CN104654653B - The dynamic co-feeding system of heat - Google Patents

The dynamic co-feeding system of heat Download PDF

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CN104654653B
CN104654653B CN201510043223.0A CN201510043223A CN104654653B CN 104654653 B CN104654653 B CN 104654653B CN 201510043223 A CN201510043223 A CN 201510043223A CN 104654653 B CN104654653 B CN 104654653B
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absorber
generator
solution
heat exchanger
pipeline
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CN104654653A (en
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李华玉
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    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems
    • Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration

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

Abstract

The present invention provides heat dynamic co-feeding system, belongs to heat dynamic alliance and technical field of heat pumps.Engine provides power to working machine,Engine provides steam discharge to generator and evaporator,Intermediate extraction is provided to the second generator and heat exchanger,Generator is connected through solution pump and solution heat exchanger with the second generator,Second generator is connected through the second solution heat exchanger with absorber,Absorber is connected through the second solution pump and the second solution heat exchanger with the second absorber,Second absorber is connected through solution heat exchanger with 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 has cooling medium pipeline and ft connection,Absorber,Second 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 heat dynamic (electricity) alliance and technical field of heat pumps.
Background technology：
In making the thermodynamic cycle device of circulatory mediator with vapor, to make engine (steam turbine) that there is inside heat higher Efficiency and its property safe and reliable to operation of increase, then require that the pressure and temperature of engine steam discharge can not be too low；When so in the winter time Section, environment temperature is relatively low, and engine exhaust temperature is higher, then the temperature difference that will have about 40 DEG C of even more highs therebetween can not It is used；Furthermore, in the Steam Power Circulation system with Thermal Power Station as representative, although the grade of steam discharge is very low, its Thermic load also is often enriched very much, if being subject to effectively using then significant.
The dynamic alliance of heat of winter heating is currently used for, also or has a dynamic alliance of heat of other heat supply purposes, corresponding technical side Case is generally comprised：(1) improving engine outlet steam discharge parameter carries 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 3rd class absorption heat pump principle, the temperature difference between engine steam discharge and cold environment is made full use of, and consider Follow thermal energy step and utilize principle, and consider making full use of for the temperature difference between steam source and heated medium, the 3rd class is inhaled Receipts formula heat pump heat supply is combined with engine heating of drawing gas, to meet the heat demand under different situations and realize heat energy utilization Rationalizing --- this can not only realize effective utilization of the temperature difference, and engine blade can be reduced or eliminated in wet-steam region Operation interval, increase engine the inside 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, various specific operating modes such as the thermic load that contains of steam discharge is how many, it is therefore desirable to have various 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. heat moves co-feeding system, 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, the second solution heat exchanger, heat exchanger, engine and Working machine 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 have the finisher that exhaust passage is sequentially communicated generator and evaporator have again condensate liquid pipeline with Ft connection, engine also has the second steam channel to be sequentially communicated the second generator and heat exchanger, and heat exchanger also has second Condensate liquid pipeline and ft connection；Generator also has concentrated solution pipeline to connect through solution pump and solution heat exchanger and the second generator Logical, the second generator also has concentrated solution pipeline to be connected with absorber through the second solution heat exchanger, and absorber also has weak solution pipe Road the second solution pump and the second solution heat exchanger are connected with the second absorber, and the second absorber also has weak solution pipeline through molten Liquid heat exchanger is connected with generator, and the second generator also has refrigerant steam channel to be connected with the second absorber, and generator also has Refrigerant steam channel is connected with condenser, and condenser also has cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump, and evaporator is also There is refrigerant steam channel to be connected with absorber, condenser also has cooling medium pipeline and ft connection, absorber and second absorb Device also has heated medium pipeline and ft connection respectively, and heat exchanger also has heated medium pipeline and ft connection, is formed The dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in the 1st, to cancel evaporator, and engine is had into row The finisher that vapour passage is sequentially communicated generator and evaporator has condensate liquid pipeline to be adjusted to engine with ft connection to have again Generator has condensate liquid pipeline and ft connection again after exhaust passage is connected with generator, and evaporator is had into refrigerant steam channel Connected with absorber and be adjusted to engine and set up exhaust passage to be connected with absorber, condenser is had into cryogen liquid pipeline through cryogen liquid Pump connects with evaporator and is adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
3. heat moves co-feeding system, 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, the second solution heat exchanger, heat exchanger, engine and Working machine is constituted；Engine connects working machine, and engine has live steam passage and ft connection, also engine or exhaust passage With ft connection, generator has condensate liquid pipeline and ft connection again after engine also has exhaust passage to be connected with generator, Engine also has the finisher that the second steam channel is connected with evaporator to have the second condensate liquid pipeline and ft connection, power again Machine also has the 3rd steam channel to be sequentially communicated the second generator and heat exchanger, heat exchanger also have the 3rd condensate liquid pipeline with it is outer Portion connects；Generator also has concentrated solution pipeline to be connected with the second generator through solution pump and solution heat exchanger, the second generator Also concentrated solution pipeline is connected through the second solution heat exchanger with absorber, and absorber also has weak solution pipeline through the second solution pump Connected with the second solution heat exchanger with the second absorber, the second absorber also has weak solution pipeline through solution heat exchanger and hair Raw device connection, the second generator also has refrigerant steam channel to be connected with the second absorber, generator also have refrigerant steam channel and Condenser is connected, and condenser also has cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump, and evaporator also has refrigerant steam channel Connected with absorber, condenser also has cooling medium pipeline and ft connection, absorber and the second absorber also have and added respectively Heat medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in the 3rd, to cancel evaporator, and engine is had into the The finisher that two steam channels are connected with evaporator has the second condensate liquid pipeline and ft connection, the evaporator to have refrigerant vapour again Passage is connected with absorber and is adjusted to have the second steam channel to be connected with absorber in engine in the lump, and condenser is had into cryogen liquid Pipeline connects with evaporator through cryogen liquid pump and is adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
5. heat moves co-feeding system, 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger 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 finisher that passage is sequentially communicated the 3rd generator, generator and evaporator has condensate liquid pipeline and ft connection, power again Machine also has the second steam channel to be sequentially communicated the second generator and heat exchanger, heat exchanger also have the second condensate liquid pipeline with it is outer Portion connects；Generator also has concentrated solution pipeline to be connected with the second generator through solution pump and solution heat exchanger, the second generator Also concentrated solution pipeline is connected through the second solution heat exchanger with absorber, and absorber also has weak solution pipeline through the second solution pump Connected with the second solution heat exchanger with the second absorber, the second absorber also has weak solution pipeline through solution heat exchanger and hair Raw device connection, the second generator also has refrigerant steam channel to be connected with the second absorber, generator also have refrigerant steam channel and 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 hair Raw device connection, the 3rd generator also has concentrated solution pipeline to be connected with the 3rd absorber through the 3rd solution heat exchanger, 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 with evaporator through cryogen liquid pump, steams Hair device also has refrigerant steam channel to be connected with absorber, and condenser and the 3rd absorber also have cooling medium pipeline with outside respectively Connection, absorber and the second absorber also have heated medium pipeline and ft connection respectively, and heat exchanger also has heated Jie Matter pipeline and ft connection, form the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in the 5th, to cancel evaporator, and engine is had into row The finisher that vapour passage is sequentially communicated the 3rd generator, generator and evaporator has condensate liquid pipeline and ft connection to adjust again Generator has condensate liquid pipeline to connect with outside again after having exhaust passage to be sequentially communicated the 3rd generator and generator for engine It is logical, there is refrigerant steam channel to be connected with absorber evaporator and be adjusted to engine and set up exhaust passage to be connected with absorber, general Condenser have cryogen liquid pipeline connected with evaporator through cryogen liquid pump be adjusted to condenser have cryogen liquid pipeline through cryogen liquid pump with Ft connection, forms the dynamic co-feeding system of heat.
7. heat moves co-feeding system, 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger 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 Passage is sequentially communicated generator and the finisher of evaporator connection the second condensate liquid pipeline and ft connection again, and engine is also There is the 3rd steam channel to be sequentially communicated the second generator and heat exchanger, heat exchanger also has the 3rd condensate liquid pipeline to connect with outside It is logical；Generator also has concentrated solution pipeline to be connected with the second generator through solution pump and solution heat exchanger, and the second generator also has Concentrated solution pipeline is connected through the second solution heat exchanger with absorber, and absorber also has weak solution pipeline through the second solution pump and Two solution heat exchangers are connected with the second absorber, and the second absorber also has weak solution pipeline through solution heat exchanger and 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 with the 3rd absorber through the 3rd solution heat exchanger, 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 with evaporator through cryogen liquid pump, evaporator Also refrigerant steam channel is connected with absorber, and condenser and the 3rd absorber also have cooling medium pipeline to connect with outside respectively Logical, absorber and the second 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.
8. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in the 7th, to cancel evaporator, and engine is had into the Two steam channels are sequentially communicated generator and the finisher of evaporator connection has the second condensate liquid pipeline to be adjusted with ft connection again It is whole there is the second steam channel to be connected with generator for engine after generator have the second condensate liquid pipeline and ft connection again, will Evaporator has refrigerant steam channel to be connected with absorber to be adjusted to engine and set up the second steam channel to be connected with absorber, will be cold Condenser have cryogen liquid pipeline connected with evaporator through cryogen liquid pump be adjusted to condenser have cryogen liquid pipeline through cryogen liquid pump with it is outer Portion connects, and forms the dynamic co-feeding system of heat.
9. heat moves co-feeding system, 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger 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 Generator has condensate liquid pipeline and ft connection again after passage is sequentially communicated the 3rd generator and generator, and engine also has The finisher that two steam channels are connected with evaporator has the second condensate liquid pipeline and ft connection again, and engine also has the 3rd steaming Vapour passage is sequentially communicated the second generator and heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection；Occur Device also has concentrated solution pipeline to be connected with the second generator through solution pump and solution heat exchanger, and the second generator also has concentrated solution pipe The solution heat exchanger of road second is connected with absorber, and absorber also has weak solution pipeline through the second solution pump and the second solution heat Exchanger is connected with the second absorber, and the second absorber also has weak solution pipeline to be connected with generator through solution heat exchanger, the Two generators also have refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel to connect with the 3rd absorber Logical, the 3rd absorber also has weak solution pipeline to be connected with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, the Three generators also have concentrated solution pipeline to be connected with the 3rd absorber through the 3rd solution heat exchanger, and the 3rd generator also has cryogen to steam Vapour passage is connected with condenser, and condenser also has cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump, and evaporator also has cryogen Steam channel is connected with absorber, and condenser and the 3rd absorber also have cooling medium pipeline and ft connection, absorber respectively Also there are heated medium pipeline and ft connection respectively with the second absorber, heat exchanger also has heated medium pipeline with outside Connection, forms the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in the 9th, to cancel evaporator, and engine is had into the The finisher that two steam channels are connected with evaporator has the second condensate liquid pipeline and ft connection, the evaporator to have refrigerant vapour again Passage is connected with absorber and is adjusted to have the second steam channel to be connected with absorber in engine in the lump, and condenser is had into cryogen liquid Pipeline connects with evaporator through cryogen liquid pump and is adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
The dynamic co-feeding system of 11. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second 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 has exhaust passage to be sequentially communicated generator, evaporator and the second evaporator is again after the second evaporator There are condensate liquid pipeline and ft connection, engine also has the second steam channel to be sequentially communicated the second generator and heat exchanger, heat Exchanger also has the second condensate liquid pipeline and ft connection；Generator also has concentrated solution pipeline through solution pump and solution heat exchanger Connected with the second generator, the second generator also has concentrated solution pipeline to be connected with absorber through the second solution heat exchanger, absorbed Device also has weak solution pipeline to be connected with the second absorber through the second solution pump and the second solution heat exchanger, and the second absorber also has Weak solution pipeline is connected through solution heat exchanger with generator, and the second generator also has refrigerant steam channel to connect with the second absorber Logical, the 3rd generator has cryogen liquid pipeline cold through second again after generator also has refrigerant steam channel to be connected with the 3rd generator Agent liquid pump 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 also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have respectively Heated medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic alliance system of heat System.
The dynamic co-feeding system of 12. heat, is in the dynamic co-feeding system of heat described in the 11st, to cancel evaporator, and engine is had Exhaust passage is sequentially communicated generator, evaporator and the second evaporator has condensate liquid pipeline and outside to connect again after the second evaporator It is logical to be adjusted to the second evaporator after engine has exhaust passage to be sequentially communicated generator and the second evaporator and have condensate line again Road and ft connection, by evaporator have refrigerant steam channel connected with absorber be adjusted to engine set up exhaust passage with absorb Device is connected, and is had cryogen liquid pipeline to be connected with evaporator through the second cryogen liquid pump in the 3rd generator and is adjusted to the 3rd generator and has cold Agent liquid pipeline forms the dynamic co-feeding system of heat through the second cryogen liquid pump and ft connection.
The dynamic co-feeding system of 13. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second 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, the second evaporator has condensate liquid again after engine also has exhaust passage to be sequentially communicated generator and the second evaporator Pipeline and ft connection, engine also have the finisher that the second steam channel is connected with evaporator to have the second condensate liquid pipeline again With ft connection, engine also has the 3rd steam channel to be sequentially communicated the second generator and heat exchanger, and heat exchanger also has Three condensate liquid pipelines and ft connection；Generator also has concentrated solution pipeline through solution pump and solution heat exchanger and the second generator Connection, the second generator also has concentrated solution pipeline to be connected with absorber through the second solution heat exchanger, and absorber also has weak solution Pipeline is connected through the second solution pump and the second solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline to pass through Solution heat exchanger is connected with generator, and the second generator also has refrigerant steam channel to be connected with the second absorber, and generator is also The 3rd generator has cryogen liquid pipeline through the second cryogen liquid pump and steaming again after having refrigerant steam channel to be connected with the 3rd generator Hair device connection, 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 3rd solution heat exchanger are connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline to be handed over through the 3rd 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 also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated Jie respectively Matter pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, is in the dynamic co-feeding system of heat described in the 13rd, to cancel evaporator, and engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline to have cryogen to steam with ft connection, evaporator again Vapour passage is connected with absorber and is adjusted to engine in the lump and has the second steam channel to be connected with absorber, and the 3rd generator is had into cold Agent liquid pipeline connects with evaporator through the second cryogen liquid pump and is adjusted to the 3rd generator and has cryogen liquid pipeline through the second cryogen liquid pump With ft connection, the dynamic co-feeding system of heat is formed.
