pump 21 also has cryogen liquid pipeline and evaporator 6 Connection;Second generator 2 also has concentrated solution pipeline through the second solution pump 8 and the second solution heat exchanger 15 and the 3rd absorber 17 Connection, the 3rd absorber 17 also has weak solution pipeline to be connected through the second solution heat exchanger 15 with the second absorber 4, and second absorbs Device 4 also has weak solution pipeline to be connected through the 3rd solution pump 18 and the 3rd solution heat exchanger 19 with the 3rd generator 16, the 3rd hair Raw device 16 also has concentrated solution pipeline to be connected through the 3rd solution heat exchanger 19 with the second generator 2, and the second generator 2 also has cryogen Steam channel is connected with the second absorber 4, and the 3rd generator 16 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 is also There is cryogen liquid pipeline to be connected through cryogen liquid pump 9 with evaporator 6, evaporator 6 also have refrigerant steam channel respectively with absorber 3 and the Three absorbers 17 are connected;The absorber 4 of condenser 5 and second also has cooling medium pipeline and ft connection, absorber 3 and respectively Three absorbers 17 also have heated medium pipeline and ft connection respectively, and heat exchanger 12 also has heated medium pipeline and outside Connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 3rd steam, 3rd steam in heat exchanger 12 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provide the second steam to generator 1 and evaporator 6, and the second steam flows through generator 1 with evaporator 6, progressively heat release is into condensation Discharged after liquid through the second condensate liquid pipeline, engine 13 provides steam discharge to the second generator 2, and steam discharge is in the second generator 2 Heat release is discharged into after condensate liquid;The concentrated solution of generator 1 enters absorber 3 through solution pump 7 and solution heat exchanger 11, absorbed Simultaneously heat release is in heated medium for refrigerant vapour, and the weak solution of absorber 3 enters generator 1, heat absorption through solution heat exchanger 11 and released Put refrigerant vapour and be supplied to the 3rd generator 16 to make driving thermal medium;The concentrated solution of second generator 2 is through the He of the second solution pump 8 Second solution heat exchanger 15 enters the 3rd absorber 17, absorbs refrigerant vapour and heat release is in heated medium, the 3rd absorber 17 weak solution enters the second absorber 4 through the second solution heat exchanger 15, absorbs refrigerant vapour and heat release in cooling medium, the The weak solution of two absorbers 4 enters the 3rd generator 16, refrigerant vapour through the 3rd solution pump 18 and the 3rd solution heat exchanger 19 Flow through the 3rd generator 16, the solution that heating enters in it discharges refrigerant vapour and provided to condenser 5, the 3rd generator 16 Concentrated solution enters the second generator 2, heat absorption release refrigerant vapour through the 3rd solution heat exchanger 19 and carried to the second absorber 4 Through the pressurization of cryogen liquid pump 9 enter evaporator 6 for the cryogen liquid of, condenser 5, flow through the refrigerant vapour heat release of the 3rd generator 16 into Enter evaporator 6 through the pressurization of the second cryogen liquid pump 21 after cryogen liquid, the cryogen liquid of evaporator 6 absorb heat into refrigerant vapour and respectively to The absorber 17 of absorber 3 and the 3rd is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 27 moves what co-feeding system was realized in:
In the heat shown in Figure 26 moves co-feeding system, there is the second steam channel to be sequentially communicated the He of generator 1 in engine 13 The finisher 6 of evaporator 6 have again the second condensate liquid pipeline and ft connection be adjusted to engine 13 have the second steam channel with Generator 1 connect after generator 1 have the second condensate liquid pipeline and ft connection again, by engine 13 have the 3rd steam channel with The rear heat exchange 12 of the connection of heat exchanger 12 has the 3rd condensate liquid pipeline to be adjusted to engine 13 with ft connection again the 3rd The finisher 6 that steam channel is connected with evaporator 6 has the 3rd condensate liquid pipeline and ft connection again, and engine 13 sets up the 4th The rear heat exchange 12 that steam channel is connected with heat exchanger 12 has the 4th condensate liquid pipeline and ft connection again, forms the dynamic connection of heat For system.
Heat shown in Figure 28 moves what co-feeding system was realized in:
(1) it is the newly-increased absorber of increase, newly-increased second absorber, new in the heat shown in Fig. 3 moves co-feeding system in structure Solubilized liquid pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, have weak solution pipeline through solution heat exchanger 11 by absorber 3 Connected with the second absorber 4 and be adjusted to absorber 3 and there is weak solution pipeline to be connected with newly-increased absorber A, increase absorber A newly also dilute Solution line is connected through newly-increased solution pump C and newly-increased solution heat exchanger E with newly-increased second absorber B, increases the second absorber newly B has weak solution pipeline to be connected through newly-increased solution heat exchanger E and solution heat exchanger 11 with the second absorber 4 again, and evaporator 6 increases If refrigerant steam channel is connected with newly-increased absorber A, condenser 5 sets up cryogen liquid pipeline through newly-increased cryogen liquid pump D and newly-increased suction Newly-increased absorber A has refrigerant steam channel to be connected with newly-increased second absorber B again after receiving device A connections, increases the second absorber B newly Also heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and the heat exchanger 12 of engine 13 provides the 3rd steam, 3rd steam in heat exchanger 12 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provide the second steam to generator 1 and evaporator 6, and the second steam flows through generator 1 with evaporator 6, progressively heat release is into condensation Discharged after liquid through the second condensate liquid pipeline, engine 13 provides steam discharge to the second generator 2, and steam discharge is in the second generator 2 Heat release is discharged into after condensate liquid;The concentrated solution of second generator 2 enters through the second solution pump 8 and solution heat exchanger 11 to be absorbed Device 3, absorption refrigerant vapour and heat release enter newly-increased absorber A, absorb cryogen steaming in heated medium, the weak solution of absorber 3 Simultaneously heat release is in cryogen liquid for vapour, and newly-increased absorber A weak solution enters through newly-increased solution pump C and newly-increased solution heat exchanger E to be increased newly Second absorber B, absorption refrigerant vapour and heat release increase the second absorber B weak solution newly through new solubilization liquid in heated medium Heat exchanger E and solution heat exchanger 11 enter the second absorber 4, absorb refrigerant vapour and heat release is inhaled in cooling medium, second Receive the weak solution of device 4 and enter generator 1, heat absorption release refrigerant vapour and to cold through the solution heat exchanger 15 of solution pump 7 and second Condenser 5 is provided, and the concentrated solution of generator 1 enters the second generator 2, heat absorption release refrigerant vapour simultaneously through the second solution heat exchanger 15 There is provided to the second absorber 4;The refrigerant vapour heat release of condenser 5 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 5 is divided into Two-way --- the first via enters evaporator 6 through the pressurization of cryogen liquid pump 9, absorbs heat into refrigerant vapour and respectively to absorber 3 and newly-increased Absorber A is provided, and the second tunnel flows through newly-increased absorber A after newly-increased cryogen liquid pump D pressurizations, absorbs heat into refrigerant vapour and to new Second absorber B offers are provided, the dynamic co-feeding system of heat is formed.
The effect that the technology of the present invention can be realized --- heat proposed by the invention move co-feeding system have the effect that and Advantage:
(1) temperature difference between engine outlet steam discharge and cold environment is utilized, and realizes the conjunction of total system heat energy utilization Physics and chemistry.
(2) the first work done (generating) of high-grade steam, is used for heat supply after grade reduction, meets thermal energy step and utilize principle.
(3) backheat cooling process is used, the temperature difference between steam discharge and cold environment can be further made full use of, low product are improved The value of position heat energy and technology flexibility.
(4) a variety of concrete technical schemes are provided, numerous different actual states is coped with, there is the wider scope of application.
(5) during variable working condition, second-kind absorption-type heat pump heat supply flow can be preferentially used, heat exchanger thermic load has regulation Space, it ensure that system is efficient and flexible.
(6) steam discharge and engine intermediate extraction are combined the thermal source for absorption heat pump flow, to meet different user Considerable flexibility is brought with duty requirements.
(7) there is the double dominant of extraction for heat supply and condensing heat supply, heating demand change is largely avoided to work done The influence of (generating).
(8) type of the dynamic co-feeding system of heat is enriched, the application of second-kind absorption-type heat pump is extended, is conducive to more Making full use of for the temperature difference is realized using second-kind absorption-type heat pump well.

