CN104654658B - The dynamic co-feeding system of heat - Google Patents

The dynamic co-feeding system of heat Download PDF

Info

Publication number
CN104654658B
CN104654658B CN201510043114.9A CN201510043114A CN104654658B CN 104654658 B CN104654658 B CN 104654658B CN 201510043114 A CN201510043114 A CN 201510043114A CN 104654658 B CN104654658 B CN 104654658B
Authority
CN
China
Prior art keywords
absorber
solution
pipeline
connection
evaporator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510043114.9A
Other languages
Chinese (zh)
Other versions
CN104654658A (en
Inventor
李华玉
Original Assignee
李华玉
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to CN2014100467269 priority Critical
Priority to CN201410046726 priority
Application filed by 李华玉 filed Critical 李华玉
Priority to CN201510043114.9A priority patent/CN104654658B/en
Publication of CN104654658A publication Critical patent/CN104654658A/en
Application granted granted Critical
Publication of CN104654658B publication Critical patent/CN104654658B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems
    • Y02B30/625Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration

Abstract

The present invention provides heat dynamic co-feeding system, belongs to the dynamic alliance of heat and technical field of heat pumps.Engine provides steam discharge to occurring evaporator, heat exchanger provides the second steam, steam chest is divided to connect absorber with solution heat exchanger through solution pump, absorber is through solution heat exchanger, solution choke valve connects a point steam chest with occurring evaporator, steam chest is divided to have refrigerant steam channel to connect the second absorber, second absorber is through the second solution pump, second solution heat exchanger connects second point of steam chest with occurring evaporator, second point of steam chest connects the second absorber through the second solution heat exchanger, second point of steam chest has refrigerant steam channel to connect condenser, condenser connects absorber through cryogen liquid pump with occurring evaporator, condenser and the second absorber have cooling medium pipeline and ft connection, absorber and heat exchanger have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.

Description

The dynamic co-feeding system of heat
Technical field:
The invention belongs to heat-electricity-cold combined supply and technical field of heat pumps.
Background technology:
Made with vapor in the thermodynamic cycle device of circulatory mediator, to make engine (steam turbine) that there is higher inside heat Efficiency and its property safe and reliable to operation of increase, then require that the pressure and temperature of engine outlet exhaust steam can not be too low;So in the winter Ji Shijie, environment temperature is relatively low, and engine outlet exhaust steam temperature is higher, then will have about 40 DEG C of even more highs therebetween The temperature difference can not be used;Furthermore, in the Steam Power Circulation system by representative of Thermal Power Station, although the grade of exhaust steam is very It is low, but its thermic load also having is often very abundant, if being subject to effectively using then significant.
Be currently used for winter heating heat move alliance, also or have other heat supply purposes heat move alliance, corresponding technical side Case is generally comprised:(1) improve engine outlet steam discharge parameter and carry out heat supply;(2) drawn gas using engine intermediate extraction or segmentation Carry out heat supply;(3) it is the high temperature heat source of first-class absorption type heat pump come recovery section exhaust steam heat to use engine intermediate extraction Carry out heat supply.But, all cold environment is not made full use of in the dynamic jointly-supplying technology measure of these heat.
Using second-kind absorption-type heat pump principle, the temperature difference between engine exhaust steam and cold environment is made full use of, and consider Follow thermal energy step and utilize principle, second-kind absorption-type heat pump heat supply is combined with engine heating of drawing gas, to meet difference In the case of heat demand and realize heat energy utilization rationalization --- this can not only realize effective utilization of the temperature difference, Er Qieneng Operation interval of the engine blade in wet-steam region is enough reduced or eliminated, increases the inside thermal efficiency of engine.
Due to being related to temperature difference size, cold ambient temperature between heat user thermal parameter and thermic load, exhaust steam and cold environment Height, a variety of specific operating modes such as the thermic load that contains of exhaust steam is how many, and consider the adaptation to existing heat power generating system, because This needs a variety of specific technical schemes.
The content of the invention:
Present invention is primarily intended to provide heat dynamic co-feeding system, specific content of the invention subitem is described below:
1. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Exchanger, solution choke valve, point steam chest, heat exchanger, engine and a working machine are constituted;Engine connects working machine, power Machine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine also has exhaust passage and hair Life-evaporator is connected, and generation-evaporator also has condensate liquid pipeline and ft connection, and engine also has the second steam channel and heat Exchanger is connected, and heat exchanger also has the second condensate liquid pipeline and ft connection;Point steam chest have concentrated solution pipeline through solution pump and Solution heat exchanger is connected with absorber, absorber also have weak solution pipeline through solution heat exchanger, solution choke valve and generation- Evaporator is connected with a point steam chest, and a point steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline warp Generation-evaporator has refrigerant steam channel to be connected with absorber again after cryogen liquid pump is connected with generation-evaporator, and condenser is also There are cooling medium pipeline and ft connection, absorber also has heated medium pipeline and ft connection, and heat exchanger, which also has, to be added Heat medium pipeline and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, is that in the heat described in the 1st moves co-feeding system, condenser is had into cryogen liquid pipeline through cold Generation-evaporator has refrigerant steam channel to be connected with absorber and is adjusted to condense again after agent liquid pump is connected with generation-evaporator Device has cryogen liquid pipeline through cryogen liquid pump and ft connection, and engine is set up exhaust passage and connected with absorber, forms the dynamic connection of heat For system.
3. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator and an evaporator are constituted;Engine connects working machine, Engine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine also has exhaust passage Connected with generator, generator also has condensate liquid pipeline and ft connection, engine also has the second steam channel to connect with evaporator Logical finisher has the second condensate liquid pipeline and ft connection again, and engine also has the 3rd steam channel to connect with heat exchanger Logical, heat exchanger also has the 3rd condensate liquid pipeline and ft connection;Steam chest is divided to have concentrated solution pipeline to be handed over through solution pump and solution heat Parallel operation is connected with absorber, and absorber also has weak solution pipeline through solution heat exchanger, solution choke valve and generator and a point vapour Room is connected, and a point steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump with steaming Device connection is sent out, evaporator also has refrigerant steam channel to be connected with absorber, and condenser also has cooling medium pipeline and ft connection, Absorber also has heated medium pipeline and ft connection, and heat exchanger also has heated medium pipeline and ft connection, is formed The dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, is in the heat described in the 3rd moves co-feeding system, to cancel evaporator, engine is had the The finisher that two steam channels are connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have refrigerant vapour again Passage is connected with absorber to be adjusted to engine and has the second steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid pipe Road is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat dynamic Co-feeding system.
5. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat It is exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, second molten Liquid heat exchanger and second point of steam chest are constituted;Engine connects working machine, and engine has live steam passage and ft connection, power Machine or also exhaust passage and ft connection, engine also have exhaust passage to be connected with generation-evaporator, and generation-evaporator is also There are condensate liquid pipeline and ft connection, engine also has the second steam channel to be connected with heat exchanger, and heat exchanger also has second Condensate liquid pipeline and ft connection;Divide steam chest to there is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, inhale Receiving device also has weak solution pipeline to be connected through solution heat exchanger, solution choke valve and generation-evaporator with a point steam chest, and point steam chest is also There is refrigerant steam channel to be connected with the second absorber, the second absorber also has weak solution pipeline through the second solution pump, the second solution Heat exchanger and generation-evaporator are connected with second point of steam chest, and second point of steam chest also has concentrated solution pipeline to be handed over through the second solution heat Parallel operation is connected with the second absorber, and second point of steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid Generation-evaporator has refrigerant steam channel to be connected with absorber again after pipeline is connected through cryogen liquid pump with generation-evaporator, cold Condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber also has heated medium pipeline and outside Connection, heat exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, is that in the heat described in the 5th moves co-feeding system, condenser is had into cryogen liquid pipeline through cold Generation-evaporator has refrigerant steam channel to be connected with absorber and is adjusted to condense again after agent liquid pump is connected with generation-evaporator Device has cryogen liquid pipeline through cryogen liquid pump and ft connection, and engine is set up exhaust passage and connected with absorber, forms the dynamic connection of heat For system.
7. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second Solution heat exchanger and second point of steam chest are constituted;Engine connects working machine, and engine has live steam passage and ft connection, moves Power machine or also exhaust passage and ft connection, engine also have exhaust passage to be connected with generator, and generator also has condensate liquid Pipeline and ft connection, the finisher that engine also has the second steam channel to be connected with evaporator have the second condensate liquid pipeline again With ft connection, engine also has the 3rd steam channel to be connected with heat exchanger, heat exchanger also have the 3rd condensate liquid pipeline with Ft connection;Steam chest is divided to have concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorber also has dilute molten Liquid pipeline connect through solution heat exchanger, solution choke valve and generator with a point steam chest, a point steam chest also have refrigerant steam channel and Second absorber is connected, and the second absorber also has weak solution pipeline through the second solution pump, the second solution heat exchanger and generator Connected with second point of steam chest, second point of steam chest also has concentrated solution pipeline to be connected through the second solution heat exchanger with the second absorber, Second point of steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and evaporator Connection, evaporator also has refrigerant steam channel to be connected with absorber, and condenser and the second absorber also have cooling medium pipe respectively Road and ft connection, absorber also have heated medium pipeline and ft connection, heat exchanger also have heated medium pipeline with Ft connection, forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is in the heat described in the 7th moves co-feeding system, to cancel evaporator, engine is had the The finisher that two steam channels are connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have refrigerant vapour again Passage is connected with absorber to be adjusted to engine and has refrigerant steam channel to be connected with absorber in the lump, forms the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, Second solution heat exchanger and second point of steam chest are constituted;Engine connects working machine, and engine has live steam passage to connect with outside Logical, engine or also exhaust passage and ft connection, engine also have exhaust passage to be connected with generator, and generator is also cold Lime set pipeline and ft connection, engine also have the second steam channel to be connected with generation-evaporator, and generation-evaporator also has Two condensate liquid pipelines and ft connection, engine also have the 3rd steam channel to be connected with heat exchanger, and heat exchanger also has the 3rd Condensate liquid pipeline and ft connection;Divide steam chest to there is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, inhale Receiving device also has weak solution pipeline to be connected through solution heat exchanger, solution choke valve and generation-evaporator with a point steam chest, and point steam chest is also There is refrigerant steam channel to be connected with the second absorber, the second absorber also has weak solution pipeline through the second solution pump, the second solution Heat exchanger and generator are connected with second point of steam chest, second point of steam chest also have concentrated solution pipeline through the second solution heat exchanger with Second absorber is connected, and second point of steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline warp Generation-evaporator has refrigerant steam channel to be connected with absorber again after cryogen liquid pump is connected with generation-evaporator, condenser and Second absorber also has cooling medium pipeline and ft connection respectively, and absorber also has heated medium pipeline and ft connection, Heat exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is that in the heat described in the 9th moves co-feeding system, condenser is had into cryogen liquid pipeline warp Generation-evaporator has refrigerant steam channel to connect with absorber to be adjusted to cold again after cryogen liquid pump is connected with generation-evaporator Condenser has cryogen liquid pipeline through cryogen liquid pump and ft connection, and engine is set up the second steam channel and connected with absorber, is formed The dynamic co-feeding system of heat.
11. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point vapour Room, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution heat exchange Device and the second generator are constituted;Engine connects working machine, and engine has live steam passage and a ft connection, engine or also has Exhaust passage and ft connection, engine also have exhaust passage to be connected with generator, and generator also has condensate liquid pipeline and outside Connection, engine also has the second steam channel to be sequentially communicated the second generator and the finisher of evaporator the second condensate liquid again Pipeline and ft connection, engine also have the 3rd steam channel to be connected with heat exchanger, and heat exchanger also has the 3rd condensate line Road and ft connection;Second generator also has concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorbs Device also has weak solution pipeline to be connected through solution heat exchanger with the second generator, and the second generator also has refrigerant steam channel and the Two absorbers connect, the second absorber also have weak solution pipeline through the second solution pump, the second solution heat exchanger and generator with Divide steam chest connection, a point steam chest also has concentrated solution pipeline to be connected through the second solution heat exchanger with the second absorber, and a point steam chest also has Refrigerant steam channel is connected with condenser, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator is also There is refrigerant steam channel to be connected with absorber, condenser and the second absorber also have cooling medium pipeline and ft connection respectively, Absorber also has heated medium pipeline and ft connection, and heat exchanger also has heated medium pipeline and ft connection, is formed The dynamic co-feeding system of heat.
12. the dynamic co-feeding system of heat, is in the heat described in the 11st moves co-feeding system, to cancel evaporator, engine is had Second steam channel is sequentially communicated the second generator and the finisher of evaporator the second condensate liquid pipeline and ft connection again Be adjusted to engine have the second steam channel connected with the second generator after the second generator have again the second condensate liquid pipeline with Ft connection, by evaporator have refrigerant steam channel connected with absorber be adjusted to engine set up the second steam channel with absorption Device is connected, and is had cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator 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.
13. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second Solution heat exchanger, second point of steam chest and the second generator are 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 connected with generator, generator Also condensate liquid pipeline and ft connection, engine also have the second steam channel to be connected with the second generator, and the second generator is also There are the second condensate liquid pipeline and ft connection, the finisher that engine also has the 3rd steam channel to be connected with evaporator has again Three condensate liquid pipelines and ft connection, engine also have the 4th steam channel to be connected with heat exchanger, and heat exchanger also has the 4th Condensate liquid pipeline and ft connection;Divide steam chest to there is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, inhale Receiving device also has weak solution pipeline to be connected through solution heat exchanger, solution choke valve and the second generator with a point steam chest, and point steam chest is also There is refrigerant steam channel to be connected with the second absorber, the second absorber also has weak solution pipeline through the second solution pump, the second solution Heat exchanger and generator are connected with second point of steam chest, second point of steam chest also have concentrated solution pipeline through the second solution heat exchanger with Second absorber is connected, and second point of steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline warp Cryogen liquid pump is connected with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber, and condenser and the second absorber are also There are cooling medium pipeline and ft connection respectively, absorber also has heated medium pipeline and ft connection, and heat exchanger also has Heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
14. the dynamic co-feeding system of heat, is in the heat described in the 13rd moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
15. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point vapour Room, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution heat exchange Device and the second generator are constituted;Engine connects working machine, and engine has live steam passage and a ft connection, engine or also has Exhaust passage and ft connection, engine also have exhaust passage to be connected with generator, and generator also has condensate liquid pipeline and outside Connection, engine also have the second steam channel connected with the second generator after the second generator have again the second condensate liquid pipeline and Ft connection, the finisher that engine also has the 3rd steam channel to be connected with evaporator has the 3rd condensate liquid pipeline and outside again Connection, engine also has the 4th steam channel to be connected with heat exchanger, and heat exchanger also has the 4th condensate liquid pipeline to connect with outside It is logical;Second generator also has concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, and absorber also has dilute molten Liquid pipeline is connected through solution heat exchanger with the second generator, and the second generator also has refrigerant steam channel to connect with the second absorber Logical, the second absorber also has weak solution pipeline to be connected through the second solution pump, the second solution heat exchanger and generator with a point steam chest, Steam chest is divided to also have concentrated solution pipeline to be connected through the second solution heat exchanger with the second absorber, a point steam chest also has refrigerant vapour to lead to Road is connected with condenser, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator also has refrigerant vapour Passage is connected with absorber, and condenser and the second absorber also have cooling medium pipeline and ft connection respectively, and absorber also has Heated medium pipeline and ft connection, heat exchanger also have heated medium pipeline and ft connection, form the dynamic alliance system of heat System.
16. the dynamic co-feeding system of heat, is in the heat described in the 15th moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
17. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution Heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump and second Steam chest is divided to be constituted;Engine connects working machine, and engine has live steam passage and ft connection, also engine or exhaust passage With ft connection, engine also has exhaust passage to be connected with generation-evaporator, and generation-evaporator also has condensate liquid pipeline and outer Portion is connected, and engine also has the second steam channel to be connected with heat exchanger, and heat exchanger also has the second condensate liquid pipeline and outside Connection;Steam chest is divided to have concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorber also has weak solution pipe Road is connected through solution heat exchanger with the second absorber, the second absorber also have weak solution pipeline through the second solution pump and occur- Evaporator is connected with second point of steam chest, and second point of steam chest also has concentrated solution pipeline through solution choke valve and generation-evaporator with dividing Steam chest is connected, and a point steam chest also has refrigerant steam channel to be connected with the second absorber, second point of steam chest also have refrigerant steam channel and Condenser connect, condenser also have cryogen liquid pipeline connected through cryogen liquid pump with generation-evaporator after generation-evaporator have again Refrigerant steam channel is connected with absorber, and condenser and the second absorber also have cooling medium pipeline and ft connection respectively, is inhaled Receive device and also have heated medium pipeline and ft connection, heat exchanger also has heated medium pipeline and ft connection, forms heat Dynamic co-feeding system.
18. the dynamic co-feeding system of heat, is that in the heat described in the 17th moves co-feeding system, condenser is had into cryogen liquid pipeline warp Generation-evaporator has refrigerant steam channel to connect with absorber to be adjusted to cold again after cryogen liquid pump is connected with generation-evaporator Condenser has cryogen liquid pipeline through cryogen liquid pump and ft connection, and engine is set up exhaust passage and connected with absorber, forms heat dynamic Co-feeding system.
19. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution Heat exchanger, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution Heat exchanger and second point of steam chest are constituted;Engine connects working machine, and engine has live steam passage and ft connection, engine Or also exhaust passage and ft connection, engine also has exhaust passage to be connected with generator, and generator also has condensate liquid pipeline With ft connection, engine also has the second steam channel generation-evaporator connection, and generation-evaporator also has the second condensate line Road and ft connection, engine also have the 3rd steam channel to be connected with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline With ft connection;Steam chest is divided to have concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorber is also dilute Solution line is connected through solution heat exchanger with the second absorber, the second absorber also have weak solution pipeline through the second solution pump, Second solution heat exchanger and generation-evaporator are connected with second point of steam chest, and second point of steam chest also has concentrated solution pipeline through second Solution heat exchanger and generator are connected with a point steam chest, and a point steam chest also has refrigerant steam channel to be connected with the second absorber, and second Steam chest is divided to also have refrigerant steam channel to be connected with condenser, condenser also has cryogen liquid pipeline through cryogen liquid pump and generation-evaporation Generation-evaporator has refrigerant steam channel to be connected with absorber again after device connection, and condenser and the second absorber also have respectively Cooling medium pipeline and ft connection, absorber also have heated medium pipeline and ft connection, and heat exchanger also has heated Medium pipeline and ft connection, form the dynamic co-feeding system of heat.
20. the dynamic co-feeding system of heat, is that in the heat described in the 19th moves co-feeding system, condenser is had into cryogen liquid pipeline warp Generation-evaporator has refrigerant steam channel to connect with absorber to be adjusted to cold again after cryogen liquid pump is connected with generation-evaporator Condenser has cryogen liquid pipeline through cryogen liquid pump and ft connection, and engine is set up the second steam channel and connected with absorber, is formed The dynamic co-feeding system of heat.
21. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution Heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution Pump, the second solution heat exchanger and the second cryogen liquid pump are constituted;Engine connects working machine, and engine has live steam passage and outer Portion is connected, and engine or also exhaust passage and ft connection, engine also have exhaust passage to be connected with generation-evaporator, is sent out Life-evaporator also has condensate liquid pipeline and ft connection, and engine also has the second steam channel to be connected with heat exchanger, heat exchange Device also has the second condensate liquid pipeline and ft connection;Steam chest is divided to have concentrated solution pipeline through solution pump and solution heat exchanger and absorption Device is connected, and absorber also has weak solution pipeline to connect through solution heat exchanger, solution choke valve and generation-evaporator with point steam chest It is logical, a point steam chest also have refrigerant steam channel connected with generator after generator have cryogen liquid pipeline and the second cryogen liquid pump company again It is logical, the second cryogen liquid pump also have cryogen liquid pipeline connected with generation-evaporator after generation-evaporator have refrigerant steam channel again Connected with absorber;Generator also has concentrated 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 through the second solution heat exchanger with generator, and generator also has refrigerant vapour Passage is connected with condenser, condenser also have cryogen liquid pipeline connected through cryogen liquid pump with generation-evaporator after generation-evaporation Device has refrigerant steam channel to be connected with the second absorber again, and condenser also has cooling medium pipeline and ft connection, absorber and Second 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.
22. the dynamic co-feeding system of heat, is that in the heat described in the 21st moves co-feeding system, the second cryogen liquid pump is had into cryogen liquid After pipeline is connected with generation-evaporator generation-evaporator there is refrigerant steam channel to be connected with absorber again to be adjusted to second cold Agent liquid pump has cryogen liquid pipeline and ft connection, and engine is set up exhaust passage and connected with absorber, forms the dynamic co-feeding system of heat.
23. the dynamic co-feeding system of heat, is that in the heat described in the 21st moves co-feeding system, the second cryogen liquid pump is had into cryogen liquid After pipeline is connected with generation-evaporator generation-evaporator there is refrigerant steam channel to be connected with absorber again to be adjusted to second cold Agent liquid pump has cryogen liquid pipeline and ft connection, has cryogen liquid pipeline to be connected through cryogen liquid pump with generation-evaporator condenser Generation-evaporator has refrigerant steam channel to be connected with the second absorber and is adjusted to condenser and has cryogen liquid pipeline through cryogen again afterwards Liquid pump and ft connection, engine are set up exhaust passage and connected respectively with absorber and the second absorber, form the dynamic alliance system of heat System.
24. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution Heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the Two solution pumps, the second solution heat exchanger and the second cryogen liquid pump are constituted;Engine connects working machine, and engine has live steam to lead to Road and ft connection, also engine or exhaust passage and ft connection, engine also have exhaust passage to connect with generation-evaporator Logical, generation-evaporator also has condensate liquid pipeline and ft connection, and engine also has after the second steam channel connects with evaporator Evaporator has the second condensate liquid pipeline and ft connection again, and engine also has the 3rd steam channel to be connected with heat exchanger, and heat is handed over Parallel operation also has the 3rd condensate liquid pipeline and ft connection;Steam chest is divided to have concentrated solution pipeline through solution pump and solution heat exchanger and suction Device connection is received, absorber also has weak solution pipeline to connect through solution heat exchanger, solution choke valve and generation-evaporator with point steam chest It is logical, a point steam chest also have refrigerant steam channel connected with generator after generator have cryogen liquid pipeline through the second cryogen liquid pump again and Evaporator is connected, and evaporator also has refrigerant steam channel to be connected with absorber;Generator also has concentrated solution pipeline through 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 to be handed over through the second solution heat Parallel operation is connected with generator, and generator also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline through cold Generation-evaporator has refrigerant steam channel to be connected with the second absorber again after agent liquid pump is connected with generation-evaporator, condenser Also cooling medium pipeline and ft connection, absorber and the second absorber also have heated medium pipeline to connect with outside respectively Logical, heat exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
25. the dynamic co-feeding system of heat, is in the heat described in the 24th moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the second steam channel to be connected with absorber in the lump, and generator is had into cryogen liquid Pipeline is connected through the second cryogen liquid pump with evaporator to be adjusted to generator and has cryogen liquid pipeline to connect through the second cryogen liquid pump with outside It is logical, form the dynamic co-feeding system of heat.
26. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second Solution heat exchanger, the second generator, the second cryogen liquid pump and the second evaporator are constituted;Engine connects working machine, power Machine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine also has exhaust passage and hair Raw device connection, generator also has condensate liquid pipeline and ft connection, and engine also has the second steam channel to be sequentially communicated evaporator There are the second condensate liquid pipeline and ft connection again with the second evaporator after the second evaporator, engine also has the 3rd steam channel Connected with heat exchanger, heat exchanger also has the 3rd condensate liquid pipeline and ft connection;Steam chest is divided to have concentrated solution pipeline through solution Pump and solution heat exchanger are connected with absorber, absorber also have weak solution pipeline through solution heat exchanger, solution choke valve and Generator connect with a point steam chest, divide a steam chest also have refrigerant steam channel connected with the second generator after the second generator have cold again Agent liquid pipeline is connected through the second cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber;Second hair Raw device also has concentrated solution pipeline to be connected through the second solution pump and the second solution heat exchanger with the second absorber, and the second absorber is also There is weak solution pipeline to be connected through the second solution heat exchanger with the second generator, the second generator also have refrigerant steam channel with it is cold Condenser is connected, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with the second evaporator, and the second evaporator also has cryogen steaming Vapour passage is connected with the second absorber, and condenser also has cooling medium pipeline and ft connection, and absorber and the second absorber are also There are heated medium pipeline and ft connection respectively, heat exchanger also has heated medium pipeline and ft connection, forms heat dynamic Co-feeding system.
27. the dynamic co-feeding system of heat, is in the heat described in the 26th moves co-feeding system, to cancel evaporator, engine is had The second evaporator has the second condensate liquid pipeline and outside again after second steam channel is sequentially communicated evaporator and the second evaporator Connection be adjusted to engine have the second steam channel connected with the second evaporator after the second evaporator have the second condensate line again Road and ft connection, by evaporator have refrigerant steam channel connected with absorber be adjusted to engine set up the second steam channel with Absorber is connected, and is had cryogen liquid pipeline to be connected through the second cryogen liquid pump with evaporator in the second generator and is adjusted to the second generator There is cryogen liquid pipeline through the second cryogen liquid pump and ft connection, form the dynamic co-feeding system of heat.
28. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second Solution heat exchanger, the second generator, the second cryogen liquid pump and the second evaporator are constituted;Engine connects working machine, power Machine has live steam passage and ft connection, also engine or exhaust passage and ft connection, and engine also has exhaust passage and hair Raw device connection, generator also has condensate liquid pipeline and ft connection, and engine also has the second steam channel and the second evaporator to connect Second evaporator has the second condensate liquid pipeline and ft connection again after logical, and engine also has the 3rd steam channel to connect with evaporator Logical finisher has the 3rd condensate liquid pipeline and ft connection again, and engine also has the 4th steam channel to connect with heat exchanger Logical, heat exchanger also has the 4th condensate liquid pipeline and ft connection;Steam chest is divided to have concentrated solution pipeline to be handed over through solution pump and solution heat Parallel operation is connected with absorber, and absorber also has weak solution pipeline through solution heat exchanger, solution choke valve and generator and a point vapour Room is connected, a point steam chest also have refrigerant steam channel connected with the second generator after the second generator have cryogen liquid pipeline again through the Two cryogen liquid pumps are connected with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber;Second generator also has dense 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 through the second solution heat exchanger with the second generator, the second generator also has refrigerant steam channel to be connected with condenser, cold Condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with the second evaporator, and the second evaporator also has refrigerant steam channel and second Absorber is connected, and condenser also has cooling medium pipeline and ft connection, and absorber and the second 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.
29. the dynamic co-feeding system of heat, is in the heat described in the 28th moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the 3rd steam channel to be connected with absorber in the lump, and the second generator is had into cold Agent liquid pipeline is connected through the second cryogen liquid pump with evaporator to be adjusted to the second generator and has cryogen liquid pipeline through the second cryogen liquid pump With ft connection, the dynamic co-feeding system of heat is formed.
30. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second Solution heat exchanger, the second generator and the second cryogen liquid pump are constituted;Engine connects working machine, and engine has live steam passage With ft connection, engine or also exhaust passage and ft connection, engine also have exhaust passage to be connected with generator, occur Device also has condensate liquid pipeline and ft connection, and the finisher that engine also has the second steam channel to be connected with evaporator has again Two condensate liquid pipelines and ft connection, engine also have the 3rd steam channel to be connected with heat exchanger, and heat exchanger also has the 3rd Condensate liquid pipeline and ft connection;Divide steam chest to there is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, inhale Receiving device also has weak solution pipeline to be connected through solution heat exchanger, solution choke valve and generator with a point steam chest, and point steam chest is also cold The second generator has cryogen liquid pipeline through the second cryogen liquid pump and evaporator again after agent steam channel is connected with the second generator Connection;Second generator also has concentrated solution pipeline to be connected through the second solution pump and the second solution heat exchanger with the second absorber, Second absorber also has weak solution pipeline to be connected through the second solution heat exchanger with the second generator, and the second generator also has cryogen Steam channel is connected with condenser, and condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, and evaporator is also cold Agent steam channel is connected with absorber and the second absorber respectively, and condenser also has cooling medium pipeline and ft connection, is absorbed Device and the second absorber also have heated medium pipeline and ft connection respectively, and heat exchanger also has heated medium pipeline and outer Portion is connected, and forms the dynamic co-feeding system of heat.