The dynamic co-feeding system of 15. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second 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, generator has condensate liquid pipeline and ft connection again after engine also has exhaust passage to be connected with generator, moves The second evaporator has the second condensate line again after power machine also has the second steam channel to be sequentially communicated evaporator and the second evaporator Road and ft connection, engine also have the 3rd steam channel to be sequentially communicated the second generator and heat exchanger, and heat exchanger also has 3rd condensate liquid pipeline and ft connection；Generator also has concentrated solution pipeline to occur through solution pump and solution heat exchanger and second Device is connected, and the second generator also has concentrated solution pipeline to be connected with absorber through the second solution heat exchanger, and absorber also has dilute molten Liquid pipeline is connected through the second solution pump and the second solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline Connected with generator through solution heat exchanger, the second generator also has refrigerant steam channel to be connected with the second absorber, generator Also refrigerant steam channel connected with the 3rd generator after the 3rd generator have again cryogen liquid pipeline through the second cryogen liquid pump with Evaporator is connected, and evaporator also has refrigerant steam channel to be connected with absorber；3rd generator also has concentrated solution pipeline through the 3rd Solution pump and the 3rd solution heat exchanger are connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline through the 3rd solution heat Exchanger 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, Condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also have heated respectively Medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, is in the dynamic co-feeding system of heat described in the 15th, to cancel evaporator, and engine is had The second evaporator has the second condensate liquid pipeline with outside again after second steam channel is sequentially communicated evaporator and the second evaporator Connection is adjusted to the second evaporator after engine has the second steam channel to be connected with the second evaporator 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 through the second cryogen liquid pump in the 3rd generator and is adjusted to the 3rd generator There is cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator, the second cryogen Liquid pump and the 4th generator are constituted；Engine connects working machine, and engine has live steam passage and a ft connection, engine or also The 4th generator has condensation again after having exhaust passage and ft connection, engine to also have exhaust passage to be connected with the 4th generator Liquid pipeline and ft connection, engine also have the second steam channel to be sequentially communicated after generator, evaporator and the second evaporator Second evaporator has the second condensate liquid pipeline and ft connection again, and engine also has the 3rd steam channel to be sequentially communicated the second generation Device and heat exchanger, heat exchanger also have the 3rd condensate liquid pipeline and ft connection；Generator also has concentrated solution pipeline through solution Pump and solution heat exchanger are connected with the second generator, the second generator also have concentrated solution pipeline through the second solution heat exchanger with Absorber is connected, and absorber also has weak solution pipeline to connect through the second solution pump and the second solution heat exchanger and the second absorber Logical, the second absorber also has weak solution pipeline to be connected with generator through solution heat exchanger, and the second generator also has refrigerant vapour Passage is connected with the second absorber, again there is the 3rd generator after generator also has refrigerant steam channel to be connected with the 3rd generator Cryogen liquid pipeline is connected through the second cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber；3rd Generator also has concentrated solution pipeline to be connected with the 4th generator, and the 4th generator also has concentrated solution pipeline through the 3rd solution pump and Three solution heat exchangers are connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline through the 3rd solution heat exchanger and Three generators are connected, and the 3rd generator also has refrigerant steam channel to be connected with condenser, and the 4th generator also has refrigerant vapour to lead to Road is connected with condenser, and condenser also has cryogen liquid pipeline to be connected with the second evaporator through cryogen liquid pump, and the second evaporator also has Refrigerant steam channel is connected with the 3rd absorber, and condenser also has cooling medium pipeline and ft connection, and absorber, second absorb Device and the 3rd absorber also have heated medium pipeline and a ft connection respectively, heat exchanger also have heated medium pipeline with it is outer Portion connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 18. heat, is in the dynamic co-feeding system of heat described in the 17th, to cancel evaporator, and engine is had Second steam channel is sequentially communicated generator, evaporator and the second evaporator has the second condensate liquid pipeline again after the second evaporator The second evaporator after engine has the second steam channel to be sequentially communicated generator and the second evaporator is adjusted to ft connection 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, there is cryogen liquid pipeline to be connected with evaporator through the second cryogen liquid pump in the 3rd generator Being adjusted to the 3rd generator has cryogen liquid pipeline through the second cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump 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 has exhaust passage to be sequentially communicated generator and the finisher of evaporator and has condensate liquid pipeline and ft connection, power again Machine also has the second steam channel to be sequentially communicated the second generator and heat exchanger, heat exchanger also have the second condensate liquid pipeline with it is outer Portion connects；Generator also has concentrated solution pipeline to be connected with the second generator through solution pump and solution heat exchanger, the second generator Also concentrated solution pipeline is connected through the second solution heat exchanger with absorber, and absorber also has weak solution pipeline through the second solution pump Connected with the second solution heat exchanger with the second absorber, the second absorber also has weak solution pipeline through solution heat exchanger and hair Raw device connection, the second generator also has refrigerant steam channel to be connected with the second absorber, generator also have refrigerant steam channel and The 3rd generator has cryogen liquid pipeline to be connected with evaporator through the second cryogen liquid pump again after the connection of 3rd generator；3rd occurs Device also has concentrated solution pipeline to be connected with the 3rd absorber through the 3rd solution pump and the 3rd solution heat exchanger, and the 3rd absorber also has Weak solution pipeline is connected through the 3rd solution heat exchanger with the 3rd generator, and the 3rd generator also has refrigerant steam channel with condensation Device is connected, and condenser also has cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump, and evaporator also has refrigerant steam channel to distinguish Connected with absorber and the 3rd absorber, condenser also has cooling medium pipeline and ft connection, absorber, the second absorber and 3rd absorber also has heated medium pipeline and ft connection respectively, and heat exchanger also has heated medium pipeline to connect with outside It is logical, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, is in the dynamic co-feeding system of heat described in the 19th, to cancel evaporator, and engine is had Exhaust passage is sequentially communicated generator and the finisher of evaporator has condensate liquid pipeline to be adjusted to steam discharge with ft connection again Generator has condensate liquid pipeline and ft connection again after passage is connected with generator, has refrigerant steam channel to distinguish evaporator Connected with absorber and the 3rd absorber and be adjusted to engine and set up exhaust passage to be connected with absorber and the 3rd absorber respectively, There is cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump condenser to be adjusted to condenser and have cryogen liquid pipeline through cryogen liquid pump With ft connection, there is cryogen liquid pipeline to be connected with evaporator through the second cryogen liquid pump in the 3rd generator and be adjusted to the 3rd generator There is cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger and the second cryogen liquid pump are constituted； Engine connects working machine, and engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, moves Generator has condensate liquid pipeline and ft connection again after power machine also has exhaust passage to be connected with generator, and engine also has second The finisher that steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection again, and engine also has the 3rd steam Passage is sequentially communicated the second generator and heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection；Generator Also concentrated solution pipeline is connected through solution pump and solution heat exchanger with the second generator, and the second generator also has concentrated solution pipeline Connected with absorber through the second solution heat exchanger, absorber also has weak solution pipeline to be handed over through the second solution pump and the second solution heat Parallel operation is connected with the second absorber, and the second absorber also has weak solution pipeline to be connected with generator through solution heat exchanger, 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 evaporator through the second cryogen liquid pump again afterwards；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 evaporator, evaporator also have refrigerant steam channel respectively with absorber and the 3rd Absorber is connected, and condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 3rd absorber also divide There are not heated medium pipeline and ft connection, heat exchanger also has heated medium pipeline and ft connection, form the dynamic connection of heat For system.
The dynamic co-feeding system of 22. heat, is in the dynamic co-feeding system of heat described in the 21st, to cancel evaporator, and engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline to have cryogen to steam with ft connection, evaporator again Vapour passage connected with absorber and the 3rd absorber respectively 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 through cryogen liquid pump condenser and be adjusted to condenser and have cryogen 3rd generator is had cryogen liquid pipeline to be connected with evaporator through the second cryogen liquid pump by liquid pipeline through cryogen liquid pump and ft connection Being adjusted to the 3rd generator has cryogen liquid pipeline through the second cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 23. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump and the 4th hair Raw device is constituted；Engine connects working machine, and engine has live steam passage and a ft connection, engine or also exhaust passage with Ft connection, the 4th generator has condensate liquid pipeline with outside again after engine also has exhaust passage to be connected with the 4th generator Connection, engine also has the second steam channel to be sequentially communicated generator and the finisher of evaporator and has the second condensate liquid pipeline again With ft connection, engine also has the 3rd steam channel to be sequentially communicated the second generator and heat exchanger, and heat exchanger also has Three condensate liquid pipelines and ft connection；Generator also has concentrated solution pipeline through solution pump and solution heat exchanger and the second generator Connection, the second generator also has concentrated solution pipeline to be connected with absorber through the second solution heat exchanger, and absorber also has weak solution Pipeline is connected through the second solution pump and the second solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline to pass through Solution heat exchanger is connected with generator, and the second generator also has refrigerant steam channel to be connected with the second absorber, and generator is also The 3rd generator has cryogen liquid pipeline through the second cryogen liquid pump and steaming again after having refrigerant steam channel to be connected with the 3rd generator Hair device connection；3rd generator also has concentrated solution pipeline to be connected with the 4th generator, and the 4th generator also has concentrated solution pipeline to pass through 3rd solution pump and the 3rd solution heat exchanger are connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline molten through the 3rd Liquid heat exchanger is connected with the 3rd generator, and the 3rd generator also has refrigerant steam channel to be connected with condenser, the 4th generator Also refrigerant steam channel is connected with condenser, and condenser also has cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump, evaporation Device also has refrigerant steam channel to be connected with absorber and the 3rd absorber respectively, and condenser also has cooling medium pipeline to connect with outside Logical, absorber, the second absorber and the 3rd absorber also have heated medium pipeline and ft connection respectively, and heat exchanger also has Heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 24. heat, is in the dynamic co-feeding system of heat described in the 23rd, to cancel evaporator, and 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 Generator has the second condensate liquid pipeline and ft connection again after having the second steam channel to be connected with generator for engine, will steam Hair device have refrigerant steam channel connect with absorber and the 3rd absorber respectively be adjusted to engine set up the second steam channel divide Do not connected with absorber and the 3rd absorber, there is cryogen liquid pipeline to be connected with evaporator through the second cryogen liquid pump in the 3rd generator Being adjusted to the 3rd generator has cryogen liquid pipeline through the second cryogen liquid pump and ft connection, and condenser is had into cryogen liquid pipeline through cold Agent liquid pump connects with evaporator and is adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms the dynamic alliance system of heat System.
The dynamic co-feeding system of 25. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th are molten Liquid heat exchanger is constituted；Engine connects working machine, and engine has live steam passage and ft connection, also engine or steam discharge Passage and ft connection, engine also have exhaust passage to be sequentially communicated generator and the finisher of evaporator and have condensate line again Road and ft connection, engine also have the second steam channel to be sequentially communicated the second generator and heat exchanger, and heat exchanger also has Second condensate liquid pipeline and ft connection；Generator also has concentrated solution pipeline through solution pump, solution heat exchanger and the second solution Heat exchanger is connected with the second generator, and the second generator also has concentrated solution pipeline to connect through the second solution heat exchanger and absorber Logical, absorber also has weak solution pipeline to be connected with the second absorber through the second solution pump and the 3rd solution heat exchanger, and second inhales Receiving device also has weak solution pipeline to be connected with the 3rd absorber through the 3rd solution heat exchanger, and the 3rd absorber also has weak solution pipeline Connected with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger, the 4th absorber also has weak solution pipeline through the 4th Solution heat exchanger and solution heat exchanger are connected with generator, and the second generator also has refrigerant steam channel and the second absorber Connection, generator also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and evaporation Device is connected, and evaporator also has refrigerant steam channel to be connected with absorber and the 3rd absorber respectively, and condenser also has cryogen liquid pipe The 3rd absorber has refrigerant steam channel to connect with the 4th absorber again after road the second cryogen liquid pump is connected with the 3rd absorber Logical, condenser also has cooling medium pipeline and ft connection, and absorber, the second absorber and the 4th absorber also have and added respectively Heat medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, is in the dynamic co-feeding system of heat described in the 25th, to cancel evaporator, and engine is had Exhaust passage is sequentially communicated generator and the finisher of evaporator has condensate liquid pipeline to be adjusted to engine with ft connection again Generator has condensate liquid pipeline and ft connection again after having exhaust passage to be connected with generator, has refrigerant vapour to lead to evaporator Road connected with absorber and the 3rd absorber respectively be adjusted to engine set up exhaust passage respectively with absorber and the 3rd absorption Device is connected, and is had cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump condenser and is adjusted to condenser and has cryogen liquid pipeline through cold Agent liquid pump and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 27. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th are molten Liquid heat exchanger is constituted；Engine connects working machine, and engine has live steam passage and ft connection, also engine or steam discharge Passage and ft connection, generator has condensate liquid pipeline to connect with outside again after engine also has exhaust passage to be connected with generator Logical, engine also has the finisher that the second steam channel is connected with evaporator to have the second condensate liquid pipeline and ft connection again, Engine also has the 3rd steam channel to be sequentially communicated the second generator and heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline With ft connection；Generator also has concentrated solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger and second Generator is connected, and the second generator also has concentrated solution pipeline to be connected with absorber through the second solution heat exchanger, and absorber also has Weak solution pipeline is connected through the second solution pump and the 3rd solution heat exchanger with the second absorber, and the second absorber also has weak solution Pipeline is connected through the 3rd solution heat exchanger with the 3rd absorber, the 3rd absorber also have weak solution pipeline through the 3rd solution pump and 4th solution heat exchanger is connected with the 4th absorber, the 4th absorber also have weak solution pipeline through the 4th solution heat exchanger and Solution heat exchanger is connected with generator, and the second generator also has refrigerant steam channel to be connected with the second absorber, and generator is also There is refrigerant steam channel to be connected with condenser, condenser also has cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump, evaporator Also refrigerant steam channel is connected with absorber and the 3rd absorber respectively, and condenser also has cryogen liquid pipeline through the second cryogen liquid The 3rd absorber has refrigerant steam channel to be connected with the 4th absorber again after pump is connected with the 3rd absorber, and condenser is also cold But medium pipeline and ft connection, absorber, the second absorber and the 4th absorber also have respectively heated medium pipeline with it is outer Portion connects, and heat exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 28. heat, is in the dynamic co-feeding system of heat described in the 27th, to cancel evaporator, and engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline to have cryogen to steam with ft connection, evaporator again Vapour passage connected with absorber and the 3rd absorber respectively 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 through cryogen liquid pump condenser and be adjusted to condenser and have cryogen Liquid pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump and ft connection.