Claims (58)

1. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, molten Liquid pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine and working machine institute group Into;Engine (13) connection working machine (14), engine (13) has live steam passage and ft connection, also engine (13) or row Vapour passage and ft connection, engine (13) also have exhaust passage to be sequentially communicated generator (1), evaporator (6) and second and occurred The second generator (2) has condensate liquid pipeline and ft connection again after device (2), and engine (13) also has the second steam channel and heat The rear heat exchange (12) of exchanger (12) connection has the second condensate liquid pipeline and ft connection again;Second generator (2) also has Concentrated solution pipeline is connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), and absorber (3) also has dilute molten Liquid pipeline is connected through solution heat exchanger (11) with the second absorber (4), and the second absorber (4) also has weak solution pipeline through solution Pump (7) is connected with generator (1), and generator (1) also has concentrated solution pipeline to connect through solution choke valve (10) and the second generator (2) Logical, the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), and generator (1) also has refrigerant steam channel Connected with condenser (5), condenser (5) also has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6), evaporator (6) Also refrigerant steam channel is connected with absorber (3), and condenser (5) and the second absorber (4) also have cooling medium pipeline respectively With ft connection, absorber (3) also has heated medium pipeline and ft connection, and heat exchanger (12) also has heated medium pipe Road and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, is in the heat described in claim 1 moves co-feeding system, to cancel evaporator, by engine (13) Having exhaust passage to be sequentially communicated generator (1), evaporator (6) and the second generator (2), the second generator (2) has condensation again afterwards Liquid pipeline and ft connection, which are adjusted to engine (13), to be had after exhaust passage connects with generator (1) and the second generator (2) Second generator (2) has condensate liquid pipeline and ft connection again, has refrigerant steam channel to connect with absorber (3) evaporator (6) It is logical to be adjusted to engine (13) and set up exhaust passage to connect with absorber (3), condenser (5) there is into cryogen liquid pipeline through cryogen liquid Pump (9) is connected with evaporator (6) to be adjusted to condenser (5) and has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, forms heat Dynamic co-feeding system.
3. the dynamic co-feeding system of heat, be in the heat described in claim 1 moves co-feeding system, by engine (13) have exhaust passage according to The second generator (2) has condensate liquid pipeline and outside again after secondary connection generator (1), evaporator (6) and the second generator (2) Connection be adjusted to engine (13) have exhaust passage connected with generator (1) and the second generator (2) after the second generator (2) There are condensate liquid pipeline and ft connection again, there is the second steam channel is warm after being connected with heat exchanger (12) to hand in engine (13) Parallel operation (12) has the second condensate liquid pipeline to be adjusted to engine (13) with ft connection again the second steam channel and evaporator (6) The finisher (6) of connection has the second condensate liquid pipeline and ft connection again, and engine (13) sets up the 3rd steam channel and heat The rear heat exchange (12) of exchanger (12) connection has the 3rd condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, is in the heat described in claim 3 moves co-feeding system, to cancel evaporator, by engine (13) The finisher (6) for having the second steam channel to be connected with evaporator (6) has the second condensate liquid pipeline and ft connection, evaporator again (6) there is refrigerant steam channel to connect with absorber (3) to be adjusted to engine (13) in the lump and have the second steam channel and absorber (3) Connection, has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) and has cryogen Liquid pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump (9) and ft connection.
5. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, molten Liquid pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine and the second solution heat exchange Device is constituted;Engine (13) connection working machine (14), engine (13) has live steam passage and a ft connection, engine (13) or Also exhaust passage and ft connection, engine (13) also have the second generator (2) after exhaust passage and the second generator (2) There are condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be sequentially communicated generator (1) and evaporator (6) finisher (6) has the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel to be handed over heat The rear heat exchange (12) of parallel operation (12) connection has the 3rd condensate liquid pipeline and ft connection again;Second generator (2) is also dense Solution line is connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), and absorber (3) also has weak solution Pipeline is connected through solution heat exchanger (11) with the second absorber (4), and the second absorber (4) also has weak solution pipeline through solution pump (7) connected with the second solution heat exchanger (15) with generator (1), generator (1) also has concentrated solution pipeline through the second solution heat Exchanger (15) is connected with the second generator (2), and the second generator (2) also has refrigerant steam channel to connect with the second absorber (4) Logical, generator (1) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) also has cryogen liquid pipeline through cryogen liquid pump (9) connected with evaporator (6), evaporator (6) also has refrigerant steam channel to be connected with absorber (3), condenser (5) and second is inhaled Receive device (4) also has cooling medium pipeline and ft connection respectively, and absorber (3) also has heated medium pipeline and ft connection, Heat exchanger (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, is in the heat described in claim 5 moves co-feeding system, to cancel evaporator, by engine (13) Have the second steam channel to be sequentially communicated generator (1) and the finisher (6) of evaporator (6) has the second condensate liquid pipeline and outer again Portion connection be adjusted to engine (13) have the second steam channel connected with generator (1) after generator (1) have the second condensation again Liquid pipeline and ft connection, have refrigerant steam channel to be connected with absorber (3) evaporator (6) and are adjusted to engine (13) and set up Second steam channel is connected with absorber (3), has cryogen liquid pipeline to connect through cryogen liquid pump (9) and evaporator (6) condenser (5) The logical condenser (5) that is adjusted to has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is that engine (13) has the second steam channel in the heat described in claim 5 moves co-feeding system Be sequentially communicated the finisher (6) of generator (1) and evaporator (6) has the second condensate liquid pipeline to be adjusted to dynamic with ft connection again Power machine (13) have the second steam channel connected with generator (1) after generator (1) there is the second condensate liquid pipeline to connect with outside again It is logical, the rear heat exchange (12) that engine (13) has the 3rd steam channel to be connected with heat exchanger (12) there is into the 3rd condensate liquid again The finisher (6) that pipeline is adjusted to engine (13) with ft connection and has the 3rd steam channel to be connected with evaporator (6) has again 3rd condensate liquid pipeline and ft connection, engine (13) set up heat friendship after the 4th steam channel is connected with heat exchanger (12) Parallel operation (12) has the 4th condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is in the heat described in claim 7 moves co-feeding system, to cancel evaporator, by engine (13) The finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, evaporator again (6) there is refrigerant steam channel to connect with absorber (3) to be adjusted to engine (13) in the lump and have the 3rd steam channel and absorber (3) Connection, has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) and has cryogen Liquid pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump (9) and ft connection.
9. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, molten Liquid pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, second Solution heat exchanger, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, also engine (13) or exhaust passage and ft connection, engine (13) exhaust passage is sequentially communicated after the 3rd generator (16), generator (1), evaporator (6) and the second generator (2) Second generator (2) has condensate liquid pipeline and ft connection again, and engine (13) also has the second steam channel and heat exchanger (12) rear heat exchange (12) of connection has the second condensate liquid pipeline and ft connection again;Second generator (2) also has concentrated solution Pipeline is connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), and absorber (3) also has weak solution pipeline Connected through solution heat exchanger (11) with the second absorber (4), the second absorber (4) also has weak solution pipeline through solution pump (7) Connected with generator (1), generator (1) also has concentrated solution pipeline to be connected through solution choke valve (10) with the second generator (2), the Two generators (2) also have refrigerant steam channel to be connected with the second absorber (4), and generator (1) also has refrigerant steam channel and the Three absorbers (17) are connected, and the 3rd absorber (17) also has weak solution pipeline through the 3rd solution pump (18) and the second solution heat exchange Device (15) is connected with the 3rd generator (16), and the 3rd generator (16) also has concentrated solution pipeline through the second solution heat exchanger (15) Connected with the 3rd absorber (17), the 3rd generator (16) also has refrigerant steam channel to be connected with condenser (5), condenser (5) Also cryogen liquid pipeline is connected through cryogen liquid pump (9) with evaporator (6), and evaporator (6) also has refrigerant steam channel and absorber (3) connect, condenser (5), the second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and outside to connect respectively Logical, absorber (3) also has heated medium pipeline and ft connection, and heat exchanger (12) also has heated medium pipeline and outside Connection, forms the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is in the heat described in claim 9 moves co-feeding system, to cancel evaporator, by engine (13) There is exhaust passage to be sequentially communicated the second hair after the 3rd generator (16), generator (1), evaporator (6) and the second generator (2) Raw device (2) has condensate liquid pipeline to be adjusted to engine (13) with ft connection again has exhaust passage to be sequentially communicated the 3rd generator (16), the second generator (2) has condensate liquid pipeline and ft connection again afterwards for generator (1) and the second generator (2), will evaporate Device (6) has refrigerant steam channel to connect with absorber (3) to be adjusted to engine (13) and set up exhaust passage and absorber (3) even It is logical, there is cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and be adjusted to condenser (5) and have cryogen liquid Pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump (9) and ft connection.