31. the dynamic co-feeding system of heat, is in the heat described in the 30th moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage connected respectively with absorber and the second absorber be adjusted in the lump engine have the second steam channel respectively with absorber Connected with the second absorber, there is cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator condenser and be adjusted to condenser and have cryogen Second generator is had cryogen liquid pipeline to be connected through the second cryogen liquid pump with evaporator by liquid pipeline through cryogen liquid pump and ft connection Being adjusted to the second generator has cryogen liquid pipeline through the second cryogen liquid pump and ft connection, forms the dynamic co-feeding system of heat.
32. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution Heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, second Solution heat exchanger, the second cryogen liquid pump and the 3rd absorber are constituted;Engine connects working machine, and engine has live steam passage With ft connection, engine or also exhaust passage and ft connection, engine also have exhaust passage to connect with generation-evaporator Logical, generation-evaporator also has condensate liquid pipeline and ft connection, and engine also has the second steam channel to be connected with heat exchanger, Heat exchanger also has the second condensate liquid pipeline and ft connection;Steam chest is divided to have concentrated solution pipeline through solution pump and solution heat exchanger Connected with absorber, absorber also has weak solution pipeline to be connected with the 3rd absorber, the 3rd absorber also has weak solution pipeline warp Second solution pump and the second solution heat exchanger are connected with the second absorber, and the second absorber also has weak solution pipeline molten through second Liquid heat exchanger, solution heat exchanger, solution choke valve and generation-evaporator are connected with a point steam chest, and a point steam chest also has cryogen steaming Vapour passage is connected with condenser, condenser also have cryogen liquid pipeline connected through cryogen liquid pump with generation-evaporator after generation-steaming Hair device has refrigerant steam channel to be connected respectively with absorber and the 3rd absorber again, and condenser also has cryogen liquid pipeline cold through second The 3rd absorber has refrigerant steam channel to be connected with the second absorber again after agent liquid pump is connected with the 3rd absorber, and condenser is also There are cooling medium pipeline and ft connection, absorber and the second absorber also have heated medium pipeline and ft connection respectively, Heat exchanger also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
33. the dynamic co-feeding system of heat, is that in the heat described in the 32nd moves co-feeding system, condenser is had into cryogen liquid pipeline warp After cryogen liquid pump is connected with generation-evaporator generation-evaporator have again refrigerant steam channel respectively with absorber and the 3rd suction Device connection is received to be adjusted to condenser and have cryogen liquid pipeline through cryogen liquid pump and ft connection, engine set up exhaust passage respectively with Absorber and the connection of the 3rd absorber, form the dynamic co-feeding system of heat.
34. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second Solution heat exchanger, the second cryogen liquid pump and the 3rd absorber are constituted;Engine connects working machine, and engine has live steam passage With ft connection, engine or also exhaust passage and ft connection, engine also have exhaust passage to be connected with generator, occur Device also has condensate liquid pipeline and ft connection, and the finisher that engine also has the second steam channel to be connected with evaporator has again Two condensate liquid pipelines and ft connection, engine also have the 3rd steam channel to be connected with heat exchanger, and heat exchanger also has the 3rd Condensate liquid pipeline and ft connection;Divide steam chest to there is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, inhale Receiving device also has weak solution pipeline to be connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline through the second solution pump and second Solution heat exchanger is connected with the second absorber, and the second absorber also has weak solution pipeline through the second solution heat exchanger, solution Heat exchanger, solution choke valve and generator are connected with a point steam chest, and a point steam chest also has refrigerant steam channel to be connected with condenser, cold Condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, evaporator also have refrigerant steam channel respectively with absorber and 3rd absorber connect, condenser also have cryogen liquid pipeline connected through the second cryogen liquid pump with the 3rd absorber after the 3rd absorption Device has refrigerant steam channel to be connected with the second absorber again, and condenser also has cooling medium pipeline and ft connection, absorber and Second 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.
35. the dynamic co-feeding system of heat, is in the heat described in the 34th moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage connected respectively with absorber and the 3rd absorber be adjusted in the lump engine have the second steam channel respectively with absorber Connected with the 3rd absorber, there is cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator 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.
36. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution Heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, evaporator, the second absorber, the second solution Pump, the second solution heat exchanger, the second cryogen liquid pump, the 3rd absorber, the 3rd cryogen liquid pump and the second solution choke valve institute group Into;Engine connects working machine, and engine has live steam passage and ft connection, and engine or also exhaust passage connect with outside Logical, engine also has exhaust passage to be connected with generation-evaporator, and generation-evaporator also has condensate liquid pipeline and ft connection, The finisher that engine also has the second steam channel to be connected with evaporator has the second condensate liquid pipeline and ft connection, power again Machine also has the 3rd steam channel to be connected with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection;Divide steam chest There is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorber also has weak solution pipeline through the second solution Choke valve is connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline through the second solution pump and the second solution heat exchanger Connected with the second absorber, the second absorber also has weak solution pipeline through the second solution heat exchanger, solution heat exchanger, solution Choke valve and generation-evaporator are connected with a point steam chest, and a point steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has Cryogen liquid pipeline is connected through cryogen liquid pump with evaporator, and evaporator also has refrigerant steam channel to be connected with absorber, and condenser is also Have cryogen liquid pipeline connected through the second cryogen liquid pump with the 3rd absorber after the 3rd absorber have refrigerant steam channel and the again Two absorbers connect, condenser also have cryogen liquid pipeline connected through the 3rd cryogen liquid pump with generation-evaporator after generation-evaporation Device has refrigerant steam channel to be connected with the 3rd absorber again, and condenser also has cooling medium pipeline and ft connection, absorber and Second 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.
37. the dynamic co-feeding system of heat, is in the heat described in the 36th moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the second steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, forms heat Dynamic co-feeding system.
38. the dynamic co-feeding system of heat, is in the heat described in the 36th moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage is connected with absorber to be adjusted to engine and has the second steam channel to be connected with absorber in the lump, and condenser is had into cryogen liquid Pipeline is connected through cryogen liquid pump with evaporator to be adjusted to condenser and has cryogen liquid pipeline through cryogen liquid pump and ft connection, will be condensed Device have cryogen liquid pipeline connected through the 3rd cryogen liquid pump with generation-evaporator after generation-evaporator have refrigerant steam channel again Connected with the 3rd absorber and be adjusted to condenser and have cryogen liquid pipeline through the 3rd cryogen liquid pump and ft connection, engine sets up row Vapour passage is connected with the 3rd absorber, forms the dynamic co-feeding system of heat.
39. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution Heat exchanger, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, second Solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd 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 connected with generation-evaporator, and generation-evaporator also has condensate liquid pipeline With ft connection, engine also has the second steam channel to be connected with heat exchanger, heat exchanger also have the second condensate liquid pipeline with Ft connection;Steam chest is divided to have concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorber also has dilute molten Liquid pipeline is connected with the 3rd absorber, and the 3rd absorber also has weak solution pipeline through the second solution pump and the second solution heat exchanger Connected with the second absorber, the second absorber also has weak solution pipeline through the second solution heat exchanger, solution heat exchanger, solution Choke valve and generation-evaporator are connected with a point steam chest, and a point steam chest also has refrigerant steam channel to be connected with the 4th absorber, and the 4th inhales Receiving device also has weak solution pipeline to be connected through the 3rd solution pump, the 3rd solution heat exchanger and generation-evaporator with second point of steam chest, Second point of steam chest also has concentrated solution pipeline to be connected through the 3rd solution heat exchanger with the 4th absorber, and second point of steam chest also has cryogen Steam channel is connected with condenser, condenser also have cryogen liquid pipeline connected through cryogen liquid pump with generation-evaporator after occur- Evaporator has refrigerant steam channel to be connected respectively with absorber and the 3rd absorber again, and condenser also has cryogen liquid pipeline through second The 3rd absorber has refrigerant steam channel to be connected with the second absorber again after cryogen liquid pump is connected with the 3rd absorber, condensation Device and the 4th absorber also have cooling medium pipeline and ft connection respectively, and absorber and the second 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.
40. the dynamic co-feeding system of heat, is that in the heat described in the 39th moves co-feeding system, condenser is had into cryogen liquid pipeline warp After cryogen liquid pump is connected with generation-evaporator generation-evaporator have again refrigerant steam channel respectively with absorber and the 3rd suction Device connection is received to be adjusted to condenser and have cryogen liquid pipeline through cryogen liquid pump and ft connection, engine set up exhaust passage respectively with Absorber and the connection of the 3rd absorber, form the dynamic co-feeding system of heat.
41. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second Solution heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd 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 connected with generator, and generator also has condensate liquid pipeline and ft connection, The finisher that engine also has the second steam channel to be connected with evaporator has the second condensate liquid pipeline and ft connection, power again Machine also has the 3rd steam channel to be connected with heat exchanger, and heat exchanger also has the 3rd condensate liquid pipeline and ft connection;Divide steam chest There is concentrated solution pipeline to be connected through solution pump and solution heat exchanger with absorber, absorber also has weak solution pipeline and the 3rd absorption Device is connected, and the 3rd 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 through the second solution heat exchanger, solution heat exchanger, solution choke valve and generator Connected with a point steam chest, a point steam chest also has refrigerant steam channel to be connected with the 4th absorber, and the 4th absorber also has weak solution pipeline Connected through the 3rd solution pump, the 3rd solution heat exchanger and generator with second point of steam chest, second point of steam chest also has concentrated solution pipe The solution heat exchangers of Lu Jing tri- are connected with the 4th absorber, and second point of steam chest also has refrigerant steam channel to be connected with condenser, Condenser also has cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator, evaporator also have refrigerant steam channel respectively with absorber Connected with the 3rd absorber, condenser also have cryogen liquid pipeline connected through the second cryogen liquid pump with the 3rd absorber after the 3rd suction Receive device has refrigerant steam channel to be connected with the second absorber again, condenser and the 4th absorber also have respectively cooling medium pipeline and Ft connection, absorber and the second absorber also have heated medium pipeline and ft connection respectively, and heat exchanger, which also has, to be added Heat medium pipeline and ft connection, form the dynamic co-feeding system of heat.