The dynamic co-feeding system of 29. 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, the second solution heat exchanger, heat exchanger, engine, Working machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator, the second cryogen liquid pump, the 4th inhale Device, the 4th solution heat exchanger and the 3rd cryogen liquid pump is received to be constituted；Engine connect working machine, engine have live steam passage with Ft connection, also engine or exhaust passage and ft connection, engine also have exhaust passage to be sequentially communicated generator and The second evaporator has condensate liquid pipeline and ft connection again after two evaporators, and engine also has the second steam channel and evaporator The finisher of connection has the second condensate liquid pipeline and ft connection again, and engine also has the 3rd steam channel to be sequentially communicated second Generator and heat exchanger, heat exchanger also have the 3rd condensate liquid pipeline and ft connection；Generator also has concentrated solution pipeline to pass through Solution pump, solution heat exchanger and the second solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipe The solution heat exchanger of road second is connected with absorber, and absorber also has weak solution pipeline through the second solution pump and the 3rd solution heat Exchanger is connected with the second absorber, and the second absorber also has weak solution pipeline through the 3rd solution heat exchanger and the 3rd absorber Connection, the 3rd absorber also has weak solution pipeline to be connected with the 4th absorber through the 3rd solution pump and the 4th solution heat exchanger, 4th absorber also has weak solution pipeline to be connected with generator through the 4th solution heat exchanger and solution heat exchanger, and second occurs Device also has refrigerant steam channel to be connected with the second absorber, and generator also has refrigerant steam channel to be connected with condenser, condenser Also cryogen liquid pipeline is connected through cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber, condensation The 3rd absorber has refrigerant steam channel again after device also has cryogen liquid pipeline to be connected with the 3rd absorber through the second cryogen liquid pump Connected with the 4th absorber, condenser also has cryogen liquid pipeline to be connected with the second evaporator through the 3rd cryogen liquid pump, the second evaporation Device also has refrigerant steam channel to be connected with the 3rd absorber, and condenser also has cooling medium pipeline and ft connection, absorber, Two absorbers and the 4th absorber also have heated medium pipeline and ft connection respectively, and heat exchanger also has heated medium pipe Road and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, is in the dynamic co-feeding system of heat described in the 29th, to cancel evaporator and the second evaporation Device, by engine have the finisher that the second steam channel is connected with evaporator have again the second condensate liquid pipeline and ft connection, Evaporator has refrigerant steam channel to be connected with absorber to be adjusted to engine in the lump and have the second steam channel to be connected with absorber, will The second evaporator has cryogen liquid pipeline with outside again after engine has exhaust passage to be sequentially communicated generator and the second evaporator Connection is adjusted to generator after engine has exhaust passage to be connected with generator and has cryogen liquid pipeline and ft connection again, by the Two evaporators have refrigerant steam channel to be connected with the 3rd absorber to be adjusted to engine and set up exhaust passage and the 3rd absorber to connect It is logical, there is cryogen liquid pipeline to be connected with evaporator through cryogen liquid pump condenser and be adjusted to condenser and have cryogen liquid pipeline through cryogen liquid Pump and ft connection, have cryogen liquid pipeline to be connected with the second evaporator through the 3rd cryogen liquid pump condenser and are adjusted to condenser and have Cryogen liquid pipeline forms the dynamic co-feeding system of heat through the 3rd cryogen liquid pump and ft connection.
The dynamic co-feeding system of 31. heat, is in the dynamic alliance system of any hot described in 1-2,5-6,11-12,19-20,25-26 In system, cancel heat exchanger, the heated medium pipeline that is connected with heat exchanger of cancellation, by engine have the second steam channel according to The second generator of secondary connection and heat exchanger, heat exchanger have the second condensate liquid pipeline and ft connection to be adjusted to engine in the lump The second generator has the second condensate liquid pipeline and ft connection again after having the second steam channel to be connected with the second generator, is formed The dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, is in the dynamic alliance of any hot described in 3-4,7-10,13-18,21-24,27-29 In system, cancel heat exchanger, engine is had the 3rd steam channel by the heated medium pipeline that cancellation is connected with heat exchanger Being sequentially communicated the second generator and heat exchanger, heat exchanger has the 3rd condensate liquid pipeline and ft connection to be adjusted to power in the lump The second generator has the 3rd condensate liquid pipeline and ft connection, shape again after machine has the 3rd steam channel to be connected with the second generator Into the dynamic co-feeding system of heat.
The features of the present invention and essence are further illustrated with reference to the dynamic co-feeding system of heat shown in Fig. 4 and Fig. 8：
(1) when between steam discharge and cold environment the temperature difference it is smaller, and exhaust steam flow it is larger when, using the dynamic alliance system of heat shown in Fig. 4 The rising of part steam discharge heat quality is realized in system, classification.
(2) when between steam discharge and cold environment the temperature difference it is larger, cold ambient temperature is relatively low, using single solution be difficult to fully realization When the temperature difference is utilized, using the dynamic co-feeding system of heat shown in Fig. 8, branch realizes that making full use of for part steam discharge heat energy is (economic benefits and social benefits) and another The rising of part steam discharge heat quality.
To the heat release of the second absorber 4, the external heat supply of the second absorber 4, is to the second steam and quilt to (3) second generators 2 The utilization of the temperature difference between heating medium, is conducive to improving the utilization ratio of high-grade heat energy.
(4) in practical application, install flow control valve additional in the second steam channel, and change the heat of heat exchanger 12 and bear Lotus --- such as reduce the heated medium flow for flowing through heat exchanger 12, the need for actual condition change and energy-conservation can be met.
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.
In figure, 1- generators, the generators of 2- second, 3- absorbers, the absorbers of 4- second, 5- condensers, 6- evaporators, 7- Solution pump, 8- the second solution pumps, 9- cryogen liquid pumps, 10- solution heat exchangers, the solution heat exchangers of 11- second, 12- heat exchanges Device, 13- engines, 14- working machines, the generators of 15- the 3rd, the absorbers of 16- the 3rd, the solution pumps of 17- the 3rd, the solution of 18- the 3rd Heat exchanger, the evaporators of 19- second, 20- the second cryogen liquid pumps, the generators of 21- the 4th, the absorbers of 22- the 4th, 23- the 4th is molten Liquid heat exchanger, the cryogen liquid pumps of 24- the 3rd.
Here following explanation is also given：
(1) steam discharge --- refer to engine export medium, such as low-pressure steam in steam turbine outlet moist steam.
(2) second steam --- engine-position is extracted out, pressure and temperature is above the working media of steam discharge.
The work that (3) the 3rd steam --- engine-position is extracted out, pressure and temperature is above the second steam is situated between Matter.
(4) it is relevant with engine, but it is not related to the operation principle of the present invention part unrelated with present invention (such as power Output block etc.) and flow (such as dynamical system backheat flow), not in express ranges of the present invention.
(5) it is molten by the 3rd generator 15, the 3rd absorber 16, condenser 5, the second evaporator the 19, the 3rd by taking Fig. 8 as an example The circulation of liquid pump 17, cryogen liquid pump 9 and the 3rd solution heat exchanger 18 composition, when making working medium with ammonia-water solution, the 3rd generator By custom, referred to as rectifying column --- now as needed, the 3rd generator 15 sets up cooling medium pipeline and ft connection.
Specific 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.Below in conjunction with the accompanying drawings the present invention is described in detail with example.
What the dynamic co-feeding system of heat shown in Fig. 1 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, the second solution heat exchanger, heat exchanger, engine and work Make machine to be constituted；Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has steam discharge Passage and ft connection, engine 13 also have exhaust passage to be sequentially communicated generator 1 and the finisher 6 of evaporator 6 and have cold again Lime set pipeline and ft connection, engine 13 also have the second steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, heat Exchanger 12 also has the second condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipeline to be handed over through solution pump 7 and solution heat Parallel operation 10 is connected with the second generator 2, and the second generator 2 also has concentrated solution pipeline through the second solution heat exchanger 11 and absorber 3 connections, absorber 3 also has weak solution pipeline to connect with the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11 Logical, the second absorber 4 also has weak solution pipeline to be connected with generator 1 through solution heat exchanger 10, and the second generator 2 also has cryogen Steam channel is connected with the second absorber 4, and generator 1 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 evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3, condenser 5 Also cooling medium pipeline and ft connection, the absorber 4 of absorber 3 and second also have heated medium pipeline to connect with outside respectively Logical, 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 engine 13 is to the second generator 2 and heat exchanger 12 There is provided the second steam, the second steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through second after condensate liquid Lime set pipeline is discharged, and engine 13 provides steam discharge to generator 1 and evaporator 6, and steam discharge flows through generator 1 and evaporator 6, progressively Heat release is discharged into condensed liquid pipeline after condensate liquid；The concentrated solution of generator 1 enters through solution pump 7 and solution heat exchanger 10 Second generator 2, heat absorption release refrigerant vapour are simultaneously provided to the second absorber 4, and the concentrated solution of the second generator 2 is through the second 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 molten through second 8 and second solution heat exchanger of liquid pump 11 enters the second absorber 4, absorbs refrigerant vapour and heat release is in heated medium, and second The weak solution of absorber 4 enter after being depressured through solution heat exchanger 10 and pipeline generator 1, heat absorption release refrigerant vapour and to Condenser 5 is provided；In cooling medium into cryogen liquid, the cryogen liquid of condenser 5 is through cryogen liquid pump for the refrigerant vapour heat release of condenser 5 9 pressurize into evaporator 6, absorb heat into refrigerant vapour and provided to absorber 3, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 2 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, the second solution heat exchanger, heat exchanger, engine and work Make machine to be constituted；Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has steam discharge Generator 1 has condensate liquid pipeline and ft connection again after passage is connected with generator 1, and engine 13 also has the second steam channel The finisher 6 connected with evaporator 6 has the second condensate liquid pipeline and ft connection again, and engine 13 also has the 3rd steam channel The second generator 2 and heat exchanger 12 are sequentially communicated, heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipeline to be connected with the second generator 2 through solution pump 7 and solution heat exchanger 10, and the second generator 2 also has dense molten Liquid pipeline is connected through the second solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipeline through the He of the second solution pump 8 Second solution heat exchanger 11 is connected with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution heat exchanger 10 Connected with generator 1, 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 Vapour passage is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected with evaporator 6 through cryogen liquid pump 9, and evaporator 6 also has Refrigerant steam channel is connected with absorber 3, and condenser 5 also has cooling medium pipeline and ft connection, and absorber 3 and second absorbs Device 4 also has heated medium pipeline and ft connection respectively, and 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 Fig. 1, main difference part is：Engine 13 is to the second hair Raw device 2 and heat exchanger 12 provide the 3rd steam, the 3rd steam flow through the second generator 2 and heat exchanger 12, progressively heat release into Discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 13 provides the second steam to evaporator 6, and the second steam is in evaporator Heat release is discharged into after condensate liquid through the second condensate liquid pipeline in 6, and engine 13 only provides steam discharge to generator 1.
What the dynamic co-feeding system of heat shown in Fig. 3 was realized in：
In the dynamic co-feeding system of heat shown in Fig. 2, cancel evaporator, engine 13 is had into the second steam channel and evaporator The finisher 6 of 6 connections has the second condensate liquid pipeline to have refrigerant steam channel and absorber 3 to connect with ft connection, evaporator 6 again It is logical to be adjusted to there is the second steam channel to be connected with absorber 3 in engine 13 in the lump, condenser 5 there is into cryogen liquid pipeline through cryogen Liquid pump 9 connects with evaporator 6 and is adjusted to condenser 5 and has cryogen liquid pipeline through cryogen liquid pump 9 and ft connection, forms the dynamic alliance of heat System.
What the dynamic co-feeding system of heat shown in Fig. 4 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted；Engine 13 connects work Machine 14, the finisher 6 that the also exhaust passage of engine 13 is sequentially communicated the 3rd generator 15, generator 1 and evaporator 6 has again Condensate liquid pipeline and ft connection, engine 13 also have the second steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, Heat exchanger 12 also has the second condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipeline through solution pump 7 and solution heat Exchanger 10 is connected with the second generator 2, and the second generator 2 also has concentrated solution pipeline through the second solution heat exchanger 11 and absorption Device 3 is connected, and absorber 3 also has weak solution pipeline to connect with the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11 Logical, the second absorber 4 also has weak solution pipeline to be connected with generator 1 through solution heat exchanger 10, and the second generator 2 also has cryogen Steam channel is connected with the second absorber 4, and generator 1 also has refrigerant steam channel to be connected with the 3rd absorber 16, and the 3rd absorbs Device 16 also has weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, the 3rd hair Raw device 15 also has concentrated solution pipeline to be connected with the 3rd absorber 16 through the 3rd solution heat exchanger 18, and the 3rd generator 15 is also cold Agent steam channel is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected with evaporator 6 through cryogen liquid pump 9, evaporator 6 Also refrigerant steam channel is connected with absorber 3, and the absorber 16 of condenser 5 and the 3rd also has cooling medium pipeline with outside respectively Connection, the absorber 4 of absorber 3 and second also has heated medium pipeline and ft connection respectively, and heat exchanger 12 is also added Heat medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and engine 13 is to the second generator 2 and heat exchanger 12 There is provided the second steam, the second steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through second after condensate liquid Lime set pipeline is discharged, and engine 13 provides steam discharge, part or all of exhaust stream to the 3rd generator 15, generator 1 and evaporator 6 Through the 3rd generator 15, generator 1 and evaporator 6, progressively heat release is discharged into condensed liquid pipeline after condensate liquid；Generator 1 Concentrated solution enters the second generator 2, heat absorption and discharges refrigerant vapour and to the second absorber through solution pump 7 and solution heat exchanger 10 4 provide, the concentrated solution of the second generator 2 enter absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour and heat release in Heated medium, the weak solution of absorber 3 enters the second absorber 4, inhales through the second solution pump 8 and the second solution heat exchanger 11 Refrigerant vapour and heat release are received in heated medium, the weak solution of the second absorber 4 through solution heat exchanger 10 enter generator 1, Heat absorption release refrigerant vapour is simultaneously provided to the 3rd absorber 16；The weak solution of the 3rd absorber 16 is through the 3rd solution pump 17 and the 3rd Solution heat exchanger 18 discharges refrigerant vapour and is provided to condenser 5 into the 3rd generator 15, heat absorption, the 3rd generator 15 Concentrated solution enters the 3rd absorber 16 through the 3rd solution heat exchanger 18, absorbs refrigerant vapour and heat release is in cooling medium；Condensation The refrigerant vapour heat release of device 5 enters evaporator in cooling medium into cryogen liquid, the cryogen liquid of condenser 5 through the pressurization of cryogen liquid pump 9 6th, absorb heat into refrigerant vapour and provided to absorber 3, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 5 was realized in：
In the dynamic co-feeding system of heat shown in Fig. 4, cancel evaporator, there is exhaust passage to be sequentially communicated the 3rd in engine 13 The finisher 6 of generator 15, generator 1 and evaporator 6 has condensate liquid pipeline and ft connection to be adjusted to engine 13 and has again Generator 1 has condensate liquid pipeline and ft connection again after exhaust passage is sequentially communicated the 3rd generator 15 and generator 1, will steam Hair device 6 has refrigerant steam channel to be connected with absorber 3 to be adjusted to engine 13 and set up exhaust passage to be connected with absorber 3, will be cold Condenser 5 has cryogen liquid pipeline to be connected with evaporator 6 through cryogen liquid pump 9 to be adjusted to condenser 5 and have cryogen liquid pipeline through cryogen liquid pump 9 With ft connection, the dynamic co-feeding system of heat is formed.
What the dynamic co-feeding system of heat shown in Fig. 6 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd generator, the 3rd absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted；Engine 13 connects work Machine 14, after engine 13 has live steam passage and ft connection, engine 13 to also have exhaust passage to be connected with the 3rd generator 15 3rd generator 15 has condensate liquid pipeline and ft connection again, and engine 13 also has the second steam channel to be sequentially communicated generator 1 The finisher 6 connected with evaporator 6 has the second condensate liquid pipeline and ft connection again, and engine 13 also has the 3rd steam channel The second generator 2 and heat exchanger 12 are sequentially communicated, heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipeline to be connected with the second generator 2 through solution pump 7 and solution heat exchanger 10, and the second generator 2 also has dense molten Liquid pipeline is connected through the second solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipeline through the He of the second solution pump 8 Second solution heat exchanger 11 is connected with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution heat exchanger 10 Connected with generator 1, 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 Vapour passage is connected with the 3rd absorber 16, and the 3rd absorber 16 also has weak solution pipeline through the 3rd solution pump 17 and the 3rd solution heat Exchanger 18 is connected with the 3rd generator 15, and the 3rd generator 15 also has concentrated solution pipeline through the 3rd solution heat exchanger 18 and the Three absorbers 16 are connected, and the 3rd generator 15 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipe Road connects through cryogen liquid pump 9 with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3, condenser 5 and the 3rd Absorber 16 also has cooling medium pipeline and ft connection respectively, and the absorber 4 of absorber 3 and second also has heated medium respectively Pipeline and ft connection, heat exchanger 12 also have heated medium pipeline and ft connection.