11. the dynamic co-feeding system of heat, is that in the heat described in claim 9 moves co-feeding system, engine (13) is had into exhaust passage It is sequentially communicated after the 3rd generator (16), generator (1), evaporator (6) and the second generator (2) the second generator (2) again Having condensate liquid pipeline to be adjusted to engine (13) with ft connection has exhaust passage to be sequentially communicated the 3rd generator (16), generator (1) and after the second generator (2) the second generator (2) has condensate liquid pipeline and ft connection again, and engine (13) is had into the The rear heat exchange (12) that two steam channels are connected with heat exchanger (12) has the second condensate liquid pipeline to be adjusted with ft connection again The finisher (6) for having the second steam channel to be connected with evaporator (6) for engine (13) has the second condensate liquid pipeline and outer again Portion is connected, and engine (13) sets up the rear heat exchange (12) that the 3rd steam channel connects with heat exchanger (12) the 3rd cold again Lime set pipeline and ft connection, form the dynamic co-feeding system of heat.
12. the dynamic co-feeding system of heat, is in the heat described in claim 11 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the second steam channel to be connected with evaporator (6) has the second condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the second steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) There is cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
13. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Engine (13) connects work Make machine (14), engine (13) has live steam passage and ft connection, and engine (13) or also exhaust passage and ft connection are moved Power machine (13) also have exhaust passage be sequentially communicated the 3rd generator (16) and the second generator (2) after the second generator (2) again There are condensate liquid pipeline and ft connection, engine (13) also has the second steam channel to be sequentially communicated generator (1) and evaporator (6) Finisher (6) have the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel and heat exchange The rear heat exchange (12) of device (12) connection has the 3rd condensate liquid pipeline and ft connection again;Second generator (2) also has dense molten Liquid pipeline is connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), and absorber (3) also has weak solution pipe Road is connected through solution heat exchanger (11) with the second absorber (4), and the second absorber (4) also has weak solution pipeline through solution pump (7) connected with the second solution heat exchanger (15) with generator (1), generator (1) also has concentrated solution pipeline through the second solution heat Exchanger (15) is connected with the second generator (2), and the second generator (2) also has refrigerant steam channel to connect with the second absorber (4) Logical, generator (1) also has refrigerant steam channel to be connected with the 3rd absorber (17), and the 3rd absorber (17) also has weak solution pipeline Connected through the 3rd solution pump (18) and the 3rd solution heat exchanger (19) with the 3rd generator (16), the 3rd generator (16) also has Concentrated solution pipeline is connected through the 3rd solution heat exchanger (19) with the 3rd absorber (17), and the 3rd generator (16) also has cryogen steaming Vapour passage is connected with condenser (5), and condenser (5) also has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6), is steamed Hair device (6) also has refrigerant steam channel to be connected with absorber (3), condenser (5), the second absorber (4) and the 3rd absorber (17) also there are cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, and heat is handed over Parallel operation (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
14. the dynamic co-feeding system of heat, is in the heat described in claim 13 moves co-feeding system, to cancel evaporator, by engine (13) there is the second steam channel to be sequentially communicated generator (1) and have the second condensate line again with the finisher (6) of evaporator (6) Road and ft connection be adjusted to engine (13) have the second steam channel connected with generator (1) after generator (1) have again Two condensate liquid pipelines and ft connection, have refrigerant steam channel to be connected with absorber (3) evaporator (6) and are adjusted to engine (13) set up the second steam channel to connect with absorber (3), have cryogen liquid pipeline through cryogen liquid pump (9) with steaming condenser (5) Hair device (6) connection, which is adjusted to condenser (5), has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, forms the dynamic alliance system of heat System.
15. the dynamic co-feeding system of heat, is that in the heat described in claim 13 moves co-feeding system, engine (13) is had into the second steam Passage is sequentially communicated generator (1) and has the second condensate liquid pipeline to be adjusted with ft connection again with the finisher (6) of evaporator (6) It is whole for engine (13) have the second steam channel connected with generator (1) after generator (1) have again the second condensate liquid pipeline and Ft connection, has the 3rd again by the rear heat exchange (12) that engine (13) has the 3rd steam channel to be connected with heat exchanger (12) Condensate liquid pipeline is adjusted to the finisher that engine (13) has the 3rd steam channel to be connected with evaporator (6) with ft connection (6) there are the 3rd condensate liquid pipeline and ft connection again, engine (13) is set up the 4th steam channel and connected with heat exchanger (12) Rear heat exchange (12) have the 4th condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
16. the dynamic co-feeding system of heat, is in the heat described in claim 15 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the 3rd steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) There is cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
17. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Two solution heat exchangers, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, also engine (13) or exhaust passage and ft connection, engine (13) exhaust passage is sequentially communicated after the second generator (2), generator (1), evaporator (6) and the 3rd generator (16) 3rd generator (16) has condensate liquid pipeline and ft connection again, and engine (13) also has the second steam channel and heat exchanger (12) rear heat exchange (12) of connection has the second condensate liquid pipeline and ft connection again;Generator (1) also has concentrated solution pipeline Connected through solution pump (7) and solution heat exchanger (11) with absorber (3), absorber (3) also has weak solution pipeline through solution heat Exchanger (11) is connected with generator (1), and generator (1) also has refrigerant steam channel to be connected with the second absorber (4), and second inhales Receiving device (4) also has weak solution pipeline to connect through the second solution pump (8) and the second solution heat exchanger (15) with the 3rd absorber (17) Logical, the 3rd absorber (17) also has weak solution pipeline to be connected through the 3rd solution pump (18) with the second generator (2), the second generator (2) concentrated solution pipeline is connected through solution choke valve (10) with the 3rd generator (16), the 3rd generator (16) also has dense molten Liquid pipeline is connected through the second solution heat exchanger (15) with the second absorber (4), and the 3rd generator (16) also has refrigerant vapour to lead to Road is connected with the 3rd absorber (17), and the second generator (2) also has refrigerant steam channel to be connected with condenser (5), condenser (5) Also cryogen liquid pipeline is connected through cryogen liquid pump (9) with evaporator (6), and evaporator (6) also has refrigerant steam channel and absorber (3) connect, condenser (5), the second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and outside to connect respectively Logical, absorber (3) also has heated medium pipeline and ft connection, and heat exchanger (12) also has heated medium pipeline and outside Connection, forms the dynamic co-feeding system of heat.
18. the dynamic co-feeding system of heat, is in the heat described in claim 17 moves co-feeding system, to cancel evaporator, by engine (13) exhaust passage is sequentially communicated after the second generator (2), generator (1), evaporator (6) and the 3rd generator (16) the Three generators (16) have condensate liquid pipeline to be adjusted to engine (13) with ft connection again has exhaust passage to be sequentially communicated the second hair The 3rd generator (16) has condensate liquid pipeline and ft connection again after raw device (2), generator (1) and the 3rd generator (16), There is refrigerant steam channel to connect with absorber (3) evaporator (6) to be adjusted to engine (13) and set up exhaust passage and absorber (3) connect, there is cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and be adjusted to condenser (5) and have Cryogen liquid pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump (9) and ft connection.