42. the dynamic co-feeding system of heat, is in the heat described in the 41st moves co-feeding system, to cancel evaporator, engine is had The finisher that second steam channel is connected with evaporator has the second condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage connected respectively with absorber and the 3rd absorber be adjusted in the lump engine have the second steam channel respectively with absorber Connected with the 3rd absorber, there is cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator 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.
43. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point vapour Room, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, second Generator, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger 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 connected with the second generator, and the second generator also has condensate liquid pipeline and ft connection, and engine is also Have the second steam channel to be sequentially communicated generator and the finisher of evaporator has the second condensate liquid pipeline and ft connection again, moves Power machine also has the 3rd steam channel to be connected with 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 through solution pump and solution heat exchanger with absorber, and absorber also has weak solution pipeline and the 3rd Absorber is connected, and the 3rd absorber also has weak solution pipeline to be absorbed through the second solution pump and the second solution heat exchanger and second Device is connected, and the second absorber also has weak solution pipeline to be connected through the second solution heat exchanger and solution heat exchanger with generator, Generator also has refrigerant steam channel to be connected with the 4th absorber, the 4th absorber also have weak solution pipeline through the 3rd solution pump, 3rd solution heat exchanger and the second generator are connected with a point steam chest, and a point steam chest also has concentrated solution pipeline through the 3rd solution heat exchange Device is connected with the 4th absorber, and a point steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline warp Cryogen liquid pump is connected with evaporator, and evaporator also has refrigerant steam channel to be connected respectively with absorber and the 3rd absorber, condensation Device also have cryogen liquid pipeline connected through the second cryogen liquid pump with the 3rd absorber after the 3rd absorber have refrigerant steam channel again Connected with the second absorber, condenser and the 4th absorber also have cooling medium pipeline and ft connection, absorber and respectively Two absorbers also have 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.
44. the dynamic co-feeding system of heat, is in the heat described in the 43rd moves co-feeding system, to cancel evaporator, engine is had Second steam channel is sequentially communicated generator and the finisher of evaporator connection the second condensate liquid pipeline and ft connection again Be adjusted to engine have the second steam channel connected with generator after generator have the second condensate liquid pipeline and ft connection again, There is refrigerant steam channel to connect with absorber and the 3rd absorber respectively evaporator to be adjusted to engine and set up the second steam to lead to Road is connected with absorber and the 3rd absorber respectively, has cryogen liquid pipeline to connect adjustment with evaporator through cryogen liquid pump condenser There is cryogen liquid pipeline through cryogen liquid pump and ft connection for condenser, form the dynamic co-feeding system of heat.
45. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point vapour Room, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, second Generator, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger 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 connected with the second generator, and the second generator also has condensate liquid pipeline and ft connection, and engine is also Have the second steam channel connected with generator after generator have the second condensate liquid pipeline and ft connection again, engine also has The finisher that three steam channels are connected with evaporator has the 3rd condensate liquid pipeline and ft connection again, and engine also has the 4th steaming Vapour passage is connected with heat exchanger, and heat exchanger also has the 4th condensate liquid pipeline and ft connection;Generator also has concentrated solution pipe Road is connected through solution pump and solution heat exchanger with absorber, and absorber also has weak solution pipeline to be connected with the 3rd absorber, the Three absorbers also have weak solution pipeline to be connected through the second solution pump and the second solution heat exchanger with the second absorber, and second absorbs Device also has weak solution pipeline to be connected through the second solution heat exchanger and solution heat exchanger with generator, and generator also has cryogen steaming Vapour passage is connected with the 4th absorber, and the 4th absorber also has weak solution pipeline through the 3rd solution pump, the 3rd solution heat exchanger Connected with the second generator with a point steam chest, a point steam chest also has concentrated solution pipeline to connect through the 3rd solution heat exchanger and the 4th absorber Logical, a point steam chest also has refrigerant steam channel to be connected with condenser, and condenser also has cryogen liquid pipeline through cryogen liquid pump and evaporator Connection, evaporator also has refrigerant steam channel to be connected respectively with absorber and the 3rd absorber, and condenser also has cryogen liquid pipeline The 3rd absorber has refrigerant steam channel to be connected with the second absorber again after being connected through the second cryogen liquid pump with the 3rd absorber, Condenser and the 4th absorber also have cooling medium pipeline and a ft connection respectively, absorber and the second absorber also have respectively by Medium pipeline and ft connection are heated, heat exchanger also has heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
46. the dynamic co-feeding system of heat, is in the heat described in the 45th moves co-feeding system, to cancel evaporator, engine is had The finisher that 3rd steam channel is connected with evaporator has the 3rd condensate liquid pipeline and ft connection, evaporator to have cryogen steaming again Vapour passage connected respectively with absorber and the 3rd absorber be adjusted in the lump engine have the 3rd steam channel respectively with absorber Connected with the 3rd absorber, there is cryogen liquid pipeline to be connected through cryogen liquid pump with evaporator 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.
47. the dynamic co-feeding system of heat, is moved in any hot described in 1-2,5-6,17-18,21-23,32-33,39-40 In co-feeding system, cancel heat exchanger, cancel the heated medium pipeline connected with heat exchanger, cancellation is connected with heat exchanger The second steam channel, cancel the second condensate liquid pipeline for connect with heat exchanger, formed and hot moves co-feeding system.
48. the dynamic co-feeding system of heat, is described in 3-4,7-12,19-20,24-27,30-31,34-38,41-44 Any hot is moved in co-feeding system, cancels heat exchanger, cancels the heated medium pipeline connected with heat exchanger, is cancelled and heat friendship 3rd steam channel of parallel operation connection, cancels the 3rd condensate liquid pipeline connected with heat exchanger, forms the dynamic co-feeding system of heat.
49. the dynamic co-feeding system of heat, is in any hot described in 13-16,28-29,45-46 moves co-feeding system, to take Disappear heat exchanger, cancels the heated medium pipeline connected with heat exchanger, cancels the 4th steam connected with heat exchanger and leads to Road, cancels the 4th condensate liquid pipeline connected with heat exchanger, forms the dynamic co-feeding system of heat.
Brief description of the drawings:
Fig. 1 is according to 1st kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 2 is according to 2nd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 3 is according to 3rd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 4 is according to 4th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 5 is according to 5th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 6 is according to 6th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 7 is according to 7th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 8 is according to 8th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Fig. 9 is according to 9th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 10 is according to 10th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 11 is according to 11st kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 12 is according to 12nd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 13 is according to 13rd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 14 is according to 14th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 15 is according to 15th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 16 is according to 16th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 17 is according to 17th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 18 is according to 18th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 19 is according to 19th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 20 is according to 20th kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 21 is according to 21st kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
Figure 22 is according to 22nd kind of principled thermal system figure of the dynamic co-feeding system of heat provided by the present invention.
In figure, 1- generations-evaporator, 2- absorbers, 3- condensers, 4- solution pumps, 5- cryogen liquid pumps, 6- solution heat exchanges Device, 7- solution choke valves, 8- points of steam chests, 9- heat exchangers, 10- engines, 11- working machines, 12- generators, 13- evaporators, The absorbers of 14- second, the solution pumps of 15- second, the solution heat exchangers of 16- second, second point of steam chest of 17-, the generators of 18- second, 19- the second cryogen liquid pumps, the evaporators of 20- second, the absorbers of 21- the 3rd, the cryogen liquid pumps of 22- the 3rd, the throttling of the solution of 23- second Valve, the absorbers of 24- the 4th, the solution pumps of 25- the 3rd, the solution heat exchangers of 26- the 3rd.
Here following explanation is also provided:
(1) live steam --- refer to converted for hot merit, pressure and temperature is above the engine working media that draws gas.
(2) steam discharge --- refer to the low-pressure steam in engine export medium, such as steam turbine outlet moist steam.
(3) second steam --- a certain position of engine is extracted out, pressure and temperature is above the working media of steam discharge.
(4) the 3rd steam --- the work that a certain position of engine is extracted out, pressure and temperature is above the second steam is situated between Matter.
(4) the 4th steam --- the work that a certain position of engine is extracted out, pressure and temperature is above the 3rd steam is situated between Matter.
(5) condensate liquid --- the liquid of steam discharge exothermic condensation formation.
(6) second condensate liquids --- the liquid of the second steam exothermic condensation formation.
(7) the 3rd condensate liquids --- the liquid of the 3rd steam exothermic condensation formation.
(8) the 4th condensate liquids --- the liquid of the 4th steam exothermic condensation formation.
(9) it is relevant with engine, but be not related to operation principle of the present invention, part (such as power unrelated with present invention System backheat heat exchanger components etc.) and flow (recovery of such as condensate liquid), not in express ranges of the present invention.
(10) the refrigerant vapour exothermic condensation formation cryogen liquid of cryogen liquid and condensate liquid --- generator solution release, power The working steam exothermic condensation formation condensate liquid of machine;Claim cryogen liquid when refrigerant vapour and working steam is same materials.
(11) engine exports the utilization of steam discharge --- for the dynamic co-feeding system of specific heat, the profit of exhaust steam heat load With being divided into three kinds of situations:1. exhaust steam heat load is all utilized;2. exhaust steam heat load part is utilized;3. exhaust steam heat load not by Utilize.Therefore, summarizing steam discharge utilization power using " engine 1 or also exhaust passage and ft connection " such statement.