(2) in flow, compared with the dynamic co-feeding system of heat shown in Fig. 4, difference is：Engine 13 is to the second generator 2 and heat exchanger 12 the 3rd steam is provided, the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into condensation Discharged through the 3rd condensate liquid pipeline after liquid, engine 13 provides the second steam, the second steam stream to generator 1 and evaporator 6 Through generator 1 and evaporator 6, progressively heat release into being discharged through the second condensate liquid pipeline after condensate liquid, engine 13 is only to the 3rd Generator 15 provides steam discharge, and part or all of steam discharge flows through the 3rd generator 15, heat release into condensed liquid pipeline after condensate liquid Discharge.
What the dynamic co-feeding system of heat shown in Fig. 7 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 15 Generator 1 has condensate liquid pipeline and ft connection again after generator 1, and engine 13 also has 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 also has the 3rd steam channel to be sequentially communicated Second generator 2 and heat exchanger 12, heat exchanger 12 also have the 3rd condensate liquid pipeline and ft connection；Generator 1 is also dense Solution line is connected through solution pump 7 and solution heat exchanger 10 with the second generator 2, and the second generator 2 also has concentrated solution pipeline Connected with absorber 3 through the second solution heat exchanger 11, absorber 3 also has weak solution pipeline molten through the second solution pump 8 and second Liquid heat exchanger 11 is connected with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution heat exchanger 10 and generation Device 1 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 steam channel Connected with the 3rd absorber 16, the 3rd absorber 16 also has weak solution pipeline through the 3rd solution pump 17 and the 3rd solution heat exchanger 18 connect with the 3rd generator 15, and the 3rd generator 15 also has concentrated solution pipeline to be absorbed through the 3rd solution heat exchanger 18 and the 3rd Device 16 is connected, and the 3rd generator 15 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipeline through cold Agent liquid pump 9 is connected with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3, the absorber of condenser 5 and the 3rd 16 also have cooling medium pipeline and a ft connection respectively, the absorber 4 of absorber 3 and second 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 Fig. 4, difference is：Engine 13 is to the second generator 2 and heat exchanger 12 the 3rd steam is provided, the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into condensation Discharged through the 3rd condensate liquid pipeline after liquid, engine 13 provides the second steam to evaporator 6, and the second steam is in evaporator 6 Heat release is discharged into after condensate liquid through the second condensate liquid pipeline, and engine 13 provides steam discharge to the 3rd generator 15 and generator 1, Part or all of steam discharge flow through the 3rd generator 15 with generator 1, progressively heat release discharged into condensed liquid pipeline after condensate liquid.
What the dynamic co-feeding system of heat shown in Fig. 8 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 evaporator 19 has condensate liquid pipeline and outside to connect again after being sequentially communicated generator 1, the evaporator 19 of evaporator 6 and second Logical, engine 13 also has the second steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, and heat exchanger 12 also has second Condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipeline to occur through solution pump 7 and solution heat exchanger 10 and second Device 2 is connected, and the second generator 2 also has concentrated solution pipeline to be connected with absorber 3 through the second solution heat exchanger 11, and absorber 3 is also There is weak solution pipeline to be connected with the second absorber 4 through the second solution pump 8 and the second solution heat exchanger 11, the second absorber 4 is also There is weak solution pipeline to be connected with generator 1 through solution heat exchanger 10, the second generator 2 also has refrigerant steam channel to be inhaled with second Receive device 4 to connect, the 3rd generator 15 has cryogen liquid again after generator 1 also has refrigerant steam channel to be connected with the 3rd generator 15 Pipeline is connected through the second cryogen liquid pump 20 with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3；3rd hair Raw device 15 also has concentrated solution pipeline to be connected with the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, and the 3rd Absorber 16 also has weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution heat exchanger 18, and the 3rd generator 15 also has Refrigerant steam channel is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected with the second evaporator 19 through cryogen liquid pump 9, Second evaporator 19 also has refrigerant steam channel to be connected with the 3rd absorber 16, and condenser 5 also has cooling medium pipeline with outside Connection, absorber 3, the second absorber 4 and the 3rd absorber 16 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 engine 13 is to the second generator 2 and heat exchanger 12 There is provided the second steam, the second steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through second after condensate liquid Lime set pipeline is discharged, and engine 13 provides steam discharge to generator 1 and evaporator 6, and part or all of steam discharge flows through generator 1 and steams Hair device 6, progressively heat release are discharged into condensed liquid pipeline after condensate liquid；The concentrated solution of generator 1 is handed over through solution pump 7 and solution heat Parallel operation 10 discharges refrigerant vapour and is provided to the second absorber 4, the concentrated solution of the second generator 2 into the second generator 2, heat absorption Enter absorber 3 through the second solution heat exchanger 11, absorb refrigerant vapour and heat release in heated medium, absorber 3 it is dilute molten Liquid enters the second absorber 4, absorbs refrigerant vapour through the second solution pump 8 and the second solution heat exchanger 11 and heat release is in heated Medium, the weak solution of the second absorber 4 is through solution heat exchanger 10 is into generator 1, heat absorption release refrigerant vapour and is supplied to 3rd generator 15 makees driving thermal medium；The concentrated solution of the 3rd generator 15 is through the 3rd solution pump 17 and the 3rd solution heat exchanger 18 enter the 3rd absorber 16, absorption refrigerant vapour and heat release in heated medium, and the weak solution of the 3rd absorber 16 is through the 3rd Solution heat exchanger 18 enters the 3rd generator 15, and refrigerant vapour flows through the 3rd generator 15, heating and released into the solution in it Put and provide refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 in cooling medium into cryogen liquid, condenser 5 it is cold Agent liquid pressurizes into the second evaporator 19 through cryogen liquid pump 9, absorbs heat into refrigerant vapour and provided to the 3rd absorber 16, flows through The refrigerant vapour heat release of three generators 15 into after cryogen liquid through the second cryogen liquid pump 20 pressurize into evaporator 6, absorb heat into it is cold Agent steam is simultaneously provided to absorber 3, forms the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 9 was realized in：
In the dynamic co-feeding system of heat shown in Fig. 8, cancel evaporator, there is exhaust passage to be sequentially communicated generation in engine 13 Second evaporator 19 has condensate liquid pipeline and ft connection to be adjusted to engine again after device 1, the evaporator 19 of evaporator 6 and second 13 have exhaust passage to be sequentially communicated the evaporator 19 of generator 1 and second, and the second evaporator 19 has condensate liquid pipeline with outside again afterwards Connection, has refrigerant steam channel to be connected with absorber 3 evaporator 6 and is adjusted to engine 13 and sets up exhaust passage and absorber 3 Connection, has cryogen liquid pipeline to be connected with evaporator 6 through the second cryogen liquid pump 20 in the 3rd generator 15 and is adjusted to the 3rd generator 15 have cryogen liquid pipeline through the second cryogen liquid pump 20 and ft connection, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 10 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 evaporator 19 has condensate liquid pipeline and ft connection, engine again after being sequentially communicated the evaporator 19 of generator 1 and second 13 finishers 6 that also the second steam channel is connected with evaporator 6 have the second condensate liquid pipeline and ft connection, engine again 13 also have the 3rd steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, and heat exchanger 12 also has the 3rd condensate line Road and ft connection；Generator 1 also has concentrated solution pipeline to be connected with the second generator 2 through solution pump 7 and solution heat exchanger 10, Second generator 2 also has concentrated solution pipeline to be connected with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has weak solution Pipeline is connected through the second solution pump 8 and the second solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution Pipeline is connected through solution heat exchanger 10 with generator 1, and the second generator 2 also has refrigerant steam channel to connect with the second absorber 4 Logical, the 3rd generator 15 has cryogen liquid pipeline to pass through again after generator 1 also has refrigerant steam channel to be connected with the 3rd generator 15 Second cryogen liquid pump 20 is connected with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3；3rd generator 15 Also concentrated solution pipeline is connected through the 3rd solution pump 17 and the 3rd solution heat exchanger 18 with the 3rd absorber 16, the 3rd absorber 16 also have weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution heat exchanger 18, and the 3rd generator 15 also has cryogen to steam Vapour passage is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected with the second evaporator 19 through cryogen liquid pump 9, and second steams Hair device 19 also has refrigerant steam channel to be connected with the 3rd absorber 16, and condenser 5 also has cooling medium pipeline and ft connection, inhales Receive device 3, the second absorber 4 and the 3rd absorber 16 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, compared with the dynamic co-feeding system of heat shown in Fig. 8, difference is：Engine 13 is to the second generator 2 and heat exchanger 12 the 3rd steam is provided, the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into condensation Discharged through the 3rd condensate liquid pipeline after liquid, engine 13 provides the second steam to evaporator 6, and the second steam is in evaporator 6 Heat release is discharged into after condensate liquid through the second condensate liquid pipeline, and engine 13 provides steam discharge to 1 and second evaporator of generator 19, Part or all of steam discharge flow through generator 1 with the second evaporator 19, progressively heat release discharged into condensed liquid pipeline after condensate liquid.
What the dynamic co-feeding system of heat shown in Figure 11 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 Generator 1 has condensate liquid pipeline and ft connection again after being connected with generator 1, and engine 13 also has the second steam channel successively Second evaporator 19 has the second condensate liquid pipeline and ft connection, engine again after the evaporator 19 of connection evaporator 6 and second 13 also have the 3rd steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, and heat exchanger 12 also has the 3rd condensate line Road and ft connection；Generator 1 also has concentrated solution pipeline to be connected with the second generator 2 through solution pump 7 and solution heat exchanger 10, Second generator 2 also has concentrated solution pipeline to be connected with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has weak solution Pipeline is connected through the second solution pump 8 and the second solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution Pipeline is connected through solution heat exchanger 10 with generator 1, and the second generator 2 also has refrigerant steam channel to connect with the second absorber 4 Logical, the 3rd generator 15 has cryogen liquid pipeline to pass through again after generator 1 also has refrigerant steam channel to be connected with the 3rd generator 15 Second cryogen liquid pump 20 is connected with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3；3rd generator 15 Also concentrated solution pipeline is connected through the 3rd solution pump 17 and the 3rd solution heat exchanger 18 with the 3rd absorber 16, the 3rd absorber 16 also have weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution heat exchanger 18, and the 3rd generator 15 also has cryogen to steam Vapour passage is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected with the second evaporator 19 through cryogen liquid pump 9, and second steams Hair device 19 also has refrigerant steam channel to be connected with the 3rd absorber 16, and condenser 5 also has cooling medium pipeline and ft connection, inhales Receive device 3, the second absorber 4 and the 3rd absorber 16 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, compared with the dynamic co-feeding system of heat shown in Fig. 8, difference is：Engine 13 is to the second generator 2 and heat exchanger 12 the 3rd steam is provided, the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into condensation Discharged through the 3rd condensate liquid pipeline after liquid, engine 13 provides the second steam to 6 and second evaporator of evaporator 19, second steams Steam flow is through evaporator 6 and the second evaporator 19, progressively heat release is through the second condensate liquid pipeline into discharging after condensate liquid, engine 13 Steam discharge is provided to generator 1, part or all of steam discharge flows through generator 1, heat release into condensed liquid pipeline discharge after condensate liquid.