19. the dynamic co-feeding system of heat, is that in the heat described in claim 17 moves co-feeding system, engine (13) is had into exhaust passage It is sequentially communicated after the second generator (2), generator (1), evaporator (6) and the 3rd generator (16) the 3rd generator (16) again Having condensate liquid pipeline to be adjusted to engine (13) with ft connection has exhaust passage to be sequentially communicated the second generator (2), generator (1) and after the 3rd generator (16) the 3rd generator (16) has condensate liquid pipeline and ft connection again, and engine (13) is had The rear heat exchange (12) that second steam channel is connected with heat exchanger (12) has the second condensate liquid pipeline to be adjusted with ft connection again The whole finisher (6) for thering is the second steam channel to be connected with evaporator (6) for engine (13) have again the second condensate liquid pipeline and Ft connection, engine (13) sets up the rear heat exchange (12) that the 3rd steam channel connects with heat exchanger (12) the 3rd again Condensate liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
20. the dynamic co-feeding system of heat, is in the heat described in claim 19 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the second steam channel to be connected with evaporator (6) has the second condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the second steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) There is cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
21. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Two solution heat exchangers, the 3rd generator, the 3rd absorber and the 3rd solution pump are constituted;Engine (13) connects working machine (14), engine (13) has live steam passage and ft connection, also engine (13) or exhaust passage and ft connection, engine (13) also having exhaust passage to be sequentially communicated the second generator (2) and the 3rd generator (16), the 3rd generator (16) has cold again afterwards Lime set pipeline and ft connection, engine (13) also have the second steam channel to be sequentially communicated after generator (1) and evaporator (6) Evaporator (6) has the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel and heat exchanger (12) rear heat exchange (12) of connection has the 3rd condensate liquid pipeline and ft connection again;Generator (1) also has concentrated solution pipeline Connected through solution pump (7) and solution heat exchanger (11) with absorber (3), absorber (3) also has weak solution pipeline through solution heat Exchanger (11) is connected with generator (1), and generator (1) also has refrigerant steam channel to be connected with the second absorber (4), and second inhales Receiving device (4) also has weak solution pipeline to connect through the second solution pump (8) and the second solution heat exchanger (15) with the 3rd absorber (17) Logical, the 3rd absorber (17) also has weak solution pipeline to be connected through the 3rd solution pump (18) with the second generator (2), the second generator (2) concentrated solution pipeline is connected through solution choke valve (10) with the 3rd generator (16), the 3rd generator (16) also has dense molten Liquid pipeline is connected through the second solution heat exchanger (15) with the second absorber (4), and the 3rd generator (16) also has refrigerant vapour to lead to Road is connected with the 3rd absorber (17), and the second generator (2) also has refrigerant steam channel to be connected with condenser (5), condenser (5) Also cryogen liquid pipeline is connected through cryogen liquid pump (9) with evaporator (6), and evaporator (6) also has refrigerant steam channel and absorber (3) connect, condenser (5), the second absorber (4) and the 3rd absorber (17) also have cooling medium pipeline and outside to connect respectively Logical, absorber (3) also has heated medium pipeline and ft connection, and heat exchanger (12) also has heated medium pipeline and outside Connection, forms the dynamic co-feeding system of heat.
22. the dynamic co-feeding system of heat, is in the heat described in claim 21 moves co-feeding system, to cancel evaporator, by engine (13) have the second steam channel to be sequentially communicated generator (1) and the finisher (6) of evaporator (6) has the second condensate liquid pipeline again With ft connection be adjusted to engine (13) have the second steam channel connected with generator (1) after generator (1) have second again Condensate liquid pipeline and ft connection, have refrigerant steam channel to be connected with absorber (3) evaporator (6) and are adjusted to engine (13) Set up the second steam channel to connect with absorber (3), condenser (5) is had into cryogen liquid pipeline through cryogen liquid pump (9) and evaporator (6) connection, which is adjusted to condenser (5), has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, forms the dynamic co-feeding system of heat.
23. the dynamic co-feeding system of heat, is that in the heat described in claim 21 moves co-feeding system, engine (13) is had into the second steam Passage is sequentially communicated generator (1) and the finisher (6) of evaporator (6) has the second condensate liquid pipeline to be adjusted with ft connection again For engine (13) have the second steam channel connected with generator (1) after generator (1) have again the second condensate liquid pipeline with it is outer Portion is connected, and the rear heat exchange (12) that engine (13) has the 3rd steam channel to be connected with heat exchanger (12) is had into the 3rd cold again Lime set pipeline is adjusted to the finisher (6) that engine (13) has the 3rd steam channel to be connected with evaporator (6) with ft connection There are the 3rd condensate liquid pipeline and ft connection again, engine (13) is set up after the 4th steam channel connects with heat exchanger (12) Heat exchanger (12) has the 4th condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
24. the dynamic co-feeding system of heat, is in the heat described in claim 23 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the 3rd steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) There is cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
25. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Engine (13) connects work Make machine (14), engine (13) has live steam passage and ft connection, and engine (13) or also exhaust passage and ft connection are moved Power machine (13) also have exhaust passage connected with the 3rd generator (16) after the 3rd generator (16) have again condensate liquid pipeline with it is outer Portion is connected, and engine (13) also has the second steam channel to be sequentially communicated the second hair after generator (1) and the second generator (2) Raw device (2) has the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel to be connected with evaporator (6) Finisher (6) have the 3rd condensate liquid pipeline and ft connection again, engine (13) also has the 4th steam channel and heat exchange The rear heat exchange (12) of device (12) connection has the 4th condensate liquid pipeline and ft connection again;Generator (1) also has concentrated solution pipe Road is connected through solution pump (7) and solution heat exchanger (11) with absorber (3), and absorber (3) also has weak solution pipeline through solution Heat exchanger (11) is connected with generator (1), and generator (1) also has refrigerant steam channel to be connected with the second absorber (4), and second Absorber (4) also has weak solution pipeline through the second solution pump (8) and the second solution heat exchanger (15) and the 3rd absorber (17) Connection, the 3rd absorber (17) also has weak solution pipeline through the 3rd solution pump (18) and the 3rd solution heat exchanger (19) and second Generator (2) is connected, and the second generator (2) also has concentrated solution pipeline through the 3rd solution heat exchanger (19) and the 3rd generator (16) connect, the 3rd generator (16) also has concentrated solution pipeline to connect through the second solution heat exchanger (15) and the second absorber (4) Logical, the 3rd generator (16) also has refrigerant steam channel to be connected with the 3rd absorber (17), and the second generator (2) also has cryogen steaming Vapour passage is connected with condenser (5), and condenser (5) also has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6), is steamed Hair device (6) also has refrigerant steam channel to be connected with absorber (3), condenser (5), the second absorber (4) and the 3rd absorber (17) also there are cooling medium pipeline and ft connection respectively, absorber (3) also has heated medium pipeline and ft connection, and heat is handed over Parallel operation (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
26. the dynamic co-feeding system of heat, is in the heat described in claim 25 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the 3rd steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) There is cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic co-feeding system of heat.
27. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporator and the second cryogen liquid pump are constituted;Engine (13) Working machine (14) is connected, engine (13) has live steam passage and ft connection, also engine (13) or exhaust passage and outside Connection, engine (13) also has exhaust passage to be sequentially communicated generator (1), evaporator (6), the second evaporator (20) and the second hair The second generator (2) has condensate liquid pipeline and a ft connection again after raw device (2), engine (13) also have the second steam channel with The rear heat exchange (12) of heat exchanger (12) connection has the second condensate liquid pipeline and ft connection again;Second generator (2) is also There is concentrated solution pipeline to be connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), absorber (3) is also dilute Solution line is connected through solution heat exchanger (11) with the second absorber (4), and the second absorber (4) also has weak solution pipeline through molten Liquid pump (7) is connected with generator (1), and generator (1) also has concentrated solution pipeline through solution choke valve (10) and the second generator (2) Connection, the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), and generator (1) also has refrigerant vapour to lead to The 3rd generator (16) has cryogen liquid pipeline to be connected with the second cryogen liquid pump (21) again after road is connected with the 3rd generator (16), Second cryogen liquid pump (21) also has cryogen liquid pipeline to be connected with evaporator (6), and evaporator (6) also has refrigerant steam channel and absorption Device (3) is connected;3rd generator (16) also has concentrated solution pipeline through the 3rd solution pump (18) and the second solution heat exchanger (15) Connected with the 3rd absorber (17), the 3rd absorber (17) also has weak solution pipeline through the second solution heat exchanger (15) and the 3rd Generator (16) is connected, and the 3rd generator (16) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) is also cold Agent liquid pipeline is connected through cryogen liquid pump (9) with the second evaporator (20), and the second evaporator (20) also has refrigerant steam channel and the Three absorbers (17) are connected, and condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, are absorbed Device (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, form the dynamic co-feeding system of heat.