(12) name on generator and generation-evaporator --- referred to as generator when being only used for solution heating vaporization, Such as the generator 12 in Fig. 2;It is referred to as generation-evaporator when being respectively used to solution heating vaporization and cryogen liquid heats vaporization, such as Generation-evaporator 1 in Fig. 3.
(13) effect of choke valve and solution choke valve --- for fluid decompression, it can be taken by gravity pressure difference or pipe resistance Generation.
Embodiment:
First it is noted that in the statement of structure and flow, it is inessential in the case of do not repeat;To apparent Flow do not state.The present invention is described in detail with example below in conjunction with the accompanying drawings.
Heat shown in Fig. 1 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine and a working machine are constituted;Engine 10 connects working machine 11, moves Power machine 10 has live steam passage and ft connection, and engine 10 also has exhaust passage and ft connection, and engine 10 also has steam discharge to lead to Road is connected with generation-evaporator 1, and generation-evaporator 1 also has condensate liquid pipeline and ft connection, and engine 10 also has second to steam Vapour passage is connected with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection;Steam chest 8 is divided to have concentrated solution pipe Road is connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorber 2 also have weak solution pipeline through solution heat exchanger 6, Solution choke valve 7 and generation-evaporator 1 are connected with a point steam chest 8, and point steam chest 8 also has refrigerant steam channel to be connected with condenser 3, Condenser 3 also have cryogen liquid pipeline connected through cryogen liquid pump 5 with generation-evaporator 1 after generation-evaporator 1 have cryogen steaming again Vapour passage is connected with absorber 2, and condenser 3 also has cooling medium pipeline and ft connection, and absorber 2 also has heated medium pipe Road and ft connection, heat exchanger 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the second steam, the Two steam in heat exchanger 9 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 10 Steam discharge is provided to generation-evaporator 1, steam discharge heat release in generation-evaporator 1 is externally discharged into condensate liquid, and engine 10 is also right Outer discharge steam discharge;The concentrated solution of steam chest 8 is divided to enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour simultaneously Heat release is flowed through in heated medium, the weak solution of absorber 2 after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 Generation-evaporator 1, heat absorbing part vaporization enter a point steam chest 8, and point release refrigerant vapour of steam chest 8 is simultaneously provided to condenser 3;Condensation The refrigerant vapour heat release of device 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 flows through hair after being pressurizeed through cryogen liquid pump 5 Life-evaporator 1, absorb heat into refrigerant vapour and provided to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Fig. 2 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator and an evaporator are constituted;Engine 10 connects working machine 11, moves Power machine 10 has live steam passage and ft connection, and engine 10 also has exhaust passage to be connected with generator 12, and generator 12 is also cold Lime set pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be connected with evaporator 13 have second again Condensate liquid pipeline and ft connection, engine 10 also have the 3rd steam channel to be connected with heat exchanger 9, heat exchanger 9 also the Three condensate liquid pipelines and ft connection;Steam chest 8 is divided to have concentrated solution pipeline to connect through solution pump 4 and solution heat exchanger 6 with absorber 2 Logical, absorber 2 also has weak solution pipeline to be connected through solution heat exchanger 6, solution choke valve 7 and generator 12 with a point steam chest 8, point Steam chest 8 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline through cryogen liquid pump 5 and evaporator 13 Connection, evaporator 13 also has refrigerant steam channel to be connected with absorber 2, and condenser 3 also has cooling medium pipeline and ft connection, Absorber 2 also has heated medium pipeline and ft connection, and heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to evaporator 13, the second steam in evaporator 13 heat release into after condensate liquid through the second condensate liquid tubes rows Go out, engine 10 provides steam discharge to generator 12, the heat release in generator 12 of all or part of steam discharge is externally discharged into condensate liquid; The concentrated solution of steam chest 8 is divided to enter absorber 2, absorption refrigerant vapour and heat release in heated through solution pump 4 and solution heat exchanger 6 Medium, the weak solution of absorber 2 flows through generator 12, heat absorption after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 Part vaporization enters a point steam chest 8, and point release refrigerant vapour of steam chest 8 is simultaneously provided to condenser 3;The refrigerant vapour heat release of condenser 3 In cooling medium into cryogen liquid, the cryogen liquid of condenser 3 enters evaporator 13 through the pressurization of cryogen liquid pump 5, absorbs heat into refrigerant vapour And provided to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Fig. 3 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution Heat exchanger and second point of steam chest are constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, Engine 10 also has exhaust passage to be connected with generation-evaporator 1, and generation-evaporator 1 also has condensate liquid pipeline and ft connection, Engine 10 also has the second steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline to connect with outside It is logical;Steam chest 8 is divided to have concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorber 2 also has weak solution Pipeline is connected through solution heat exchanger 6, solution choke valve 7 and generation-evaporator 1 with a point steam chest 8, and point steam chest 8 also has cryogen to steam Vapour passage is connected with the second absorber 14, and the second absorber 14 also has weak solution pipeline through the second solution pump 15, the second solution heat Exchanger 16 and generation-evaporator 1 are connected with second point of steam chest 17, and second point of steam chest 17 also has concentrated solution pipeline through the second solution Heat exchanger 16 is connected with the second absorber 14, and second point of steam chest 17 also has refrigerant steam channel to be connected with condenser 3, condenser 3 also have cryogen liquid pipeline connected through cryogen liquid pump 5 with generation-evaporator 1 after generation-evaporator 1 have refrigerant steam channel again Connected with absorber 2, the absorber 14 of condenser 3 and second also has cooling medium pipeline and ft connection respectively, and absorber 2 also has Heated medium pipeline and ft connection, heat exchanger 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the second steam, the Two steam in heat exchanger 9 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 10 Steam discharge is provided to generation-evaporator 1, the heat release in generation-evaporator 1 of all or part of steam discharge is externally discharged into condensate liquid;Point The concentrated solution of steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorbs refrigerant vapour and heat release is in heated Jie Matter, the weak solution of absorber 2 flows through generation-evaporator 1, suction after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 Hot part vaporization enters a point steam chest 8, and point release refrigerant vapour of steam chest 8 is simultaneously provided to the second absorber 14;Second absorber 14 Weak solution flows through generation-evaporator 1, heat absorbing part vaporization after the second solution pump 15 and the second solution heat exchanger 16 and entered Second point of steam chest 17, second point of steam chest 17 release refrigerant vapour is simultaneously provided to condenser 3, and the concentrated solution of second point of steam chest 17 is through the Two solution heat exchangers 16 enter the second absorber 14, absorb refrigerant vapour and heat release is in cooling medium;The cryogen of condenser 3 steams Vapour heat release in cooling medium into cryogen liquid, the cryogen liquid of condenser 3 flowed through after being pressurizeed through cryogen liquid pump 5 generation-evaporator 1, Absorb heat into refrigerant vapour and provided to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Fig. 4 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger and second point of steam chest are constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, Engine 10 also has exhaust passage to be connected with generator 12, and generator 12 also has condensate liquid pipeline and ft connection, engine 10 The finisher 13 that also the second steam channel is connected with evaporator 13 has the second condensate liquid pipeline and ft connection, engine again 10 also have the 3rd steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection;Divide vapour Room 8 has concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, and absorber 2 also has weak solution pipeline warp Solution heat exchanger 6, solution choke valve 7 and generator 12 are connected with a point steam chest 8, and point steam chest 8 also has refrigerant steam channel and the Two absorbers 14 are connected, and the second absorber 14 also has weak solution pipeline through the second solution pump 15, the and of the second solution heat exchanger 16 Generator 12 is connected with second point of steam chest 17, and second point of steam chest 17 also has concentrated solution pipeline through the second solution heat exchanger 16 and the Two absorbers 14 are connected, and second point of steam chest 17 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipe Road is connected through cryogen liquid pump 5 with evaporator 13, and evaporator 13 also has refrigerant steam channel to be connected with absorber 2, condenser 3 and the Two absorbers 14 also have cooling medium pipeline and ft connection respectively, and absorber 2 also has heated medium pipeline and ft connection, Heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to evaporator 13, the second steam in evaporator 13 heat release into after condensate liquid through the second condensate liquid tubes rows Go out, engine 10 provides steam discharge to generator 12, the heat release in generator 12 of all or part of steam discharge is externally discharged into condensate liquid; The concentrated solution of steam chest 8 is divided to enter absorber 2, absorption refrigerant vapour and heat release in heated through solution pump 4 and solution heat exchanger 6 Medium, the weak solution of absorber 2 flows through generator 12, heat absorption after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 Part vaporization enters a point steam chest 8, and a point steam chest 8 discharges and provides refrigerant vapour to the second absorber 14;Second absorber 14 it is dilute Solution flows through generator 12, heat absorbing part vaporization after the second solution pump 15 and the second solution heat exchanger 16 and enters second point Steam chest 17, second point of steam chest 17 discharges and provides refrigerant vapour to condenser 3, and the concentrated solution of second point of steam chest 17 is through the second solution Heat exchanger 16 enters the second absorber 14, absorbs refrigerant vapour and heat release is in cooling medium;The refrigerant vapour heat release of condenser 3 In cooling medium into cryogen liquid, the cryogen liquid of condenser 3 enters evaporator 13 through the pressurization of cryogen liquid pump 5, absorbs heat into refrigerant vapour And provided to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Fig. 5 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the Two solution heat exchangers and second point of steam chest are constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and outer Portion is connected, and engine 10 also has exhaust passage to be connected with generator 12, and generator 12 also has condensate liquid pipeline and ft connection, is moved Power machine 10 also has the second steam channel to be connected with generation-evaporator 1, and generation-evaporator 1 also has the second condensate liquid pipeline and outside Connection, engine 10 also