What the dynamic co-feeding system of heat shown in Figure 12 was realized in：
In the dynamic co-feeding system of heat shown in Figure 11, cancel evaporator, there is the second steam channel to connect successively in engine 13 Second evaporator 19 has the second condensate liquid pipeline to be adjusted to power with ft connection again after the evaporator 19 of logical evaporator 6 and second Second evaporator 19 has the second condensate liquid pipeline with outside again after machine 13 has the second steam channel to be connected with the second evaporator 19 Connection, by evaporator 6 have refrigerant steam channel connect with absorber 3 be adjusted to engine 13 set up the second steam channel and absorption Device 3 is connected, and is had cryogen liquid pipeline to be connected with evaporator 6 through the second cryogen liquid pump 20 in the 3rd generator 15 and is adjusted to the 3rd generation Device 15 has cryogen liquid pipeline through the second cryogen liquid pump 20 and ft connection, forms the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 13 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator, the second cryogen liquid pump Constituted with the 4th generator；Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, engine 13 The 4th generator 21 has condensate liquid pipeline and ft connection again after also exhaust passage is connected with the 4th generator 21, engine 13 also have the second steam channels to be sequentially communicated the second evaporator 19 after generator 1, the evaporator 19 of evaporator 6 and second the again Two condensate liquid pipelines and ft connection, engine 13 also have the 3rd steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipeline through solution pump 7 and molten Liquid heat exchanger 10 is connected with the second generator 2, the second generator 2 also have concentrated solution pipeline through the second solution heat exchanger 11 with Absorber 3 is connected, and absorber 3 also has weak solution pipeline to be absorbed through the second solution pump 8 and the second solution heat exchanger 11 and second Device 4 is connected, and the second absorber 4 also has weak solution pipeline to be connected with generator 1 through solution heat exchanger 10, and the second generator 2 is also There is refrigerant steam channel to be connected with the second absorber 4, after generator 1 also has refrigerant steam channel to be connected with the 3rd generator 15 3rd generator 15 has cryogen liquid pipeline to be connected with evaporator 6 through the second cryogen liquid pump 20 again, and evaporator 6 also has refrigerant vapour to lead to Road is connected with absorber 3；3rd generator 15 also has concentrated solution pipeline to be connected with the 4th generator 21, and the 4th generator 21 also has Concentrated solution pipeline is connected through the 3rd solution pump 17 and the 3rd solution heat exchanger 18 with the 3rd absorber 16, and the 3rd absorber 16 is also There is weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution heat exchanger 18, the 3rd generator 15 also has refrigerant vapour to lead to Road is connected with condenser 5, and the 4th generator 21 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipe Road connects through cryogen liquid pump 9 with the second evaporator 19, and the second evaporator 19 also has refrigerant steam channel to connect with the 3rd absorber 16 Logical, condenser 5 also has cooling medium pipeline and ft connection, and absorber 3, the second absorber 4 and the 3rd absorber 16 are also distinguished There are heated medium pipeline and 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 engine 13 is to the second generator 2 and heat exchanger 12 There is provided the 3rd steam, the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through the 3rd after condensate liquid Lime set pipeline is discharged, and engine 13 provides the second steam to generator 1,6 and second evaporator of evaporator 19, and the second steam is flowed through Progressively heat release is discharged into after condensate liquid through the second condensate liquid pipeline for generator 1, evaporator 6 and the second evaporator 19, engine 13 provide steam discharge to the 4th generator 21, part or all of steam discharge flow through the 4th generator 21, heat release into after condensate liquid through cold Lime set pipeline is discharged；The concentrated solution of generator 1 enters the second generator 2, heat absorption release through solution pump 7 and solution heat exchanger 10 Refrigerant vapour is simultaneously provided to the second absorber 4, and the concentrated solution of the second generator 2 enters absorber through the second solution heat exchanger 11 3rd, absorb refrigerant vapour and heat release is in heated medium, the weak solution of absorber 3 is through the second solution pump 8 and the second solution heat exchange Device 11 enters the second absorber 4, absorbs refrigerant vapour and heat release is in heated medium, and the weak solution of the second absorber 4 is through solution Heat exchanger 10 is into generator 1, heat absorption release refrigerant vapour and is supplied to the 3rd generator 15 to make driving thermal medium；3rd hair The concentrated solution of raw device 15 enters the 4th generator 21, heat absorption release refrigerant vapour and is provided to condenser 5, the 4th generator 21 Concentrated solution enter the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, absorb refrigerant vapour and heat release in Heated medium, the weak solution of the 3rd absorber 16 enters the 3rd generator 15, refrigerant vapour through the 3rd solution heat exchanger 18 Flow through the 3rd generator 15, the solution release that heating enters in it and provide refrigerant vapour, the cryogen of condenser 5 to condenser 5 Steam heat release enters the second evaporator 19, inhales in cooling medium into cryogen liquid, the cryogen liquid of condenser 5 through the pressurization of cryogen liquid pump 9 Heat is provided into refrigerant vapour and to the 3rd absorber 16, flows through the refrigerant vapour heat release of the 3rd generator 15 into passing through after cryogen liquid Second cryogen liquid pump 20 pressurizes into evaporator 6, absorbs heat into refrigerant vapour and provided to absorber 3, forms the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 14 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 to be sequentially communicated hair The finisher 6 of raw device 1 and evaporator 6 has condensate liquid pipeline and a ft connection again, engine 13 also have the second steam channel according to Secondary connection the second generator 2 and heat exchanger 12, heat exchanger 12 also have the second condensate liquid pipeline and ft connection；Generator 1 Also concentrated solution pipeline is connected through solution pump 7 and solution heat exchanger 10 with the second generator 2, and the second generator 2 also has dense molten Liquid pipeline is connected through the second solution heat exchanger 11 with absorber 3, and absorber 3 also has weak solution pipeline through the He of the second solution pump 8 Second solution heat exchanger 11 is connected with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution heat exchanger 10 Connected with generator 1, 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 15 has cryogen liquid pipeline through the second cryogen liquid pump 20 and evaporation again after vapour passage is connected with the 3rd generator 15 Device 6 is connected；3rd generator 15 also has concentrated solution pipeline to be inhaled through the 3rd solution pump 17 and the 3rd solution heat exchanger 18 and the 3rd Receive device 16 to connect, the 3rd absorber 16 also has weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution heat exchanger 18, 3rd generator 15 also has refrigerant steam channel to be connected with condenser 5, condenser 5 also have cryogen liquid pipeline through cryogen liquid pump 9 and Evaporator 6 is connected, and evaporator 6 also has refrigerant steam channel to be connected with the absorber 16 of absorber 3 and the 3rd respectively, and condenser 5 is also There are cooling medium pipeline and ft connection, absorber 3, the second absorber 4 and the 3rd absorber 16 also have heated medium respectively 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 engine 13 is to the second generator 2 and heat exchanger 12 There is provided the second steam, the second steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through second after condensate liquid Lime set pipeline is discharged, and engine 13 provides steam discharge to generator 1 and evaporator 6, and steam discharge flows through generator 1 and evaporator 6, progressively Heat release is discharged into condensed liquid pipeline after condensate liquid；The concentrated solution of generator 1 enters through solution pump 7 and solution heat exchanger 10 Second generator 2, heat absorption release refrigerant vapour are simultaneously provided to the second absorber 4, and the concentrated solution of the second generator 2 is through the second 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 molten through second 8 and second solution heat exchanger of liquid pump 11 enters the second absorber 4, absorbs refrigerant vapour and heat release is in heated medium, and second The weak solution of absorber 4 is through solution heat exchanger 10 is into generator 1, heat absorption release refrigerant vapour and is supplied to the 3rd generator 15 make driving thermal medium；The concentrated solution of the 3rd generator 15 enters the 3rd through the 3rd solution pump 17 and the 3rd solution heat exchanger 18 , in heated medium, the weak solution of the 3rd absorber 16 is through the 3rd solution heat exchange for absorber 16, absorption refrigerant vapour and heat release Device 18 enters the 3rd generator 15, and the solution that refrigerant vapour flows through the 3rd generator 15, heating enters in it discharges and to condensation Device 5 provides refrigerant vapour, and in cooling medium into cryogen liquid, the cryogen liquid of condenser 5 is through cryogen for the refrigerant vapour heat release of condenser 5 The pressurization of liquid pump 9 enters evaporator 6, flow through the refrigerant vapour heat release of the 3rd generator 15 into after cryogen liquid through the second cryogen liquid pump 20 pressurizations enter evaporator 6, and the cryogen liquid of evaporator 6 absorbs heat into refrigerant vapour and respectively to the absorber 16 of absorber 3 and the 3rd There is provided, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 15 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 to connect with generator 1 Generator 1 has condensate liquid pipeline and ft connection again after logical, and engine 13 also has the second steam channel to connect it with 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 sequentially communicated the second hair Raw device 2 and heat exchanger 12, heat exchanger 12 also have the 3rd condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipe Road connects through solution pump 7 and solution heat exchanger 10 with the second generator 2, and the second generator 2 also has concentrated solution pipeline through second Solution heat exchanger 11 is connected with absorber 3, and absorber 3 also has weak solution pipeline to be handed over through the second solution pump 8 and the second solution heat Parallel operation 11 is connected with the second absorber 4, and the second absorber 4 also has weak solution pipeline to connect with generator 1 through solution heat exchanger 10 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 and the 3rd The 3rd generator 15 has cryogen liquid pipeline to be connected with evaporator 6 through the second cryogen liquid pump 20 again after generator 15 is connected；3rd Generator 15 also has concentrated solution pipeline to be connected with the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, the Three absorbers 16 also have weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution heat exchanger 18, and the 3rd generator 15 is also There is refrigerant steam channel to be connected with condenser 5, condenser 5 also has cryogen liquid pipeline to be connected with evaporator 6 through cryogen liquid pump 9, steams Hair device 6 also has refrigerant steam channel to be connected with the absorber 16 of absorber 3 and the 3rd respectively, and condenser 5 also has cooling medium pipeline With ft connection, absorber 3, the second absorber 4 and the 3rd absorber 16 also have heated medium pipeline and ft connection respectively, Heat exchanger 12 also has heated medium pipeline and ft connection.
(2) in flow, compared with the dynamic co-feeding system of heat shown in Figure 14, difference is：Engine 13 occurs to second Device 2 and heat exchanger 12 provide the 3rd steam, and the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release Cheng Leng Discharged through the 3rd condensate liquid pipeline after lime set, engine 13 provides the second steam to evaporator 6, and the second steam is in evaporator 6 Interior heat release is discharged into after condensate liquid through the second condensate liquid pipeline, and engine 13 provides steam discharge to generator 1, partly or entirely row Steam flow is discharged through generator 1, heat release into condensed liquid pipeline after condensate liquid.
What the dynamic co-feeding system of heat shown in Figure 16 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump and the 4th generator Constituted；Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage The 4th generator 21 has condensate liquid pipeline and ft connection again after being connected with the 4th generator 21, and engine 13 also has second to steam Vapour passage is sequentially communicated generator 1 and the finisher 6 of evaporator 6 the second condensate liquid pipeline and ft connection, engine again 13 also have the 3rd steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, and heat exchanger 12 also has the 3rd condensate line Road and ft connection；Generator 1 also has concentrated solution pipeline to be connected with the second generator 2 through solution pump 7 and solution heat exchanger 10, Second generator 2 also has concentrated solution pipeline to be connected with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has weak solution Pipeline is connected through the second solution pump 8 and the second solution heat exchanger 11 with the second absorber 4, and the second absorber 4 also has weak solution Pipeline is connected through solution heat exchanger 10 with generator 1, and the second generator 2 also has refrigerant steam channel to connect with the second absorber 4 Logical, the 3rd generator 15 has cryogen liquid pipeline to pass through again after generator 1 also has refrigerant steam channel to be connected with the 3rd generator 15 Second cryogen liquid pump 20 is connected with evaporator 6；3rd generator 15 also has concentrated solution pipeline to be connected with the 4th generator 21, and the 4th Generator 21 also has concentrated solution pipeline to be connected with the 3rd absorber 16 through the 3rd solution pump 17 and the 3rd solution heat exchanger 18, the Three absorbers 16 also have weak solution pipeline to be connected with the 3rd generator 15 through the 3rd solution heat exchanger 18, and the 3rd generator 15 is also There is refrigerant steam channel to be connected with condenser 5, the 4th generator 21 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 16 is connected, and condenser 5 also has cooling medium pipeline and ft connection, absorber 3, the second absorber 4 and the 3rd Absorber 16 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.
(2) in flow, live steam enters engine 13 and is depressured work done, and engine 13 is to the second generator 2 and heat exchanger 12 There is provided the 3rd steam, the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through the 3rd after condensate liquid Lime set pipeline is discharged, and engine 13 provides the second steam to generator 1 and evaporator 6, and the second steam flows through generator 1 and evaporation Device 6, progressively heat release are discharged into after condensate liquid through the second condensate liquid pipeline, and engine 13 provides steam discharge to the 4th generator 21, Part or all of steam discharge flows through the 4th generator 21, heat release into condensed liquid pipeline discharge after condensate liquid；Generator 1 it is dense molten Liquid discharges refrigerant vapour and is carried to the second absorber 4 through solution pump 7 and solution heat exchanger 10 into the second generator 2, heat absorption For the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 11, absorbs refrigerant vapour and heat release is in quilt Heating medium, the weak solution of absorber 3 enters the second absorber 4, absorbs through the second solution pump 8 and the second solution heat exchanger 11 Refrigerant vapour and heat release enter generator 1, inhale in heated medium, the weak solution of the second absorber 4 through solution heat exchanger 10 Heat release refrigerant vapour is simultaneously supplied to the 3rd generator 15 to make driving thermal medium；The concentrated solution of the 3rd generator 15 enters the 4th hair Raw device 21, heat absorption release refrigerant vapour are simultaneously provided to condenser 5, and the concentrated solution of the 4th generator 21 is through the 3rd solution pump 17 and the Three solution heat exchanger 18 enters the 3rd absorber 16, absorbs refrigerant vapour and heat release is in heated medium, the 3rd absorber 16 Weak solution through the 3rd solution heat exchanger 18 enter the 3rd generator 15, refrigerant vapour flow through the 3rd generator 15, heat into Enter the solution release in it and provide refrigerant vapour to condenser 5, the refrigerant vapour heat release of condenser 5 is in cooling medium into cryogen Liquid, the cryogen liquid of condenser 5 enters evaporator 6 through the pressurization of cryogen liquid pump 9, flow through the refrigerant vapour heat release of the 3rd generator 15 into Enter evaporator 6 through the pressurization of the second cryogen liquid pump 20 after cryogen liquid, the cryogen liquid of evaporator 6 absorbs heat into refrigerant vapour and difference There is provided to the absorber 16 of absorber 3 and the 3rd, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 17 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat Exchanger is constituted；Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has to be arranged Vapour passage is sequentially communicated generator 1 and the finisher 6 of evaporator 6 condensate liquid pipeline and ft connection again, and engine 13 is also There is the second steam channel to be sequentially communicated the second generator 2 and heat exchanger 12, heat exchanger 12 also have the second condensate liquid pipeline with Ft connection；Generator 1 also have concentrated solution pipeline through solution pump 7, the solution heat exchanger 11 of solution heat exchanger 10 and second with Second generator 2 is connected, and the second generator 2 also has concentrated solution pipeline to be connected with absorber 3 through the second solution heat exchanger 11, inhales Receiving device 3 also has weak solution pipeline to be connected with the second absorber 4 through the second solution pump 8 and the 3rd solution heat exchanger 18, and second inhales Receiving device 4 also has weak solution pipeline to be connected with the 3rd absorber 16 through the 3rd solution heat exchanger 18, and the 3rd absorber 16 is also dilute Solution line is connected through the 3rd solution pump 17 and the 4th solution heat exchanger 23 with the 4th absorber 22, and the 4th absorber 22 also has Weak solution pipeline is connected through the 4th solution heat exchanger 23 and solution heat exchanger 10 with generator 1, and the second generator 2 is also cold Agent steam channel is connected with the second absorber 4, and generator 1 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has 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 the 3rd Absorber 16 is connected, condenser 5 also have cryogen liquid pipeline connected with the 3rd absorber 16 through the second cryogen liquid pump 20 after the 3rd Absorber 16 has refrigerant steam channel to be connected with the 4th absorber 22 again, and condenser 5 also has cooling medium pipeline and ft connection, Absorber 3, the second absorber 4 and the 4th absorber 22 also have heated medium pipeline and ft connection, heat exchanger 12 respectively Also heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 13 and is depressured work done, and engine 13 is to the second generator 2 and heat exchanger 12 There is provided the second steam, the second steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through second after condensate liquid Lime set pipeline is discharged, and engine 13 provides steam discharge to generator 1 and evaporator 6, and part or all of steam discharge flows through generator 1 and steams Hair device 6, progressively heat release are discharged into condensed liquid pipeline after condensate liquid；The concentrated solution of generator 1 is handed over through solution pump 7, solution heat 10 and second solution heat exchanger of parallel operation 11 enters the second generator 2, and concentrated solution heat absorption release cryogen in the second generator 2 steams Vapour is simultaneously provided to the second absorber 4, and the concentrated solution of the second generator 2 enters absorber 3, absorbs through the second solution heat exchanger 11 , in heated medium, the weak solution pipeline of absorber 3 is through the second solution pump 8 and the 3rd solution heat exchanger for refrigerant vapour and heat release 18 enter the second absorbers 4, absorb refrigerant vapour and heat release in heated medium, and the weak solution pipeline of the second absorber 4 is through the Three solution heat exchanger 18 enters the 3rd absorber 16, absorbs refrigerant vapour and heat release in cryogen liquid, the 3rd absorber 16 it is dilute Solution enters the 4th absorber 22 through the 3rd solution pump 17 and the 4th solution heat exchanger 23, absorbs refrigerant vapour and heat release is in quilt Heating medium, the weak solution of the 4th absorber 22 through the 4th solution heat exchanger 23 and solution heat exchanger 10 enter generator 1, Heat absorption release refrigerant vapour is simultaneously provided to condenser 5；The refrigerant vapour heat release of condenser 5 is in cooling medium into cryogen liquid, condensation The cryogen liquid of device 5 is divided into two-way --- and the first via is pressurizeed into evaporator 6 through cryogen liquid pump 9, absorbs heat into refrigerant vapour and difference There is provided to the absorber 16 of absorber 3 and the 3rd, second tunnel the second cryogen liquid pump 20 flows through the 3rd absorber 16, inhales after pressurizeing Heat is provided into refrigerant vapour and to the 4th absorber 22, forms the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 18 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat Exchanger is constituted；Engine 13 connects working machine 14, and engine 13 has live steam passage and ft connection, and engine 13 also has to be arranged Generator 1 has condensate liquid pipeline and ft connection again after vapour passage is connected with generator 1, and engine 13 also has the second steam to lead to The finisher 6 that road is connected with evaporator 6 has the second condensate liquid pipeline and ft connection again, and engine 13 also has the 3rd steam to lead to Road is sequentially communicated the second generator 2 and heat exchanger 12, and heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection；Occur Device 1 also has concentrated solution pipeline to connect through solution pump 7, the solution heat exchanger 11 of solution heat exchanger 10 and second and the second generator 2 Logical, the second generator 2 also has concentrated solution pipeline to be connected with absorber 3 through the second solution heat exchanger 11, and absorber 3 also has dilute molten Liquid pipeline is connected through the second solution pump 8 and the 3rd solution heat exchanger 18 with the second absorber 4, and the second absorber 4 also has dilute molten Liquid pipeline is connected through the 3rd solution heat exchanger 18 with the 3rd absorber 16, and the 3rd absorber 16 also has weak solution pipeline through the 3rd The solution heat exchanger 23 of solution pump 17 and the 4th is connected with the 4th absorber 22, and the 4th absorber 22 also has weak solution pipeline through the Four solution heat exchangers 23 and solution heat exchanger 10 are connected with generator 1, and the second generator 2 also has refrigerant steam channel and the Two absorbers 4 are connected, and generator 1 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen liquid pipeline through cold Agent liquid pump 9 is connected with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with the absorber 16 of absorber 3 and the 3rd respectively, The 3rd absorber 16 has cold again after condenser 5 also has cryogen liquid pipeline to be connected with the 3rd absorber 16 through the second cryogen liquid pump 20 Agent steam channel is connected with the 4th absorber 22, and condenser 5 also has cooling medium pipeline and ft connection, and absorber 3, second is inhaled Receive the absorber 22 of device 4 and the 4th also has heated medium pipeline and ft connection respectively, and 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 17, difference is：Engine 13 occurs to second Device 2 and heat exchanger 12 provide the 3rd steam, and the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release Cheng Leng Discharged through the 3rd condensate liquid pipeline after lime set, engine 13 provides the second steam to evaporator 6, and the second steam is in evaporator 6 Interior heat release is discharged into after condensate liquid through the second condensate liquid pipeline, and engine 13 provides steam discharge to generator 1, partly or entirely row Steam flow is discharged through generator 1, heat release into condensed liquid pipeline after condensate liquid.