28. the dynamic co-feeding system of heat, is in the heat described in claim 27 moves co-feeding system, to cancel evaporator, by engine (13) exhaust passage is sequentially communicated after generator (1), evaporator (6), the second evaporator (20) and the second generator (2) the Two generators (2) have condensate liquid pipeline to be adjusted to engine (13) with ft connection again has exhaust passage to be sequentially communicated generator (1), the second generator (2) has condensate liquid pipeline and ft connection again afterwards for the second evaporator (20) and the second generator (2), will Evaporator (6) has refrigerant steam channel to connect with absorber (3) to be adjusted to engine (13) and set up exhaust passage and absorber (3) Connection, has cryogen liquid pipeline to be connected with evaporator (6) the second cryogen liquid pump (21) and is adjusted to the second cryogen liquid pump (21) and has cold Agent liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
29. the dynamic co-feeding system of heat, is that in the heat described in claim 27 moves co-feeding system, engine (13) is had into exhaust passage It is sequentially communicated after generator (1), evaporator (6), the second evaporator (20) and the second generator (2) the second generator (2) again Having condensate liquid pipeline to be adjusted to engine (13) with ft connection has exhaust passage to be sequentially communicated generator (1) and the second generator (2) the second generator (2) has condensate liquid pipeline and ft connection again after, has the second steam channel to be handed over heat in engine (13) The rear heat exchange (12) of parallel operation (12) connection has the second condensate liquid pipeline and ft connection to be adjusted to engine (13) again the The second evaporator (20) has the second condensate line again after two steam channels are sequentially communicated evaporator (6) and the second evaporator (20) Road and ft connection, engine (13) sets up the rear heat exchange (12) that the 3rd steam channel connects with heat exchanger (12) to be had again 3rd condensate liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
30. the dynamic co-feeding system of heat, is in the heat described in claim 29 moves co-feeding system, to cancel evaporator, by engine (13) having the second steam channel to be sequentially communicated evaporator (6) and the second evaporator (20), the second evaporator (20) has second again afterwards Condensate liquid pipeline and ft connection be adjusted to engine (13) have the second steam channel connected with the second evaporator (20) after Two evaporators (20) have the second condensate liquid pipeline and ft connection again, and evaporator (6) is had into refrigerant steam channel and absorber (3) Connection is adjusted to engine (13) and sets up the second steam channel to connect with absorber (3), and the second cryogen liquid pump (21) is had into cryogen Liquid pipeline is connected with evaporator (6) to be adjusted to the second cryogen liquid pump (21) and has cryogen liquid pipeline and a ft connection, forms the dynamic connection of heat For system.
31. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the second evaporator and the second cryogen liquid pump are constituted;Engine (13) Working machine (14) is connected, engine (13) has live steam passage and ft connection, also engine (13) or exhaust passage and outside Connection, engine (13) also has exhaust passage to be sequentially communicated the second generator (2) after generator (1) and the second generator (2) Have condensate liquid pipeline and ft connection again, engine (13) also have the second steam channel connected with the second evaporator (20) after Two evaporators (20) have the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel and evaporator (6) finisher (6) of connection has the 3rd condensate liquid pipeline and a ft connection again, engine (13) also have the 4th steam channel with The rear heat exchange (12) of heat exchanger (12) connection has the 4th condensate liquid pipeline and ft connection again;Second generator (2) is also There is concentrated solution pipeline to be connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), absorber (3) is also dilute Solution line is connected through solution heat exchanger (11) with the second absorber (4), and the second absorber (4) also has weak solution pipeline through molten Liquid pump (7) is connected with generator (1), and generator (1) also has concentrated solution pipeline through solution choke valve (10) and the second generator (2) Connection, the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), and generator (1) also has refrigerant vapour to lead to The 3rd generator (16) has cryogen liquid pipeline to be connected with the second cryogen liquid pump (21) again after road is connected with the 3rd generator (16), Second cryogen liquid pump (21) also has cryogen liquid pipeline to be connected with evaporator (6), and evaporator (6) also has refrigerant steam channel and absorption Device (3) is connected;3rd generator (16) also has concentrated solution pipeline through the 3rd solution pump (18) and the second solution heat exchanger (15) Connected with the 3rd absorber (17), the 3rd absorber (17) also has weak solution pipeline through the second solution heat exchanger (15) and the 3rd Generator (16) is connected, and the 3rd generator (16) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) is also cold Agent liquid pipeline is connected through cryogen liquid pump (9) with the second evaporator (20), and the second evaporator (20) also has refrigerant steam channel and the Three absorbers (17) are connected, and condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, are absorbed Device (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, form the dynamic co-feeding system of heat.
32. the dynamic co-feeding system of heat, is in the heat described in claim 31 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the 3rd steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected with evaporator (6) the second cryogen liquid pump (21) and is adjusted to the second cryogen liquid pump (21) There are cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
33. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator and the second cryogen liquid pump Constituted;Engine (13) connection working machine (14), engine (13) has live steam passage and a ft connection, engine (13) or also Have an exhaust passage and ft connection, engine (13) also have exhaust passage connected with the second generator (2) after the second generator (2) there are condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be sequentially communicated generator (1), evaporation The second evaporator (20) has the second condensate liquid pipeline and ft connection, engine again after device (6) and the second evaporator (20) (13) rear heat exchange (12) for also having the 3rd steam channel to be connected with heat exchanger (12) has the 3rd condensate liquid pipeline and outer again Portion is connected;Second generator (2) also has concentrated solution pipeline through the second solution pump (8) and solution heat exchanger (11) and absorber (3) connect, absorber (3) also has weak solution pipeline to be connected through solution heat exchanger (11) with the second absorber (4), second absorbs Device (4) also has weak solution pipeline to be connected through solution pump (7) and the second solution heat exchanger (15) with generator (1), generator (1) Also concentrated solution pipeline is connected through the second solution heat exchanger (15) with the second generator (2), and the second generator (2) also has cryogen Steam channel is connected with the second absorber (4), and generator (1) also has after refrigerant steam channel connects with the 3rd generator (16) 3rd generator (16) has cryogen liquid pipeline to be connected with the second cryogen liquid pump (21) again, and the second cryogen liquid pump (21) also has cryogen liquid Pipeline is connected with evaporator (6), and evaporator (6) also has refrigerant steam channel to be connected with absorber (3);3rd generator (16) is also There is concentrated solution pipeline to be connected through the 3rd solution pump (18) and the 3rd solution heat exchanger (19) with the 3rd absorber (17), the 3rd inhales Receiving device (17) also has weak solution pipeline to be connected through the 3rd solution heat exchanger (19) with the 3rd generator (16), the 3rd generator (16) refrigerant steam channel is connected with condenser (5), condenser (5) also has cryogen liquid pipeline through cryogen liquid pump (9) and the Two evaporators (20) are connected, and the second evaporator (20) also has refrigerant steam channel to be connected with the 3rd absorber (17), condenser (5) Also there are cooling medium pipeline and ft connection respectively with the second absorber (4), absorber (3) and the 3rd absorber (17) are also distinguished There are heated medium pipeline and ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, forms heat dynamic Co-feeding system.
34. the dynamic co-feeding system of heat, is in the heat described in claim 33 moves co-feeding system, to cancel evaporator, by engine (13) the second steam channel is sequentially communicated the second evaporator after generator (1), evaporator (6) and the second evaporator (20) (20) having the second condensate liquid pipeline to be adjusted to engine (13) with ft connection again has the second steam channel to be sequentially communicated generator (1) and after the second evaporator (20) the second evaporator (20) has the second condensate liquid pipeline and ft connection again, by evaporator (6) There is refrigerant steam channel to connect with absorber (3) to be adjusted to engine (13) and set up the second steam channel to connect with absorber (3), There is cryogen liquid pipeline to connect with evaporator (6) the second cryogen liquid pump (21) to be adjusted to the second cryogen liquid pump (21) and have cryogen liquid pipe Road and ft connection, form the dynamic co-feeding system of heat.
35. the dynamic co-feeding system of heat, is that in the heat described in claim 33 moves co-feeding system, engine (13) is had into the second steam The second evaporator (20) has the second condensation again after passage is sequentially communicated generator (1), evaporator (6) and the second evaporator (20) Liquid pipeline is adjusted to engine (13) with ft connection has the second steam channel to be sequentially communicated generator after generator (1) is connected (1) there are the second condensate liquid pipeline and ft connection again, there is the 3rd steam channel to be connected with heat exchanger (12) in engine (13) Rear heat exchange (12) have again the 3rd condensate liquid pipeline and ft connection be adjusted to engine (13) have the 3rd steam channel according to The second evaporator (20) has the 3rd condensate liquid pipeline to connect with outside again after secondary connection evaporator (6) and the second evaporator (20) Logical, engine (13) sets up the rear heat exchange (12) that the 4th steam channel connects with heat exchanger (12) the 4th condensate liquid again Pipeline and ft connection, form the dynamic co-feeding system of heat.
36. the dynamic co-feeding system of heat, is in the heat described in claim 35 moves co-feeding system, to cancel evaporator, by engine (13) having the 3rd steam channel to be sequentially communicated evaporator (6) and the second evaporator (20), the second evaporator (20) has the 3rd again afterwards Condensate liquid pipeline and ft connection be adjusted to engine (13) have the 3rd steam channel connected with the second evaporator (20) after Two evaporators (20) have the 3rd condensate liquid pipeline and ft connection again, and evaporator (6) is had into refrigerant steam channel and absorber (3) Connection is adjusted to engine (3) and sets up the 3rd steam channel to connect with absorber (3), and the second cryogen liquid pump (21) is had into cryogen liquid Pipeline is connected with evaporator (6) to be adjusted to the second cryogen liquid pump (21) and has cryogen liquid pipeline and a ft connection, forms the dynamic alliance of heat System.
37. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator and the second cryogen liquid pump Constituted;Engine (13) connection working machine (14), engine (13) has live steam passage and a ft connection, engine (13) or also Have an exhaust passage and ft connection, engine (13) also have exhaust passage connected with the second generator (2) after the second generator (2) there are condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to occur after being connected with generator (1) Device (1) has the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel and the second evaporator (20) The second evaporator (20) has the 3rd condensate liquid pipeline and ft connection again after connection, and engine (13) also has the 4th steam channel There are the 4th condensate liquid pipeline and ft connection again with the finisher (6) of evaporator (6), engine (13) also has the 5th steam to lead to The rear heat exchange (12) that road is connected with heat exchanger (12) has the 5th condensate liquid pipeline and ft connection again;Second generator (2) concentrated solution pipeline is connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), absorber (3) is also There is weak solution pipeline to be connected through solution heat exchanger (11) with the second absorber (4), the second absorber (4) also has weak solution pipeline Connected through solution pump (7) and the second solution heat exchanger (15) with generator (1), generator (1) also has concentrated solution pipeline through Two solution heat exchangers (15) are connected with the second generator (2), and the second generator (2) also has refrigerant steam channel to be absorbed with second Device (4) connect, generator (1) also have refrigerant steam channel connected with the 3rd generator (16) after the 3rd generator (16) have again Cryogen liquid pipeline is connected with the second cryogen liquid pump (21), and the second cryogen liquid pump (21) also has cryogen liquid pipeline to connect with evaporator (6) Logical, evaporator (6) also has refrigerant steam channel to be connected with absorber (3);3rd generator (16) also has concentrated solution pipeline through Three solution pumps (18) and the 3rd solution heat exchanger (19) are connected with the 3rd absorber (17), and the 3rd absorber (17) also has dilute molten Liquid pipeline is connected through the 3rd solution heat exchanger (19) with the 3rd generator (16), and the 3rd generator (16) also has refrigerant vapour Passage is connected with condenser (5), and condenser (5) also has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with the second evaporator (20), Second evaporator (20) also has refrigerant steam channel to be connected with the 3rd absorber (17), and condenser (5) and the second absorber (4) are also There are cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline respectively With ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
38. the dynamic co-feeding system of heat, is in the heat described in claim 37 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 4th steam channel to be connected with evaporator (6) has the 4th condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the 4th steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected with evaporator (6) the second cryogen liquid pump (21) and is adjusted to the second cryogen liquid pump (21) There are cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
39. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution choke valve, solution heat exchanger, heat exchanger, engine, working machine, Two solution heat exchangers, the 3rd generator, the 3rd absorber, the 3rd solution pump and the second cryogen liquid pump are constituted;Engine (13) connection working machine (14), engine (13) has live steam passage and a ft connection, engine (13) or also exhaust passage with Ft connection, engine (13) also has exhaust passage to be sequentially communicated after generator (1), evaporator (6) and the second generator (2) Second generator (2) has condensate liquid pipeline and ft connection again, and engine (13) also has the second steam channel and heat exchanger (12) rear heat exchange (12) of connection has the second condensate liquid pipeline and ft connection again;Second generator (2) also has concentrated solution Pipeline is connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), and absorber (3) also has weak solution pipeline Connected through solution heat exchanger (11) with the second absorber (4), the second absorber (4) also has weak solution pipeline through solution pump (7) Connected with generator (1), generator (1) also has concentrated solution pipeline to be connected through solution choke valve (10) with the second generator (2), the Two generators (2) also have refrigerant steam channel to be connected with the second absorber (4), and generator (1) also has refrigerant steam channel and the The 3rd generator (16) has cryogen liquid pipeline to be connected with the second cryogen liquid pump (21) again after three generators (16) connection, and second is cold Agent liquid pump (21) also has cryogen liquid pipeline to be connected with evaporator (6);3rd generator (16) also has concentrated solution pipeline molten through the 3rd Liquid pump (18) and the second solution heat exchanger (15) are connected with the 3rd absorber (17), and the 3rd absorber (17) also has weak solution pipe The solution heat exchanger of road second (15) is connected with the 3rd generator (16), the 3rd generator (16) also have refrigerant steam channel with Condenser (5) is connected, and condenser (5) also has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6), and evaporator (6) is also There is refrigerant steam channel to be connected respectively with absorber (3) and the 3rd absorber (17), condenser (5) and the second absorber (4) are also There are cooling medium pipeline and ft connection respectively, absorber (3) and the 3rd absorber (17) also have heated medium pipeline respectively With ft connection, heat exchanger (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
40. the dynamic co-feeding system of heat, is in the heat described in claim 39 moves co-feeding system, to cancel evaporator, by engine (13) having exhaust passage to be sequentially communicated generator (1), evaporator (6) and the second generator (2), the second generator (2) has again afterwards Condensate liquid pipeline is adjusted to engine (13) with ft connection has exhaust passage to be sequentially communicated generator (1) and the second generator (2) after the second generator (2) have condensate liquid pipeline and ft connection again, by evaporator (6) have refrigerant steam channel respectively with Absorber (3) and the connection of the 3rd absorber (17) be adjusted to engine (13) set up exhaust passage respectively with absorber (3) and the Three absorbers (17) are connected, and are had cryogen liquid pipeline to be connected with evaporator (6) the second cryogen liquid pump (21) and are adjusted to the second cryogen Liquid pump (21) has cryogen liquid pipeline and ft connection, and condenser (5) is had into cryogen liquid pipeline through cryogen liquid pump (9) and evaporator (6) connection, which is adjusted to condenser (5), has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, forms the dynamic co-feeding system of heat.
41. the dynamic co-feeding system of heat, is that in the heat described in claim 39 moves co-feeding system, engine (13) is had into exhaust passage The second generator (2) has condensate liquid pipeline and outer again after being sequentially communicated generator (1), evaporator (6) and the second generator (2) Portion's connection, which is adjusted to engine (13), has exhaust passage to be sequentially communicated the second generation after generator (1) and the second generator (2) Device (2) has condensate liquid pipeline and ft connection again, has the second steam channel to connect it with heat exchanger (12) in engine (13) Rear heat exchange (12) has the second condensate liquid pipeline to be adjusted to engine (13) with ft connection again the second steam channel and steaming The finisher (6) of hair device (6) connection has the second condensate liquid pipeline and ft connection again, and engine (13) is set up the 3rd steam and led to The rear heat exchange (12) that road is connected with heat exchanger (12) has the 3rd condensate liquid pipeline and ft connection again, forms the dynamic alliance of heat System.
42. the dynamic co-feeding system of heat, is in the heat described in claim 41 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the second steam channel to be connected with evaporator (6) has the second condensate liquid pipeline and ft connection, steaming again Hair device (6) has refrigerant steam channel to connect with absorber (3) and the 3rd absorber (17) respectively and be adjusted to engine (13) in the lump There is the second steam channel to be connected respectively with absorber (3) and the 3rd absorber (17), the second cryogen liquid pump (21) is had into cryogen liquid Pipeline is connected with evaporator (6) to be adjusted to the second cryogen liquid pump (21) and has cryogen liquid pipeline and ft connection, and condenser (5) is had Cryogen liquid pipeline is connected through cryogen liquid pump (9) with evaporator (6) to be adjusted to condenser (5) and has cryogen liquid pipeline through cryogen liquid pump (9) the dynamic co-feeding system of heat and ft connection, is formed.
43. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump are constituted;Power Machine (13) connection working machine (14), engine (13) has live steam passage and ft connection, also engine (13) or exhaust passage With ft connection, engine (13) also have exhaust passage connected with the second generator (2) after the second generator (2) have condensation again Liquid pipeline and ft connection, engine (13) also have the second steam channel to be steamed after being sequentially communicated generator (1) and evaporator (6) Hair device (6) has the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel and heat exchanger (12) The rear heat exchange (12) of connection has the 3rd condensate liquid pipeline and ft connection again;Second generator (2) also has concentrated solution pipeline Connected through the second solution pump (8) and solution heat exchanger (11) with absorber (3), absorber (3) also has weak solution pipeline through molten Liquid heat exchanger (11) is connected with the second absorber (4), and the second absorber (4) also has weak solution pipeline through solution pump (7) and Two solution heat exchangers (15) are connected with generator (1), and generator (1) also has concentrated solution pipeline through the second solution heat exchanger (15) connect, the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), occur with the second generator (2) Device (1) also have refrigerant steam channel connected with the 3rd generator (16) after the 3rd generator (16) have cryogen liquid pipeline and again Two cryogen liquid pumps (21) are connected, and the second cryogen liquid pump (21) also has cryogen liquid pipeline to be connected with evaporator (6);3rd generator (16) concentrated solution pipeline is connected through the 3rd solution pump (18) and the 3rd solution heat exchanger (19) with the 3rd absorber (17), 3rd absorber (17) also has weak solution pipeline to be connected through the 3rd solution heat exchanger (19) with the 3rd generator (16), the 3rd hair Raw device (16) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) also has cryogen liquid pipeline through cryogen liquid pump (9) Connected with evaporator (6), evaporator (6) also has refrigerant steam channel to be connected respectively with absorber (3) and the 3rd absorber (17); Condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection, absorber (3) and the 3rd absorber respectively (17) also there are heated medium pipeline and ft connection respectively, heat exchanger (12) also has heated medium pipeline to connect with outside It is logical, form the dynamic co-feeding system of heat.