has the 3rd steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and outer Portion is connected;Steam chest 8 is divided to have concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorber 2 is also dilute Solution line is connected through solution heat exchanger 6, solution choke valve 7 and generation-evaporator 1 with a point steam chest 8, and point steam chest 8 is also cold Agent steam channel is connected with the second absorber 14, and the second absorber 14 also has weak solution pipeline molten through the second solution pump 15, second Liquid heat exchanger 16 and generator 12 are connected with second point of steam chest 17, and second point of steam chest 17 also has concentrated solution pipeline through the second solution Heat exchanger 16 is connected with the second absorber 14, and second point of steam chest 17 also has refrigerant steam channel to be connected with condenser 3, condenser 3 also have cryogen liquid pipeline connected through cryogen liquid pump 5 with generation-evaporator 1 after generation-evaporator 1 have refrigerant steam channel again Connected with absorber 2, the absorber 14 of condenser 3 and second also has cooling medium pipeline and ft connection respectively, and absorber 2 also has Heated medium pipeline and ft connection, heat exchanger 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to generation-evaporator 1, the second steam in generation-evaporator 1 heat release into after condensate liquid through the second condensation Liquid pipeline is discharged, and engine 10 provides steam discharge to generator 12, and all or part of steam discharge is external into condensate liquid in generator 12 Discharge;The concentrated solution of point steam chest 8 enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in Heated medium, the weak solution of absorber 2 flows through generation-steaming after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 Send out device 1, heat absorbing part vaporization and enter a point steam chest 8, point release refrigerant vapour of steam chest 8 is simultaneously provided to the second absorber 14;Second inhales The weak solution for receiving device 14 flows through generator 12, heat absorbing part vaporization after the second solution pump 15 and the second solution heat exchanger 16 Into second point of steam chest 17, second point of steam chest 17 discharges and provides refrigerant vapour, the concentrated solution of second point of steam chest 17 to condenser 3 Enter the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release is in cooling medium;Condenser 3 it is cold The heat release of agent steam is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 flows through generation-evaporation after being pressurizeed through cryogen liquid pump 5 Device 1, absorb heat into refrigerant vapour and provided to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Fig. 6 moves what co-feeding system was realized in:
(1) in structure, it mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution heat exchanger and Second generator is constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10 is also There is exhaust passage to be connected with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also has second to steam Vapour passage is sequentially communicated the second generator 18 and the finisher 13 of evaporator 13 the second condensate liquid pipeline and ft connection again, Engine 10 also has the 3rd steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline to connect with outside It is logical;Second generator 18 also has concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, and absorber 2 is also There is weak solution pipeline to be connected through solution heat exchanger 6 with the second generator 18, the second generator 18 also have refrigerant steam channel with Second absorber 14 is connected, and the second absorber 14 also has weak solution pipeline through the second solution pump 15, the second solution heat exchanger 16 Connected with generator 12 with a point steam chest 8, point steam chest 8 also has concentrated solution pipeline through the second solution heat exchanger 16 and the second absorber 14 connections, point steam chest 8 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline through cryogen liquid pump 5 Connected with evaporator 13, evaporator 13 also has refrigerant steam channel to be connected with absorber 2, the absorber 14 of condenser 3 and second is also There are cooling medium pipeline and ft connection respectively, absorber 2 also has heated medium pipeline and ft connection, and heat exchanger 9 is also There are heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 The second steam is provided to the second generator 18 and evaporator 13, and the second steam flows through the second generator 18 and evaporator 13, progressively Heat release through the second condensate liquid pipeline into discharging after condensate liquid, and engine 10 provides steam discharge, all or part of row to generator 12 Vapour heat release in generator 12 is externally discharged into condensate liquid;The concentrated solution of second generator 18 is through solution pump 4 and solution heat exchange Device 6 enters absorber 2, absorbs refrigerant vapour and heat release is in heated medium, and the weak solution of absorber 2 is through solution heat exchanger 6 There is provided into the second generator 18, heat absorption release refrigerant vapour and to the second absorber 14;The weak solution warp of second absorber 14 Generator 12, heat absorbing part vaporization are flowed through after second solution pump 15 and the second solution heat exchanger 16 and enters a point steam chest 8, point vapour Room 8 discharges and provides refrigerant vapour to condenser 3, and the concentrated solution of point steam chest 8 enters second through the second solution heat exchanger 16 and inhaled Device 14 is received, refrigerant vapour is absorbed and heat release is in cooling medium;The refrigerant vapour heat release of condenser 3 in cooling medium into cryogen liquid, The cryogen liquid of condenser 3 enters evaporator 13 through the pressurization of cryogen liquid pump 5, absorbs heat into refrigerant vapour and provided to absorber 2, is formed The dynamic co-feeding system of heat.
Heat shown in Fig. 7 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, second point of steam chest and the second generator are constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage With ft connection, engine 10 also has exhaust passage to be connected with generator 12, and generator 12 also has condensate liquid pipeline to connect with outside Logical, engine 10 also has the second steam channel to be connected with the second generator 18, and the second generator 18 also has the second condensate liquid pipeline With ft connection, the finisher 13 that engine 10 also has the 3rd steam channel to be connected with evaporator 13 has the 3rd condensate line again Road and ft connection, engine 10 also have the 4th steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the 4th condensate liquid Pipeline and ft connection;Divide steam chest 8 to there is concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorb Device 2 also has weak solution pipeline to be connected through solution heat exchanger 6, the generator 18 of solution choke valve 7 and second with a point steam chest 8, point vapour Room 8 also has refrigerant steam channel to be connected with the second absorber 14, and the second absorber 14 also has weak solution pipeline through the second solution pump 15th, the second solution heat exchanger 16 and generator 12 are connected with second point of steam chest 17, and second point of steam chest 17 also has concentrated solution pipeline Connected through the second solution heat exchanger 16 with the second absorber 14, second point of steam chest 17 also has refrigerant steam channel and condenser 3 Connection, condenser 3 also has cryogen liquid pipeline to be connected through cryogen liquid pump 5 with evaporator 13, and evaporator 13 also has refrigerant steam channel Connected with absorber 2, the absorber 14 of condenser 3 and second also has cooling medium pipeline and ft connection respectively, and absorber 2 also has Heated medium pipeline and ft connection, heat exchanger 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 4th steam, the Four steam in heat exchanger 9 heat release in heated medium into being discharged through the 4th condensate liquid pipeline after condensate liquid, engine 10 There is provided the 3rd steam to evaporator 13, the 3rd steam in evaporator 13 heat release into after condensate liquid through the 3rd condensate liquid tubes rows Go out, engine 10 to the second generator 18 provide the second steam, the second steam in the second generator 18 heat release into condensate liquid it Discharged by the second condensate liquid pipeline, engine 10 provides steam discharge to generator 12, and all or part of steam discharge is in generator 12 Externally discharged into condensate liquid;The concentrated solution of steam chest 8 is divided to enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb cryogen Simultaneously heat release is in heated medium for steam, and the weak solution of absorber 2 cools and the decompression of solution choke valve 7 through solution heat exchanger 6 After flow through the second generator 18, heat absorbing part vaporization and enter a point steam chest 8, point release refrigerant vapour of steam chest 8 and to the second absorber 14 provide;The weak solution of second absorber 14 flows through generator after the second solution pump 15 and the second solution heat exchanger 16 12nd, heat absorbing part vaporization enters a point steam chest 8, and a point steam chest 8 discharges and provides refrigerant vapour to condenser 3, the concentrated solution of point steam chest 8 Enter the second absorber 14 through the second solution heat exchanger 16, absorb refrigerant vapour and heat release is in cooling medium;Condenser 3 it is cold The heat release of agent steam is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 enters evaporator 13, heat absorption through the pressurization of cryogen liquid pump 5 There is provided into refrigerant vapour and to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Fig. 8 moves what co-feeding system was realized in:
(1) in structure, it mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution heat exchanger and Second generator is constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10 is also There is exhaust passage to be connected with generator 12, generator 12 also has condensate liquid pipeline and ft connection, engine 10 also has second to steam Second generator 18 has the second condensate liquid pipeline and ft connection, engine 10 again after vapour passage is connected with the second generator 18 The finisher 13 that also the 3rd steam channel is connected with evaporator 13 has the 3rd condensate liquid pipeline and ft connection, engine again 10 also have the 4th steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the 4th condensate liquid pipeline and ft connection;Second Generator 18 also has concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, and absorber 2 also has weak solution Pipeline is connected through solution heat exchanger 6 with the second generator 18, and the second generator 18 also has refrigerant steam channel to be absorbed with second Device 14 is connected, and the second absorber 14 also has weak solution pipeline through the second solution pump 15, the second solution heat exchanger 16 and generator 12 connect with a point steam chest 8, and point steam chest 8 also has concentrated solution pipeline to be connected through the second solution heat exchanger 16 with the second absorber 14, Steam chest 8 is divided to also have refrigerant steam channel to be connected with condenser 3, condenser 3 also has cryogen liquid pipeline through cryogen liquid pump 5 and evaporator 13 connections, evaporator 13 also has refrigerant steam channel to be connected with absorber 2, and the absorber 14 of condenser 3 and second also has cold respectively But medium pipeline and ft connection, absorber 2 also have heated medium pipeline and ft connection, and heat exchanger 9, which also has, to be heated Medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 4th steam, the Four steam in heat exchanger 9 heat release in heated medium into being discharged through the 4th condensate liquid pipeline after condensate liquid, engine 10 There is provided the 3rd steam to evaporator 13, the 3rd steam in evaporator 13 heat release into after condensate liquid through the 3rd condensate liquid tubes rows Go out, engine 10 to the second generator 18 provide the second steam, the second steam in the second generator 18 