What the dynamic co-feeding system of heat shown in Figure 19 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator, the second cryogen liquid pump, the 4th absorber, 4th solution heat exchanger and the 3rd cryogen liquid pump are constituted；Engine 13 connects working machine 14, and engine 13 has live steam passage With ft connection, engine 13 also has exhaust passage to be sequentially communicated the second evaporator 19 after the evaporator 19 of generator 1 and second There are condensate liquid pipeline and ft connection again, the finisher 6 that also the second steam channel is connected with evaporator 6 of engine 13 has again Second condensate liquid pipeline and ft connection, engine 13 also have the 3rd steam channel to be sequentially communicated the second generator 2 and heat exchange Device 12, heat exchanger 12 also has the 3rd condensate liquid pipeline and ft connection；Generator 1 also has concentrated solution pipeline through solution pump 7, molten The solution heat exchanger 11 of liquid heat exchanger 10 and second is connected with the second generator 2, and the second generator 2 also has concentrated solution pipeline warp Second solution heat exchanger 11 is connected with absorber 3, and absorber 3 also has weak solution pipeline through the second solution pump 8 and the 3rd solution Heat exchanger 18 is connected with the second absorber 4, and the second absorber 4 also has weak solution pipeline through the 3rd solution heat exchanger 18 and the Three absorbers 16 are connected, the 3rd absorber 16 also have weak solution pipeline through the 3rd solution pump 17 and the 4th solution heat exchanger 23 with 4th absorber 22 is connected, and the 4th absorber 22 also has weak solution pipeline through the 4th solution heat exchanger 23 and solution heat exchanger 10 connect with generator 1, and the second generator 2 also has refrigerant steam channel to be connected with the second absorber 4, and generator 1 also has cryogen Steam channel is connected with condenser 5, and condenser 5 also has cryogen liquid pipeline to be connected with evaporator 6 through cryogen liquid pump 9, and evaporator 6 is also There is refrigerant steam channel to be connected with absorber 3, condenser 5 also has cryogen liquid pipeline through the second cryogen liquid pump 20 and the 3rd absorber The 3rd absorber 16 has refrigerant steam channel to be connected with the 4th absorber 22 again after 16 connections, and condenser 5 also has cryogen liquid pipe The cryogen liquid pumps 24 of Lu Jing tri- are connected with the second evaporator 19, and the second evaporator 19 also has refrigerant steam channel and the 3rd absorber 16 connections, condenser 5 also has cooling medium pipeline and ft connection, and absorber 3, the second absorber 4 and the 4th absorber 22 are 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 engine 13 is to the second generator 2 and heat exchanger 12 There is provided the 3rd steam, the 3rd steam flows through the second generator 2 and heat exchanger 12, progressively heat release is into cold through the 3rd after condensate liquid Lime set pipeline discharge, engine 13 to evaporator 6 provide the second steam, the second steam in evaporator 6 heat release into condensate liquid it Discharged by the second condensate liquid pipeline, engine 13 provides steam discharge, part or all of steam discharge to 1 and second evaporator of generator 19 Flow through generator 1 and the second evaporator 19, progressively heat release discharged into condensed liquid pipeline after condensate liquid；Generator 1 it is dense molten Liquid enters the second generator 2 through solution pump 7,10 and second solution heat exchanger of solution heat exchanger 11, and concentrated solution is in the second hair Heat absorption discharges refrigerant vapour and is provided to the second absorber 4 in raw device 2, and the concentrated solution of the second generator 2 is handed over through the second solution heat Parallel operation 11 enters absorber 3, absorbs refrigerant vapour and heat release is in heated medium, and the weak solution pipeline of absorber 3 is molten through second Liquid pump 8 and the 3rd solution heat exchanger 18 enter the second absorber 4, absorb refrigerant vapour and heat release is in heated medium, and second The weak solution pipeline of absorber 4 through the 3rd solution heat exchanger 18 enter the 3rd absorber 16, absorb refrigerant vapour and heat release in Cryogen liquid, the weak solution of the 3rd absorber 16 enters the 4th absorber through the 3rd solution pump 17 and the 4th solution heat exchanger 23 22nd, absorb refrigerant vapour and heat release is in heated medium, the weak solution of the 4th absorber 22 is through the He of the 4th solution heat exchanger 23 Solution heat exchanger 10 discharges refrigerant vapour and is provided to condenser 5 into generator 1, heat absorption；The refrigerant vapour of condenser 5 is put In cooling medium into cryogen liquid, the cryogen liquid of condenser 5 is divided into three tunnels to heat --- and the first via enters evaporation through the pressurization of cryogen liquid pump 9 Device 6, absorb heat into refrigerant vapour and provided to absorber 3, second tunnel the second cryogen liquid pump 20 flows through the 3rd absorption after pressurizeing Device 16, absorb heat into refrigerant vapour and provided to the 4th absorber 22, the pressurization of the 3rd the 3rd cryogen liquid pump of tunnel 24 enters second and steams Device 19 is sent out, refrigerant vapour is absorbed heat into and is provided to the 3rd absorber 16, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of the effect that the technology of the present invention can be realized --- heat proposed by the invention have the effect that and Advantage：
(1) temperature difference between engine steam discharge and cold environment is utilized, and realizes the rationalization of total system heat energy utilization.
(2) high-grade steam elder generation's work done (generating), heat supply is used for after grade reduction, is met thermal energy step and is utilized principle.
(3) farthest reduce the heat transfer temperature difference between thermal source and heated medium, improve utilization efficiency of heat energy.
(4) various concrete technical schemes are given, numerous different actual states are coped with, there is the scope of application wider.
(5) steam discharge and engine intermediate extraction is combined the thermal source as absorption heat pump flow, to meet different user Flexibility is brought with duty requirements.
(6) during variable working condition, the 3rd class absorption heat pump heat supply flow, the thermic load of heat exchanger can be preferentially used to have Regulation is visible, it ensure that system is efficient and flexible.
(7) double dominant with extraction for heat supply and condensing heat supply, largely avoids heating demand change to work done The influence of (generating).
(8) type of the dynamic co-feeding system of heat is enriched, the range of application of the 3rd class absorption heat pump is extended, is conducive to more Making full use of for the temperature difference is realized using the 3rd class absorption heat pump well.

Claims (32)

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 heat exchanger, the second solution heat exchanger, heat exchanger, engine and work Machine is constituted；Engine (13) connects working machine (14), and engine (13) has live steam passage and a ft connection, engine (13) or Also exhaust passage and ft connection, engine (13) also have exhaust passage to be sequentially communicated after generator (1) and evaporator (6) Evaporator (6) has condensate liquid pipeline and ft connection again, and engine (13) also has the second steam channel to be sequentially communicated the second generation Device (2) and heat exchanger (12), heat exchanger (12) also have the second condensate liquid pipeline and ft connection；Generator (1) is also dense Solution line is connected through solution pump (7) and solution heat exchanger (10) with the second generator (2), and the second generator (2) is also dense Solution line is connected through the second solution heat exchanger (11) with absorber (3), and absorber (3) also has weak solution pipeline molten through second Liquid pump (8) and the second solution heat exchanger (11) are connected with the second absorber (4), and the second absorber (4) also has weak solution pipeline Connected with generator (1) through solution heat exchanger (10), the second generator (2) also has refrigerant steam channel and the second absorber (4) connect, generator (1) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) also has cryogen liquid pipeline through cold Agent liquid pump (9) is connected with evaporator (6), and evaporator (6) also has refrigerant steam channel to be connected with absorber (3), and condenser (5) is also There are cooling medium pipeline and ft connection, absorber (3) and the second absorber (4) also have heated medium pipeline with outside respectively Connection, heat exchanger (12) 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 dynamic co-feeding system of heat described in claim 1, to cancel evaporator, by engine (13) Have exhaust passage to be sequentially communicated generator (1) and the finisher (6) of evaporator (6) has condensate liquid pipeline to be adjusted with ft connection again It is whole there is exhaust passage to be connected with generator (1) for engine (13) after generator (1) have condensate liquid pipeline and ft connection again, There is refrigerant steam channel to be connected 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 with evaporator (6) through cryogen liquid pump (9) 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.
3. 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, the second solution heat exchanger, heat exchanger, engine and work Machine is constituted；Engine (13) connects working machine (14), and engine (13) has live steam passage and a ft connection, engine (13) or Also exhaust passage and ft connection, there are generator (1) again after engine (13) also has exhaust passage to be connected with generator (1) Condensate liquid pipeline and ft connection, engine (13) also have finisher (6) that the second steam channel connects with evaporator (6) again Have the second condensate liquid pipeline and a ft connection, engine (13) also have the 3rd steam channel be sequentially communicated the second generator (2) and Heat exchanger (12), heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection；Generator (1) also has concentrated solution pipeline Connected with the second generator (2) through solution pump (7) and solution heat exchanger (10), the second generator (2) also has concentrated solution pipeline Connected with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline through the second solution pump (8) Connected with the second solution heat exchanger (11) with the second absorber (4), the second absorber (4) also has weak solution pipeline through solution heat Exchanger (10) is connected with generator (1), and the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), hair Raw device (1) also has refrigerant steam channel to be connected with condenser (5), condenser (5) also have cryogen liquid pipeline through cryogen liquid pump (9) and Evaporator (6) is connected, and evaporator (6) also has refrigerant steam channel to be connected with absorber (3), and condenser (5) also has cooling medium Pipeline and ft connection, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection respectively, and heat is handed over Parallel operation (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 3, 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) refrigerant steam channel connects be adjusted in the lump with absorber (3) engine (13) is had into the second steam channel and absorber (3) connect, there is cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9) 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.
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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 has exhaust passage to be sequentially communicated the finisher (6) of the 3rd generator (15), generator (1) and evaporator (6) There are condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be sequentially communicated the second generator (2) and heat Exchanger (12), heat exchanger (12) also has the second condensate liquid pipeline and ft connection；Generator (1) also has concentrated solution pipeline to pass through Solution pump (7) and solution heat exchanger (10) are connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline to pass through Second solution heat exchanger (11) is connected with absorber (3), absorber (3) also have weak solution pipeline through the second solution pump (8) and Second solution heat exchanger (11) is connected with the second absorber (4), and the second absorber (4) also has weak solution pipeline to be handed over through solution heat Parallel operation (10) is connected with generator (1), and the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), is occurred Device (1) also has refrigerant steam channel to be connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd Solution pump (17) and the 3rd solution heat exchanger (18) are connected with the 3rd generator (15), and the 3rd generator (15) also has concentrated solution Pipeline is connected through the 3rd solution heat exchanger (18) with the 3rd absorber (16), and the 3rd generator (15) also has refrigerant steam channel Connected with condenser (5), condenser (5) also has cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9), evaporator (6) Also refrigerant steam channel is connected with absorber (3), and condenser (5) and the 3rd absorber (16) also have cooling medium pipeline respectively With ft connection, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection, heat exchanger respectively (12) there are 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 dynamic co-feeding system of heat described in claim 5, to cancel evaporator, by engine (13) The finisher (6) for having exhaust passage to be sequentially communicated the 3rd generator (15), generator (1) and evaporator (6) has condensate liquid again Pipeline is adjusted to engine (13) with ft connection has exhaust passage to be sequentially communicated after the 3rd generator (15) and generator (1) Generator (1) has condensate liquid pipeline and ft connection again, has refrigerant steam channel to connect tune with absorber (3) evaporator (6) It is whole to set up exhaust passage for engine (13) and connected with absorber (3), condenser (5) there is into cryogen liquid pipeline through cryogen liquid pump (9) connected with evaporator (6) and be adjusted to condenser (5) and have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form heat dynamic Co-feeding system.
7. 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 to be connected with the 3rd generator (15) after the 3rd generator (15) have again condensate liquid pipeline with it is outer Portion connects, and engine (13) also has the second steam channel to be sequentially communicated the finisher that generator (1) is connected with evaporator (6) (6) there are the second condensate liquid pipeline and ft connection again, engine (13) also has the 3rd steam channel to be sequentially communicated the second generator (2) and heat exchanger (12), heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection；Generator (1) also has dense molten Liquid pipeline is connected through solution pump (7) and solution heat exchanger (10) with the second generator (2), and the second generator (2) also has dense molten Liquid pipeline is connected through the second solution heat exchanger (11) with absorber (3), and absorber (3) also has weak solution pipeline through the second solution Pump (8) and the second solution heat exchanger (11) are connected with the second absorber (4), and the second absorber (4) also has weak solution pipeline to pass through Solution heat exchanger (10) is connected with generator (1), and the second generator (2) also has refrigerant steam channel and the second absorber (4) Connection, generator (1) also has refrigerant steam channel to be connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipe The solution pumps (17) of Lu Jing tri- and the 3rd solution heat exchanger (18) are connected with the 3rd generator (15), and the 3rd generator (15) is also There is concentrated solution pipeline to be connected with the 3rd absorber (16) through the 3rd solution heat exchanger (18), the 3rd generator (15) also has cryogen Steam channel is connected with condenser (5), and condenser (5) also has cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9), Evaporator (6) also has refrigerant steam channel to be connected with absorber (3), and condenser (5) and the 3rd absorber (16) also have cold respectively But medium pipeline and ft connection, absorber (3) and the second absorber (4) also have heated medium pipeline to connect with outside respectively Logical, heat exchanger (12) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 7, to cancel evaporator, by engine (13) Have the second steam channel to be sequentially communicated the finisher (6) that generator (1) connects with evaporator (6) has the second condensate liquid pipeline again Be adjusted to generator (1) after engine (13) has the second steam channel to be connected with generator (1) with ft connection has 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 be connected with absorber (3), condenser (5) is had into cryogen liquid pipeline through cryogen liquid pump (9) and evaporator (6) connection 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.