44. the dynamic co-feeding system of heat, is in the heat described in claim 43 moves co-feeding system, to cancel evaporator, by engine (13) have the second steam channel to be sequentially communicated generator (1) and the finisher (6) of evaporator (6) has the second condensate liquid pipeline again With ft connection be adjusted to engine (13) have second channel connected with generator (1) after generator (1) have the second condensation again Liquid pipeline and ft connection, have refrigerant steam channel to be connected respectively with absorber (3) and the 3rd absorber (17) evaporator (6) It is adjusted to engine (13) and sets up the second steam channel to connect with absorber (3) and the 3rd absorber (17) respectively, by condenser (5) there is cryogen liquid pipeline to connect with evaporator (6) through cryogen liquid pump (9) to be adjusted to condenser (5) and have cryogen liquid pipeline through cryogen Liquid pump (9) and ft connection, have cryogen liquid pipeline to be connected with evaporator (6) the second cryogen liquid pump (21) and are adjusted to the second cryogen Liquid pump (21) has cryogen liquid pipeline and ft connection, forms the dynamic co-feeding system of heat.
45. the dynamic co-feeding system of heat, is that in the heat described in claim 43 moves co-feeding system, engine (13) is had into the second steam Passage is sequentially communicated generator (1) and the finisher (6) of evaporator (6) has the second condensate liquid pipeline to be adjusted with ft connection again For engine (13) have second channel connected with generator (1) after generator (1) there is the second condensate liquid pipeline to connect with outside again It is logical, the rear heat exchange (12) that engine (13) has the 3rd steam channel to be connected with heat exchanger (12) there is into the 3rd condensate liquid again The finisher (6) that pipeline is adjusted to engine (13) with ft connection and has the 3rd steam channel to be connected with evaporator (6) has again 3rd condensate liquid pipeline and ft connection, engine (13) set up heat friendship after the 4th steam channel is connected with heat exchanger (12) Parallel operation (12) has the 4th condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
46. the dynamic co-feeding system of heat, is in the heat described in claim 45 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, steaming again Hair device (6) has refrigerant steam channel to connect with absorber (3) and the 3rd absorber (17) respectively to be adjusted to engine (13) and have the Three steam channels are connected with absorber (3) and the 3rd absorber (17) respectively, and condenser (5) is had into cryogen liquid pipeline through cryogen liquid Pump (9) is connected with evaporator (6) to be adjusted to condenser (5) and has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, by second Cryogen liquid pump (21) have cryogen liquid pipeline connected with evaporator (6) be adjusted to the second cryogen liquid pump (21) have cryogen liquid pipeline with it is outer Portion is connected, and forms the dynamic co-feeding system of heat.
47. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator and the second cryogen liquid pump Constituted;Engine (13) connection working machine (14), engine (13) has live steam passage and a ft connection, engine (13) or also Have an exhaust passage and ft connection, engine (13) also have exhaust passage connected with the second generator (2) after the second generator (2) there are condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be sequentially communicated generator (1), evaporation The second evaporator (20) has the second condensate liquid pipeline and ft connection, engine again after device (6) and the second evaporator (20) (13) rear heat exchange (12) for also having the 3rd steam channel to be connected with heat exchanger (12) has the 3rd condensate liquid pipeline and outer again Portion is connected;Generator (1) also has concentrated solution pipeline to be connected through solution pump (7) and solution heat exchanger (11) with absorber (3), inhales Receiving device (3) also has weak solution pipeline to be connected through solution heat exchanger (11) with generator (1), and generator (1) also has refrigerant vapour After passage is connected with the 3rd generator (16) the 3rd generator (16) have again cryogen liquid pipeline through the second cryogen liquid pump (21) with Evaporator (6) is connected, and evaporator (6) also has refrigerant steam channel to be connected with absorber (3);Second generator (2) also has dense molten Liquid pipeline is connected through the second solution pump (8) and the second solution heat exchanger (15) with the 3rd absorber (17), the 3rd absorber (17) weak solution pipeline is connected through the second solution heat exchanger (15) with the second absorber (4), the second absorber (4) also has Weak solution pipeline is connected through the 3rd solution pump (18) and the 3rd solution heat exchanger (19) with the 3rd generator (16), and the 3rd occurs Device (16) also has concentrated solution pipeline to be connected through the 3rd solution heat exchanger (19) with the second generator (2), and the second generator (2) is also There is refrigerant steam channel to be connected with the second absorber (4), the 3rd generator (16) also has refrigerant steam channel and condenser (5) Connection, condenser (5) also has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with the second evaporator (20), the second evaporator (20) Also refrigerant steam channel is connected with the 3rd absorber (17);Condenser (5) and the second absorber (4) also have cooling medium respectively Pipeline and ft connection, absorber (3) and the 3rd absorber (17) also have heated medium pipeline and ft connection respectively, and heat is handed over Parallel operation (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
48. the dynamic co-feeding system of heat, is in the heat described in claim 47 moves co-feeding system, to cancel evaporator, by engine (13) the second steam channel is sequentially communicated the second evaporator after generator (1), evaporator (6) and the second evaporator (20) (20) having the second condensate liquid pipeline to be adjusted to engine (13) with ft connection again has the second steam channel to be sequentially communicated generator (1) and after the second evaporator (20) the second evaporator (20) has the second condensate liquid pipeline and ft connection again, by evaporator (6) There is refrigerant steam channel to connect with absorber (3) to be adjusted to engine (13) and set up the second steam channel to connect with absorber (3), There is cryogen liquid pipeline to connect with evaporator (6) the second cryogen liquid pump (21) to be adjusted to the second cryogen liquid pump (21) and have cryogen liquid pipe Road and ft connection, form the dynamic co-feeding system of heat.
49. the dynamic co-feeding system of heat, is that in the heat described in claim 47 moves co-feeding system, engine (13) is had into the second steam The second evaporator (20) has the second condensation again after passage is sequentially communicated generator (1), evaporator (6) and the second evaporator (20) Liquid pipeline is adjusted to engine (13) with ft connection has the second steam channel to be sequentially communicated generator (1) and the second evaporator (20) the second evaporator (20) has the second condensate liquid pipeline and ft connection again after, and engine (13) is had into the 3rd steam channel The rear heat exchange (12) connected with heat exchanger (12) has the 3rd condensate liquid pipeline to be adjusted to engine with ft connection again (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection again, moves Power machine (13) sets up the rear heat exchange (12) that the 4th steam channel connects with heat exchanger (12) the 4th condensate liquid pipeline again With ft connection, the dynamic co-feeding system of heat is formed.