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 heat exchanger, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 Generator (1) has condensate liquid again after power machine (13) also has exhaust passage to be sequentially communicated the 3rd generator (15) and generator (1) Pipeline and ft connection, engine (13) also have the finisher (6) that the second steam channel is connected with evaporator (6) to have second again Condensate liquid pipeline and ft connection, engine (13) also have the 3rd steam channel to be sequentially communicated the second generator (2) and heat exchange Device (12), heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection；Generator (1) also has concentrated solution pipeline through solution Pump (7) and solution heat exchanger (10) are connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline through second Solution heat exchanger (11) is connected with absorber (3), and absorber (3) also has weak solution pipeline through the second solution pump (8) and second Solution heat exchanger (11) is connected with the second absorber (4), and the second absorber (4) also has weak solution pipeline through solution heat exchanger (10) connected with generator (1), the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), generator (1) refrigerant steam channel is connected with the 3rd absorber (16), the 3rd absorber (16) also has weak solution pipeline molten through the 3rd Liquid pump (17) and the 3rd solution heat exchanger (18) are connected with the 3rd generator (15), and the 3rd generator (15) also has concentrated solution pipe The solution heat exchangers of Lu Jing tri- (18) is connected with the 3rd absorber (16), the 3rd generator (15) also have refrigerant steam channel with Condenser (5) is connected, and condenser (5) also has cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9), and evaporator (6) is also There is refrigerant steam channel to be connected with absorber (3), condenser (5) and the 3rd absorber (16) also have respectively cooling medium pipeline with Ft connection, absorber (3) and the second absorber (4) also have heated medium pipeline and ft connection, heat exchanger respectively (12) there are heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is in the dynamic co-feeding system of heat described in claim 9, 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) refrigerant steam channel connects be adjusted in the lump with absorber (3) engine (13) is had into the second steam channel and absorber (3) connect, there is cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9) 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.
The 11. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 a ft connection, engine (13) or also There are exhaust passage and ft connection, engine (13) also has exhaust passage to be sequentially communicated generator (1), evaporator (6) and second The second evaporator (19) has condensate liquid pipeline and ft connection again after evaporator (19), and engine (13) also has the second steam to lead to Road is sequentially communicated the second generator (2) and heat exchanger (12), and heat exchanger (12) also has the second condensate liquid pipeline to connect with outside It is logical；Generator (1) also has concentrated solution pipeline to be connected with the second generator (2) through solution pump (7) and solution heat exchanger (10), the Two generators (2) also have concentrated solution pipeline to be connected with absorber (3) through the second solution heat exchanger (11), and absorber (3) also has Weak solution pipeline is connected through the second solution pump (8) and the second solution heat exchanger (11) with the second absorber (4), the second absorber (4) weak solution pipeline is connected with generator (1) through solution heat exchanger (10), the second generator (2) also has refrigerant vapour Passage is connected with the second absorber (4), generator (1) also have refrigerant steam channel to be connected with the 3rd generator (15) after the 3rd Generator (15) has cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) again, and evaporator (6) also has cryogen to steam Vapour passage is connected with absorber (3)；3rd generator (15) also has concentrated solution pipeline through the 3rd solution pump (17) and the 3rd solution Heat exchanger (18) is connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution heat exchange Device (18) is connected with the 3rd generator (15), and the 3rd generator (15) also has refrigerant steam channel to be connected with condenser (5), condensation Device (5) also has cryogen liquid pipeline to be connected with the second evaporator (19) through cryogen liquid pump (9), and the second evaporator (19) also has cryogen to steam Vapour passage is connected with the 3rd absorber (16), and condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second Absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, and heat exchanger (12) also has quilt Heating medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, is in the dynamic co-feeding system of heat described in claim 11, to cancel evaporator, by engine (13) exhaust passage is sequentially communicated after generator (1), evaporator (6) and the second evaporator (19) the second evaporator (19) 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 evaporator (19) the second evaporator (19) has condensate liquid pipeline and ft connection again after, and evaporator (6) is had refrigerant steam channel and inhaled Receive device (3) connection to be adjusted to engine (13) and set up exhaust passage to be connected with absorber (3), the 3rd generator (15) is had into cryogen Liquid pipeline connects with evaporator (6) through the second cryogen liquid pump (20) and is adjusted to the 3rd generator (15) and has cryogen liquid pipeline through second Cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The 13. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 a ft connection, engine (13) or also There are exhaust passage and ft connection, engine (13) also has exhaust passage to be sequentially communicated generator (1) and the second evaporator (19) The second evaporator (19) has condensate liquid pipeline and ft connection again afterwards, and engine (13) also has the second steam channel and evaporator (6) finisher (6) of connection has the second condensate liquid pipeline and a ft connection again, engine (13) also have the 3rd steam channel according to The second generator of secondary connection (2) and heat exchanger (12), heat exchanger (12) also have the 3rd condensate liquid pipeline and ft connection；Hair Raw device (1) also has concentrated solution pipeline to be connected with the second generator (2) through solution pump (7) and solution heat exchanger (10), the second hair Raw device (2) also has concentrated solution pipeline to be connected with absorber (3) through the second solution heat exchanger (11), and absorber (3) also has dilute molten Liquid pipeline is connected through the second solution pump (8) and the second solution heat exchanger (11) with the second absorber (4), the second absorber (4) Also weak solution pipeline is connected through solution heat exchanger (10) with generator (1), and the second generator (2) also has refrigerant steam channel Connected with the second absorber (4), the 3rd occurs after generator (1) also has refrigerant steam channel to be connected with the 3rd generator (15) Device (15) has cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) again, and evaporator (6) also has refrigerant vapour to lead to Road is connected with absorber (3)；3rd generator (15) also has concentrated solution pipeline to be handed over through the 3rd solution pump (17) and the 3rd solution heat Parallel operation (18) is connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution heat exchanger (18) connected with the 3rd generator (15), the 3rd generator (15) also has refrigerant steam channel to be connected with condenser (5), condenser (5) cryogen liquid pipeline is connected with the second evaporator (19) through cryogen liquid pump (9), the second evaporator (19) also has refrigerant vapour Passage is connected with the 3rd absorber (16), and condenser (5) also has cooling medium pipeline and ft connection, and absorber (3), second inhale Receive device (4) and the 3rd absorber (16) also has heated medium pipeline and a ft connection respectively, and heat exchanger (12) also has and added Heat medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, is in the dynamic co-feeding system of heat described in claim 13, 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 with 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 absorption Device (3) is connected, and is had cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) in the 3rd generator (15) and is adjusted to 3rd generator (15) has cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, forms the dynamic co-feeding system of heat.
The 15. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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 a ft connection, engine (13) or also Generator (1) has cold again after having exhaust passage and ft connection, engine (13) to also have exhaust passage to be connected with generator (1) Lime set pipeline and ft connection, engine (13) also have the second steam channel to be sequentially communicated evaporator (6) and the second evaporator (19) the second evaporator (19) has the second condensate liquid pipeline and ft connection again after, and engine (13) also has the 3rd steam channel The second generator (2) and heat exchanger (12) are sequentially communicated, heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection； Generator (1) also has concentrated solution pipeline to be connected with the second generator (2) through solution pump (7) and solution heat exchanger (10), and second Generator (2) also has concentrated solution pipeline to be connected with absorber (3) through the second solution heat exchanger (11), and absorber (3) is also dilute Solution line is connected through the second solution pump (8) and the second solution heat exchanger (11) with the second absorber (4), the second absorber (4) weak solution pipeline is connected with generator (1) through solution heat exchanger (10), the second generator (2) also has refrigerant vapour Passage is connected with the second absorber (4), generator (1) also have refrigerant steam channel to be connected with the 3rd generator (15) after the 3rd Generator (15) has cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) again, and evaporator (6) also has cryogen to steam Vapour passage is connected with absorber (3)；3rd generator (15) also has concentrated solution pipeline through the 3rd solution pump (17) and the 3rd solution Heat exchanger (18) is connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution heat exchange Device (18) is connected with the 3rd generator (15), and the 3rd generator (15) also has refrigerant steam channel to be connected with condenser (5), condensation Device (5) also has cryogen liquid pipeline to be connected with the second evaporator (19) through cryogen liquid pump (9), and the second evaporator (19) also has cryogen to steam Vapour passage is connected with the 3rd absorber (16), and condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second Absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, and heat exchanger (12) also has quilt Heating medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 16. heat, is in the dynamic co-feeding system of heat described in claim 15, to cancel evaporator, by engine (13) the second evaporator (19) has second again after having the second steam channel to be sequentially communicated evaporator (6) and the second evaporator (19) Condensate liquid pipeline is adjusted to after engine (13) has the second steam channel to be connected with the second evaporator (19) with ft connection Two evaporators (19) 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 be connected with absorber (3), and the 3rd generator (15) is had into cryogen liquid Pipeline connects with evaporator (6) through the second cryogen liquid pump (20) and is adjusted to the 3rd generator (15) and has cryogen liquid pipeline cold through second Agent liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The 17. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator, the second cryogen liquid pump Constituted with the 4th generator；Engine (13) connects working machine (14), and engine (13) has live steam passage and ft connection, moves Power machine (13) or also exhaust passage and ft connection, engine (13) also have exhaust passage to connect it with the 4th generator (21) The 4th generator (21) has condensate liquid pipeline and ft connection again afterwards, and engine (13) also has the second steam channel to be sequentially communicated hair The second evaporator (19) has the second condensate liquid pipeline and outside to connect again afterwards for raw device (1), evaporator (6) and the second evaporator (19) Logical, engine (13) also has the 3rd steam channel to be sequentially communicated the second generator (2) and heat exchanger (12), heat exchanger (12) Also the 3rd condensate liquid pipeline and ft connection；Generator (1) also has concentrated solution pipeline through solution pump (7) and solution heat exchanger (10) connected with the second generator (2), the second generator (2) also has concentrated solution pipeline through the second solution heat exchanger (11) and suction Receive device (3) connection, absorber (3) also has weak solution pipeline through the second solution pump (8) and the second solution heat exchanger (11) and the Two absorbers (4) are connected, and the second absorber (4) also has weak solution pipeline to be connected with generator (1) through solution heat exchanger (10), Second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), generator (1) also have refrigerant steam channel with The 3rd generator (15) has cryogen liquid pipeline through the second cryogen liquid pump (20) and evaporator again after the connection of 3rd generator (15) (6) connect, evaporator (6) also has refrigerant steam channel to be connected with absorber (3)；3rd generator (15) also has concentrated solution pipeline Connected with the 4th generator (21), the 4th generator (21) also has concentrated solution pipeline through the 3rd solution pump (17) and the 3rd solution heat Exchanger (18) is connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution heat exchanger (18) connected with the 3rd generator (15), the 3rd generator (15) also has refrigerant steam channel to be connected with condenser (5), the 4th hair Raw device (21) 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 the second evaporator (19), the second evaporator (19) also has refrigerant steam channel to be connected with the 3rd absorber (16), condensed Device (5) also has cooling medium pipeline and ft connection, and absorber (3), the second absorber (4) and the 3rd absorber (16) 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.
The dynamic co-feeding system of 18. heat, is in the dynamic co-feeding system of heat described in claim 17, 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 (19) (19) 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 (19) the second evaporator (19) has the second condensate liquid pipeline and ft connection again, by evaporator (6) There is refrigerant steam channel to be connected with absorber (3) to be adjusted to engine (13) and set up the second steam channel to be connected with absorber (3), There is cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) in the 3rd generator (15) and be adjusted to the 3rd generator (15) there is cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The 19. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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, also engine (13) or exhaust passage With ft connection, engine (13) also has exhaust passage to be sequentially communicated the finisher (6) of generator (1) and evaporator (6) again There are condensate liquid pipeline and ft connection, engine (13) also has the second steam channel to be sequentially communicated the second generator (2) and heat friendship Parallel operation (12), heat exchanger (12) also has the second condensate liquid pipeline and ft connection；Generator (1) also has concentrated solution pipeline through molten Liquid pump (7) and solution heat exchanger (10) are connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline through Two solution heat exchangers (11) are connected with absorber (3), and absorber (3) also has weak solution pipeline through the second solution pump (8) and Two solution heat exchangers (11) are connected with the second absorber (4), and the second absorber (4) also has weak solution pipeline through solution heat exchange Device (10) is connected with generator (1), and the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), generator (1) the 3rd generator (15) has cryogen liquid pipeline through second again after also having refrigerant steam channel to be connected with the 3rd generator (15) Cryogen liquid pump (20) is connected with evaporator (6)；3rd generator (15) also has concentrated solution pipeline through the 3rd solution pump (17) and Three solution heat exchangers (18) are connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution Heat exchanger (18) is connected with the 3rd generator (15), and the 3rd generator (15) also has refrigerant steam channel with condenser (5) even Logical, condenser (5) also has cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9), and evaporator (6) also has refrigerant vapour Passage is connected with absorber (3) and the 3rd absorber (16) respectively, and condenser (5) also has cooling medium pipeline and ft connection, Absorber (3), the second absorber (4) and the 3rd absorber (16) 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.
The dynamic co-feeding system of 20. heat, is in the dynamic co-feeding system of heat described in claim 19, to cancel evaporator, by engine (13) have exhaust passage to be sequentially communicated generator (1) and the finisher (6) of evaporator (6) has condensate liquid pipeline to connect with outside again It is logical to be adjusted to generator (1) after exhaust passage is connected with generator (1) and have condensate liquid pipeline and ft connection again, will evaporate Device (6) has refrigerant steam channel to be connected with absorber (3) and the 3rd absorber (16) respectively to be adjusted to engine (13) row of setting up Vapour passage is connected with absorber (3) and the 3rd absorber (16) respectively, and condenser (5) is had into cryogen liquid pipeline through cryogen liquid pump (9) connected with evaporator (6) and be adjusted to condenser (5) and have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, by the 3rd hair Raw device (15) has cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) and have cold Agent liquid pipeline forms the dynamic co-feeding system of heat through the second cryogen liquid pump (20) and ft connection.
The 21. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, 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, also engine (13) or exhaust passage With ft connection, engine (13) also have exhaust passage to be connected with generator (1) after generator (1) have again condensate liquid pipeline with Ft connection, engine (13) also has the finisher (6) that the second steam channel is connected with evaporator (6) to have the second condensate liquid again Pipeline and ft connection, engine (13) also have the 3rd steam channel to be sequentially communicated the second generator (2) and heat exchanger (12), Heat exchanger (12) also has the 3rd condensate liquid pipeline and ft connection；Generator (1) also have concentrated solution pipeline through solution pump (7) and Solution heat exchanger (10) is connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline to be handed over through the second solution heat Parallel operation (11) is connected with absorber (3), and absorber (3) also has weak solution pipeline to be handed over through the second solution pump (8) and the second solution heat Parallel operation (11) is connected with the second absorber (4), and the second absorber (4) also has weak solution pipeline through solution heat exchanger (10) and hair Raw device (1) connection, the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), and generator (1) is also cold The 3rd generator (15) has cryogen liquid pipeline through the second cryogen liquid pump again after agent steam channel is connected with the 3rd generator (15) (20) connected with evaporator (6)；3rd generator (15) also has concentrated solution pipeline through the 3rd solution pump (17) and the 3rd solution heat Exchanger (18) is connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution heat exchanger (18) connected with the 3rd generator (15), the 3rd generator (15) also has refrigerant steam channel to be connected with condenser (5), condenser (5) also have cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9), evaporator (6) also have refrigerant steam channel respectively with Absorber (3) is connected with the 3rd absorber (16), and condenser (5) also has cooling medium pipeline and ft connection, absorber (3), Second absorber (4) and the 3rd absorber (16) also have heated medium pipeline and ft connection respectively, and heat exchanger (12) is also There are heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 22. heat, is in the dynamic co-feeding system of heat described in claim 21, 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 with ft connection, steaming again Hair device (6) has refrigerant steam channel to connect and be adjusted in the lump engine (13) with absorber (3) and the 3rd absorber (16) respectively There is the second steam channel to be connected with absorber (3) and the 3rd absorber (16) respectively, condenser (5) is had into cryogen liquid pipeline through cold Agent liquid pump (9) connects with evaporator (6) and is adjusted to condenser (5) and has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, will 3rd generator (15) has cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) there is cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, form the dynamic co-feeding system of heat.