50. the dynamic co-feeding system of heat, is in the heat described in claim 49 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, steaming again Hair device (6) have refrigerant steam channel connect with absorber (3) be adjusted in the lump engine (13) have the 3rd steam channel and absorb Device (3) is connected, and is had cryogen liquid pipeline to be connected with evaporator (6) the second cryogen liquid pump (21) and is adjusted to the second cryogen liquid pump (21) There are cryogen liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
51. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Solution pump, the second solution pump, cryogen liquid pump, solution heat exchanger, heat exchanger, engine, working machine, the second solution heat exchange Device, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump are constituted;Power Machine (13) connection working machine (14), engine (13) has live steam passage and ft connection, also engine (13) or exhaust passage With ft connection, engine (13) also have exhaust passage connected with the second generator (2) after the second generator (2) have condensation again Liquid pipeline and ft connection, engine (13) also have the second steam channel to be steamed after being sequentially communicated generator (1) and evaporator (6) Hair device (6) has the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel and heat exchanger (12) The rear heat exchange (12) of connection has the 3rd condensate liquid pipeline and ft connection again;Generator (1) also has concentrated solution pipeline through molten Liquid pump (7) and solution heat exchanger (11) are connected with absorber (3), and absorber (3) also has weak solution pipeline through solution heat exchange Device (11) is connected with generator (1), generator (1) also have refrigerant steam channel connected with the 3rd generator (16) after the 3rd hair Raw device (16) has cryogen liquid pipeline to be connected with the second cryogen liquid pump (21) again, the second cryogen liquid pump (21) also have cryogen liquid pipeline and Evaporator (6) is connected;Second generator (2) also has concentrated solution pipeline through the second solution pump (8) and the second solution heat exchanger (15) connected with the 3rd absorber (17), the 3rd absorber (17) also have weak solution pipeline through the second solution heat exchanger (15) with Second absorber (4) is connected, and the second absorber (4) also has weak solution pipeline to be handed over through the 3rd solution pump (18) and the 3rd solution heat Parallel operation (19) is connected with the 3rd generator (16), and the 3rd generator (16) also has concentrated solution pipeline through the 3rd solution heat exchanger (19) connected with the second generator (2), the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), the 3rd Generator (16) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) also has cryogen liquid pipeline through cryogen liquid pump (9) connected with evaporator (6), evaporator (6) also has refrigerant steam channel to connect respectively with absorber (3) and the 3rd absorber (17) It is logical;Condenser (5) and the second absorber (4) also have cooling medium pipeline and ft connection respectively, and absorber (3) and the 3rd absorb Device (17) also has heated medium pipeline and ft connection respectively, and heat exchanger (12) also has heated medium pipeline to connect with outside It is logical, form the dynamic co-feeding system of heat.
52. the dynamic co-feeding system of heat, is in the heat described in claim 51 moves co-feeding system, to cancel evaporator, by engine (13) have the second steam channel to be sequentially communicated generator (1) and the finisher (6) of evaporator (6) has the second condensate liquid pipeline again With ft connection be adjusted to engine (13) have the second steam channel connected with generator (1) after generator (1) have second again Condensate liquid pipeline and ft connection, by evaporator (6) have refrigerant steam channel respectively with absorber (3) and the 3rd absorber (17) Connection is adjusted to engine (13) and sets up the second steam channel to connect with absorber (3) and the 3rd absorber (17) respectively, by the Two cryogen liquid pumps (21) have cryogen liquid pipeline connected with evaporator (6) be adjusted to the second cryogen liquid pump (21) have cryogen liquid pipeline with Ft connection, has cryogen liquid pipeline to be connected through cryogen liquid pump (9) with evaporator (6) condenser (5) and is adjusted to condenser (5) and has Cryogen liquid pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump (9) and ft connection.
53. the dynamic co-feeding system of heat, is that in the heat described in claim 51 moves co-feeding system, engine (13) is had into the second steam Passage is sequentially communicated generator (1) and the finisher (6) of evaporator (6) has the second condensate liquid pipeline to be adjusted with ft connection again For engine (13) have the second steam channel connected with generator (1) after generator (1) have again the second condensate liquid pipeline with it is outer Portion is connected, and the rear heat exchange (12) that engine (13) has the 3rd steam channel to be connected with heat exchanger (12) is had into the 3rd cold again Lime set pipeline is adjusted to the finisher (6) that engine (13) has the 3rd steam channel to be connected with evaporator (6) with ft connection There are the 3rd condensate liquid pipeline and ft connection again, engine (13) is set up after the 4th steam channel connects with heat exchanger (12) Heat exchanger (12) has the 4th condensate liquid pipeline and ft connection again, forms the dynamic co-feeding system of heat.
54. the dynamic co-feeding system of heat, is in the heat described in claim 53 moves co-feeding system, to cancel evaporator, by engine (13) finisher (6) for having the 3rd steam channel to be connected with evaporator (6) has the 3rd condensate liquid pipeline and ft connection, steaming again Hair device (13) has refrigerant steam channel to connect with absorber (3) and the 3rd absorber (17) respectively to be adjusted to engine (13) and have the Three steam channels are connected with absorber (3) and the 3rd absorber (17) respectively, and the second cryogen liquid pump (21) is had into cryogen liquid pipeline Connected with evaporator (6) and be adjusted to the second cryogen liquid pump (21) and have cryogen liquid pipeline and ft connection, condenser (5) is had into cryogen Liquid pipeline connected through cryogen liquid pump (9) with evaporator (6) be adjusted to condenser (5) have cryogen liquid pipeline through cryogen liquid pump (9) with Ft connection, forms the dynamic co-feeding system of heat.
55. the dynamic co-feeding system of heat, is in any hot described in claim 1,3,5,7,9,11,13,15 moves co-feeding system, to increase Plus newly-increased absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, it will absorb Device (3) has weak solution pipeline to connect with the second absorber (4) through solution heat exchanger (11) to be adjusted to absorber (3) and have weak solution Pipeline is connected with newly-increased absorber (A), and newly-increased absorber (A) also has weak solution pipeline through newly-increased solution pump (C) and new solubilization liquid Heat exchanger (E) is connected with newly-increased second absorber (B), and newly-increased second absorber (B) has weak solution pipeline through new solubilization liquid again Heat exchanger (E) and solution heat exchanger (11) are connected with the second absorber (4), evaporator (6) set up refrigerant steam channel with Newly-increased absorber (A) connection, condenser (5) sets up cryogen liquid pipeline through increasing cryogen liquid pump (D) and newly-increased absorber (A) newly even Newly-increased absorber (A) has refrigerant steam channel to be connected with newly-increased second absorber (B) again after logical, increases the second absorber (B) newly Also heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
56. the dynamic co-feeding system of heat, is that increase is new in any hot described in claim 17,19,21,25,26 moves co-feeding system Increase absorber, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and newly-increased solution heat exchanger, by absorber (3) Have weak solution pipeline connected through solution heat exchanger (11) with generator (1) be adjusted to absorber (3) have weak solution pipeline with it is new Increase absorber (A) connection, newly-increased absorber (A) also has weak solution pipeline through newly-increased solution pump (C) and newly-increased solution heat exchanger (E) connected with newly-increased second absorber (B), newly-increased second absorber (B) has weak solution pipeline through newly-increased solution heat exchanger again (E) connected with solution heat exchanger (11) with generator (1), evaporator (6) sets up refrigerant steam channel and newly-increased absorber (A) Connection, condenser (5), which is set up to increase newly after cryogen liquid pipeline is connected through newly-increased cryogen liquid pump (D) with newly-increased absorber (A), to be absorbed Device (A) has refrigerant steam channel to be connected with newly-increased second absorber (B) again, and newly-increased second absorber (B) also has heated medium Pipeline and ft connection, form the dynamic co-feeding system of heat.
57. the dynamic co-feeding system of heat, is in the dynamic connection of any hot described in claim 27,29,31,33,35,37,39,41,43,45 For in system, the newly-increased absorber of increase, newly-increased second absorber, newly-increased solution pump, newly-increased cryogen liquid pump and new solubilization liquid heat are handed over Parallel operation, has weak solution pipeline to be connected through solution heat exchanger (11) with the second absorber (4) absorber (3) and is adjusted to absorber (3) weak solution pipeline is connected with newly-increased absorber (A), newly-increased absorber (A) also has weak solution pipeline through newly-increased solution pump (C) Connected with newly-increased solution heat exchanger (E) with newly-increased second absorber (B), newly-increased second absorber (B) has weak solution pipeline again Connected through newly-increased solution heat exchanger (E) and solution heat exchanger (11) with the second absorber (4), evaporator (6) sets up cryogen Steam channel is connected with newly-increased absorber (A), and generator (1) is had after refrigerant steam channel connects with the 3rd generator (16) 3rd generator (16) have again cryogen liquid pipeline connected with the second cryogen liquid pump (21) be adjusted to generator (1) have refrigerant vapour lead to After road is connected with the 3rd generator (16) the 3rd generator (16) have again cryogen liquid pipeline respectively with the second cryogen liquid pump (21) Connected with newly-increased cryogen liquid pump (D), newly-increased cryogen liquid pump (D) also has cryogen liquid pipeline new after being connected with newly-increased absorber (A) Increase absorber (A) has refrigerant steam channel to be connected with newly-increased second absorber (B) again, and newly-increased second absorber (B), which also has, to be added Heat medium pipeline and ft connection, form the dynamic co-feeding system of heat.
58. the dynamic co-feeding system of heat, is in any hot described in claim 1-57 moves co-feeding system, to cancel heat exchanger, take Disappear the heated medium pipeline connected with heat exchanger (12), forms the dynamic co-feeding system of heat.
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