The 23. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd generator, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump and the 4th generator Constituted；Engine (13) connects working machine (14), and engine (13) has live steam passage and a ft connection, engine (13) or also 4th generator after thering is exhaust passage and ft connection, engine (13) to also have exhaust passage to be connected with the 4th generator (21) (21) there are condensate liquid pipeline and ft connection again, engine (13) also has the second steam channel to be sequentially communicated generator (1) and steam The finisher (6) of hair device (6) has the second condensate liquid pipeline and a ft connection again, engine (13) also have the 3rd steam channel according to The second generator of secondary connection (2) and heat exchanger (12), heat exchanger (12) also have the 3rd condensate liquid pipeline and ft connection；Hair Raw device (1) also has concentrated solution pipeline to be connected with the second generator (2) through solution pump (7) and solution heat exchanger (10), the second hair Raw device (2) also has concentrated solution pipeline to be connected with absorber (3) through the second solution heat exchanger (11), and absorber (3) also has dilute molten Liquid pipeline is connected through the second solution pump (8) and the second solution heat exchanger (11) with the second absorber (4), the second absorber (4) Also weak solution pipeline is connected through solution heat exchanger (10) with generator (1), and the second generator (2) also has refrigerant steam channel Connected with the second absorber (4), the 3rd occurs after generator (1) also has refrigerant steam channel to be connected with the 3rd generator (15) Device (15) has cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) again；3rd generator (15) also has dense molten Liquid pipeline is connected with the 4th generator (21), and the 4th generator (21) also has concentrated solution pipeline through the 3rd solution pump (17) and the 3rd Solution heat exchanger (18) is connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution heat Exchanger (18) is connected with the 3rd generator (15), and the 3rd generator (15) also has refrigerant steam channel to be connected with condenser (5), 4th generator (21) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) also has cryogen liquid pipeline through cryogen liquid Pump (9) is connected with evaporator (6), evaporator (6) also have refrigerant steam channel respectively with absorber (3) and the 3rd absorber (16) Connection, condenser (5) also has cooling medium pipeline and ft connection, absorber (3), the second absorber (4) and the 3rd absorber (16) 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.
The dynamic co-feeding system of 24. heat, is in the dynamic co-feeding system of heat described in claim 23, 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 Be adjusted to generator (1) after engine (13) has the second steam channel to be connected with generator (1) with ft connection has second again Condensate liquid pipeline and ft connection, by evaporator (6) have refrigerant steam channel respectively with absorber (3) and the 3rd absorber (16) Connection is adjusted to engine (13) and sets up the second steam channel to be connected with absorber (3) and the 3rd absorber (16) respectively, by the Three generators (15) have cryogen liquid pipeline to be connected with evaporator (6) through the second cryogen liquid pump (20) to be adjusted to the 3rd generator (15) There is cryogen liquid pipeline through the second cryogen liquid pump (20) and ft connection, condenser (5) is had into cryogen liquid pipeline through cryogen liquid pump (9) Connected with evaporator (6) and be adjusted to condenser (5) and have cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, form the dynamic connection of heat For system.
The 25. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat Exchanger is constituted；Engine (13) connects working machine (14), and engine (13) has live steam passage and ft connection, engine (13) or also exhaust passage and ft connection, engine (13) also have exhaust passage to be sequentially communicated generator (1) and evaporator (6) finisher (6) has condensate liquid pipeline and ft connection again, and engine (13) also has the second steam channel to be sequentially communicated Two generators (2) and heat exchanger (12), heat exchanger (12) also have the second condensate liquid pipeline and ft connection；Generator (1) Also concentrated solution pipeline is through solution pump (7), solution heat exchanger (10) and the second solution heat exchanger (11) and the second generator (2) connect, the second generator (2) also has concentrated solution pipeline to be connected with absorber (3) through the second solution heat exchanger (11), absorb Device (3) also has weak solution pipeline to be connected with the second absorber (4) through the second solution pump (8) and the 3rd solution heat exchanger (18), Second absorber (4) also has weak solution pipeline to be connected with the 3rd absorber (16) through the 3rd solution heat exchanger (18), and the 3rd inhales Receive device (16) and also have weak solution pipeline through the 3rd solution pump (17) and the 4th solution heat exchanger (23) and the 4th absorber (22) Connection, the 4th absorber (22) also has weak solution pipeline through the 4th solution heat exchanger (23) and solution heat exchanger (10) and hair Raw device (1) connection, 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 connect through cryogen liquid pump (9) and evaporator (6) Logical, evaporator (6) also has refrigerant steam channel to be connected with absorber (3) and the 3rd absorber (16) respectively, and condenser (5) also has The 3rd absorber (16) has cryogen to steam again after cryogen liquid pipeline is connected through the second cryogen liquid pump (20) with the 3rd absorber (16) Vapour passage is connected with the 4th absorber (22), and condenser (5) also has cooling medium pipeline and ft connection, absorber (3), second Absorber (4) and the 4th absorber (22) also have heated medium pipeline and ft connection respectively, and heat exchanger (12) also has quilt Heating medium pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 26. heat, is in the dynamic co-feeding system of heat described in claim 25, to cancel evaporator, by engine (13) have exhaust passage to be sequentially communicated generator (1) and the finisher (6) of evaporator (6) has condensate liquid pipeline to connect with outside again It is logical to be adjusted to generator (1) after engine (13) has exhaust passage connect with generator (1) and have condensate liquid pipeline and outside again Connection, has refrigerant steam channel to connect and be adjusted to engine with absorber (3) and the 3rd absorber (16) respectively evaporator (6) (13) set up exhaust passage to be connected with absorber (3) and the 3rd absorber (16) respectively, there is cryogen liquid pipeline to pass through condenser (5) Cryogen liquid pump (9) connects with evaporator (6) and is adjusted to condenser (5) and has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, Form the dynamic co-feeding system of heat.
The 27. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second cryogen liquid pump, the 4th absorber and the 4th solution heat Exchanger is constituted；Engine (13) connects working machine (14), and engine (13) has live steam passage and ft connection, engine (13) or also exhaust passage and ft connection, engine (13) also have exhaust passage to be connected with generator (1) after generator (1) evaporated after thering is condensate liquid pipeline and ft connection, engine (13) to also have the second steam channel to be connected with evaporator (6) again Device (6) has the second condensate liquid pipeline and ft connection again, and engine (13) also has the 3rd steam channel to be sequentially communicated the second generation Device (2) and heat exchanger (12), heat exchanger (12) also have the 3rd condensate liquid pipeline and ft connection；Generator (1) is also dense Solution line connects through solution pump (7), solution heat exchanger (10) and the second solution heat exchanger (11) and the second generator (2) Logical, the second generator (2) also has concentrated solution pipeline to be connected with absorber (3) through the second solution heat exchanger (11), absorber (3) Also weak solution pipeline is connected through the second solution pump (8) and the 3rd solution heat exchanger (18) with the second absorber (4), and second inhales Receiving device (4) also has weak solution pipeline to be connected with the 3rd absorber (16) through the 3rd solution heat exchanger (18), the 3rd absorber (16) weak solution pipeline is connected with the 4th absorber (22) through the 3rd solution pump (17) and the 4th solution heat exchanger (23), 4th absorber (22) also has weak solution pipeline through the 4th solution heat exchanger (23) and solution heat exchanger (10) and generator (1) connect, 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 Vapour passage is connected with condenser (5), and condenser (5) also has cryogen liquid pipeline to be connected with evaporator (6) through cryogen liquid pump (9), is steamed Hair device (6) also has refrigerant steam channel to be connected with absorber (3) and the 3rd absorber (16) respectively, and condenser (5) also has cryogen The 3rd absorber (16) has refrigerant vapour to lead to again after liquid pipeline is connected through the second cryogen liquid pump (20) with the 3rd absorber (16) Road is connected with the 4th absorber (22), and condenser (5) also has cooling medium pipeline and ft connection, and absorber (3), second absorb Device (4) and the 4th absorber (22) 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.
The dynamic co-feeding system of 28. heat, is in the dynamic co-feeding system of heat described in claim 27, 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 with ft connection, steaming again Hair device (6) has refrigerant steam channel to connect and be adjusted in the lump engine (13) with absorber (3) and the 3rd absorber (16) respectively There is the second steam channel to be connected with absorber (3) and the 3rd absorber (16) respectively, condenser (5) is had into cryogen liquid pipeline through cold Agent liquid pump (9) connects with evaporator (6) and is adjusted to condenser (5) and has cryogen liquid pipeline through cryogen liquid pump (9) and ft connection, shape Into the dynamic co-feeding system of heat.
The 29. dynamic co-feeding systems 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, the second solution heat exchanger, heat exchanger, engine, work Machine, the 3rd absorber, the 3rd solution pump, the 3rd solution heat exchanger, the second evaporator, the second cryogen liquid pump, the 4th absorber, 4th solution heat exchanger and the 3rd cryogen liquid pump are constituted；Engine (13) connects working machine (14), and engine (13) has newly Vapour passage and ft connection, engine (13) or also exhaust passage and ft connection, engine (13) also have exhaust passage according to The second evaporator (19) has condensate liquid pipeline and ft connection again after secondary connection generator (1) and the second evaporator (19), moves Power machine (13) also have the finisher (6) that the second steam channel is connected with evaporator (6) have again the second condensate liquid pipeline with it is outside Connection, engine (13) also has the 3rd steam channel to be sequentially communicated the second generator (2) and heat exchanger (12), heat exchanger (12) there are the 3rd condensate liquid pipeline and ft connection；Generator (1) also has concentrated solution pipeline to be handed over through solution pump (7), solution heat Parallel operation (10) and the second solution heat exchanger (11) are connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline Connected with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline through the second solution pump (8) Connected with the second absorber (4) with the 3rd solution heat exchanger (18), the second absorber (4) also has weak solution pipeline molten through the 3rd Liquid heat exchanger (18) is connected with the 3rd absorber (16), and the 3rd absorber (16) also has weak solution pipeline through the 3rd solution pump (17) connected with the 4th absorber (22) with the 4th solution heat exchanger (23), the 4th absorber (22) also has weak solution pipeline to pass through 4th solution heat exchanger (23) and solution heat exchanger (10) are connected with generator (1), and the second generator (2) also has cryogen to steam Vapour passage is connected with the second absorber (4), and generator (1) 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) also have cryogen liquid pipeline to be connected with the 3rd absorber (16) through the second cryogen liquid pump (20) after the 3rd Absorber (16) has refrigerant steam channel to be connected with the 4th absorber (22) again, and condenser (5) also has cryogen liquid pipeline through the 3rd Cryogen liquid pump (24) is connected with the second evaporator (19), and the second evaporator (19) also has refrigerant steam channel and the 3rd absorber (16) connect, condenser (5) also has cooling medium pipeline and ft connection, absorber (3), the second absorber (4) and the 4th inhale Receive device (22) also has heated medium pipeline and ft connection respectively, and heat exchanger (12) also has heated medium pipeline with outside Connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 30. heat, is in the dynamic co-feeding system of heat described in claim 29, to cancel evaporator and the second evaporation Device, by engine (13) have the finisher (6) that the second steam channel is connected with evaporator (6) have again the second condensate liquid pipeline with Ft connection, evaporator (6) have refrigerant steam channel to be connected with absorber (3) be adjusted in the lump engine (13) and have the second steam Passage is connected with absorber (3), by engine (13) have exhaust passage be sequentially communicated generator (1) and the second evaporator (19) it The second evaporator (19) has cryogen liquid pipeline to be adjusted to engine (13) with ft connection and has exhaust passage and generator (1) again afterwards Generator (1) has cryogen liquid pipeline and ft connection again after connection, and the second evaporator (19) is had into refrigerant steam channel and the Three absorbers (16) connection is adjusted to engine (13) and sets up exhaust passage to be connected with the 3rd absorber (16), by condenser (5) There is cryogen liquid pipeline to be connected 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, cryogen liquid pipeline connects tune with the second evaporator (19) through the 3rd cryogen liquid pump (24) condenser (5) It is whole for condenser (5) has cryogen liquid pipeline through the 3rd cryogen liquid pump (24) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 31. heat, is in the dynamic alliance system of any hot described in claim 1-2,5-6,11-12,19-20,25-26 In system, cancel heat exchanger, engine (13) is had the second steaming by the heated medium pipeline that cancellation is connected with heat exchanger (12) Vapour passage is sequentially communicated the second generator (2) and heat exchanger (12), heat exchanger (12) has the second condensate liquid pipeline with outside Connection is adjusted to after engine (13) has the second steam channel to be connected with the second generator (2) the second generator (2) again in the lump There are the second condensate liquid pipeline and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 32. heat, is in the dynamic alliance of any hot described in claim 3-4,7-10,13-18,21-24,27-29 In system, cancel heat exchanger, engine (13) is had the 3rd by the heated medium pipeline that cancellation is connected with heat exchanger (12) Steam channel is sequentially communicated the second generator (2) and heat exchanger (12), heat exchanger (12) have the 3rd condensate liquid pipeline with it is outer Portion's connection is adjusted to the second generator (2) after engine (13) has the 3rd steam channel to be connected with the second generator (2) in the lump There are the 3rd condensate liquid pipeline and ft connection again, form the dynamic co-feeding system of heat.
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CN106352591B (en) * 2016-05-30 2020-01-31 李华玉 Combined heat and power system
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CN106403351B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system
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Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0518833B1 (en) * 1991-06-13 1998-05-13 Enea Ente Per Le Nuove Tecnologie, L'energia E L'ambiente Heat pump for heating or refrigerating buildings and delivering in combination hot water for sanitary fixtures
JP2001099520A (en) * 1999-09-29 2001-04-13 Osaka Gas Co Ltd Hybrid absorbing type electrical power and cold heat or hot heat supplying device
CN1811303A (en) * 2006-02-18 2006-08-02 李华玉 Single-effect heat pump/double-effect cooling absorption set and combined heat, electricity and cold supply system
CN1912499A (en) * 2006-08-11 2007-02-14 李华玉 Open-type first kind absorption heat pump and its application technology
CN1967055A (en) * 2006-08-25 2007-05-23 李华玉 Backheating and heating technology by using residual heat of exhaust steam in steam power cycle
US8601825B2 (en) * 2007-05-15 2013-12-10 Ingersoll-Rand Company Integrated absorption refrigeration and dehumidification system

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