heat release into condensate liquid it Discharged by the second condensate liquid pipeline, engine 10 provides steam discharge to generator 12, and all or part of steam discharge is in generator 12 Heat release is externally discharged into condensate liquid;The concentrated solution of second generator 18 through solution pump 4 and solution heat exchanger 6 enter absorber 2, Absorb refrigerant vapour and heat release is in heated medium, the weak solution of absorber 2 enters the second generator through solution heat exchanger 6 18th, heat absorption discharges refrigerant vapour and provided to the second absorber 14;The weak solution of second absorber 14 is through the He of the second solution pump 15 Generator 12, heat absorbing part vaporization are flowed through after second solution heat exchanger 16 and enters a point steam chest 8, a point steam chest 8 discharges and to cold Condenser 3 provides refrigerant vapour, and the concentrated solution of point steam chest 8 enters the second absorber 14 through the second solution heat exchanger 16, absorbs cold Agent steam and heat release are in cooling medium;The refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, the cryogen of condenser 3 Liquid enters evaporator 13 through the pressurization of cryogen liquid pump 5, absorbs heat into refrigerant vapour and provided to absorber 2, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 9 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump and second point Steam chest is constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10 also has steam discharge Passage is connected with generation-evaporator 1, and generation-evaporator 1 also has condensate liquid pipeline and ft connection, and engine 10 also has second Steam channel is connected with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection;Steam chest 8 is divided to have concentrated solution Pipeline is connected through solution pump 4 and solution heat exchanger 6 with absorber 2, and absorber 2 also has weak solution pipeline through solution heat exchanger 6 connect with the second absorber 14, the second absorber 14 also have weak solution pipeline through the second solution pump 15 and generation-evaporator 1 with Second point of steam chest 17 is connected, and second point of steam chest 17 also has concentrated solution pipeline through solution choke valve 7 and generation-evaporator 1 and a point vapour Room 8 is connected, and point steam chest 8 also has refrigerant steam channel to be connected with the second absorber 14, and second point of steam chest 17 also has refrigerant vapour to lead to Road is connected with condenser 3, generation-steaming after the also cryogen liquid pipeline of condenser 3 is connected through cryogen liquid pump 5 with generation-evaporator 1 Hair device 1 has refrigerant steam channel to be connected with absorber 2 again, and the absorber 14 of condenser 3 and second also has cooling medium pipeline respectively With ft connection, absorber 2 also have heated medium pipeline and ft connection, heat exchanger 9 also have heated medium pipeline with Ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the second steam, the Two steam in heat exchanger 9 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 10 Steam discharge is provided to generation-evaporator 1, the heat release in generation-evaporator 1 of all or part of steam discharge is externally discharged into condensate liquid;Point The concentrated solution of steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorbs refrigerant vapour and heat release is in heated Jie Matter, the weak solution of absorber 2 enters the second absorber 14 through solution heat exchanger 6, absorbs refrigerant vapour and heat release is in heated Medium, the weak solution of the second absorber 14 flows through generation-evaporator 1, heat absorbing part and vaporized after being pressurizeed through the second solution pump 15 Into second point of steam chest 17, second point of release refrigerant vapour of steam chest 17 is simultaneously provided, the concentrated solution of second point of steam chest 17 to condenser 3 Generation-evaporator 1, heat absorbing part vaporization are flowed through after the reducing pressure by regulating flow of solution choke valve 17 and enters a point steam chest 8, a point steam chest 8 is released Put refrigerant vapour and provided to the second absorber 14;The refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, condenser 3 cryogen liquid flows through generation-evaporator 1 after being pressurizeed through cryogen liquid pump 5, absorbs heat into refrigerant vapour and provided to absorber 2, shape Into the dynamic co-feeding system of heat.
Heat shown in Figure 10 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat are handed over Parallel operation and second point of steam chest are constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, power Machine 10 also has exhaust passage to be connected with generator 12, and generator 12 also has condensate liquid pipeline and ft connection, and engine 10 also has Second steam channel generation-evaporator 1 is connected, and generation-evaporator 1 also has the second condensate liquid pipeline and ft connection, engine 10 also have the 3rd steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection;Divide vapour Room 8 has concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, and absorber 2 also has weak solution pipeline warp Solution heat exchanger 6 is connected with the second absorber 14, and the second absorber 14 also has weak solution pipeline through the second solution pump 15, second Solution heat exchanger 16 and generation-evaporator 1 are connected with second point of steam chest 17, and second point of steam chest 17 also has concentrated solution pipeline through the Two solution heat exchangers 17 and generator 12 are connected with a point steam chest 8, and point steam chest 8 also has refrigerant steam channel and the second absorber 14 Connection, second point of steam chest 17 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline through cryogen liquid Generation-evaporator 1 has refrigerant steam channel to be connected with absorber 2 again after pump 5 is connected with generation-evaporator 1, the He of condenser 3 Second absorber 14 also has cooling medium pipeline and ft connection respectively, and absorber 2 also has heated medium pipeline to connect with outside Logical, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to generation-evaporator 1, the second steam in generation-evaporator 1 heat release into after condensate liquid through the second condensation Liquid pipeline is discharged, and engine 10 provides steam discharge to generator 12, all or part of steam discharge in generator 12 heat release into condensate liquid Externally discharge;The concentrated solution of steam chest 8 is divided to enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and put Heat enters the second absorber 14 through solution heat exchanger 6, absorbs refrigerant vapour simultaneously in heated medium, the weak solution of absorber 2 Heat release is flowed in heated medium, the weak solution of the second absorber 14 after the second solution pump 15 and the second solution heat exchanger 16 Enter second point of steam chest 17 through generation-evaporator 1, heat absorbing part vaporization, second point of release refrigerant vapour of steam chest 17 and to condensation Device 3 is provided, and the concentrated solution of second point of steam chest 17 flows through generator 12, heat absorbing part after cooling through the second solution heat exchanger 16 Vaporization enters a point steam chest 8, and point release refrigerant vapour of steam chest 8 is simultaneously provided to the second absorber 14;The refrigerant vapour heat release of condenser 3 In cooling medium into cryogen liquid, the cryogen liquid of condenser 3 flows through generation-evaporator 1 after being pressurizeed through cryogen liquid pump 5, absorbed heat into Refrigerant vapour is simultaneously provided to absorber 2, forms the dynamic co-feeding system of heat.
Heat shown in Figure 11 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the Two solution heat exchangers and the second cryogen liquid pump are constituted;Engine 10 connect working machine 11, engine 10 have live steam passage with Ft connection, engine 10 also have exhaust passage connected with generation-evaporator 1, generation-evaporator 1 also have condensate liquid pipeline and Ft connection, engine 10 also has the second steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline With ft connection;Steam chest 8 is divided to have concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorber 2 is also There is weak solution pipeline to be connected through solution heat exchanger 6, solution choke valve 7 and generation-evaporator 1 with a point steam chest 8, point steam chest 8 is also Have refrigerant steam channel connected with generator 12 after generator 12 there is cryogen liquid pipeline to be connected with the second cryogen liquid pump 19 again, Two cryogen liquid pumps 19 also have cryogen liquid pipeline connected with generation-evaporator 1 after generation-evaporator 1 have refrigerant steam channel again Connected with absorber 2;Generator 12 also has concentrated solution pipeline through the second solution pump 15 and the second solution heat exchanger 16 and second Absorber 14 is connected, and the second absorber 14 also has weak solution pipeline to be connected through the second solution heat exchanger 16 with generator 12, is sent out Raw device 12 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline through cryogen liquid pump 5 and generation-steaming Generation-evaporator 1 has refrigerant steam channel to be connected with the second absorber 14 again after hair device 1 is connected, and condenser 3, which also has to cool down, to be situated between Matter pipeline and ft connection, the absorber 14 of absorber 2 and second also have heated medium pipeline and ft connection, heat exchange respectively Device 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the second steam, the Two steam in heat exchanger 9 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 10 Steam discharge is provided to generation-evaporator 1, the heat release in generation-evaporator 1 of all or part of steam discharge is externally discharged into condensate liquid;Point The concentrated solution of steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorbs refrigerant vapour and heat release is in heated Jie Matter, the weak solution of absorber 2 flows through generation-evaporator 1, suction after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 Hot part vaporization enters a point steam chest 8, and point release refrigerant vapour of steam chest 8 is simultaneously supplied to generator 12 to make driving thermal medium;Generator 12 concentrated solution enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorbs refrigerant vapour and puts Heat enters generator 12, refrigerant vapour in heated medium, the weak solution of the second absorber 14 through the second solution heat exchanger 16 Flow through generator 18, the solution that heating enters in it discharges and provides refrigerant vapour, the refrigerant vapour of condenser 3 to condenser 3 Heat release is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 flows through generation-evaporator 1, suction after being pressurizeed through cryogen liquid pump 5 Heat is provided into refrigerant vapour and to the second absorber 14;The refrigerant vapour heat release of generator 12 is flowed through into cryogen liquid, then through second Cryogen liquid pump 19 flows through generation-evaporator 1 after pressurizeing, absorbs heat into refrigerant vapour and provided to absorber 2, forms the dynamic connection of heat For system.
Heat shown in Figure 12 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat It is parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, second molten Liquid pump, the second solution heat exchanger and the second cryogen liquid pump are constituted;Engine 10 connects working machine 11, and engine 10 has live steam Passage and ft connection, engine 10 also have exhaust passage to be connected with generation-evaporator 1, and generation-evaporator 1 also has condensate liquid Pipeline and ft connection, the finisher 13 that engine 10 also has the second steam channel to be connected with evaporator 13 have the second condensation again Liquid pipeline and ft connection, engine 10 also have the 3rd steam channel to be connected with heat exchanger 9, and heat exchanger 9 the also the 3rd is cold Lime set pipeline and ft connection;Steam chest 8 is divided to have concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, Absorber 2 also has weak solution pipeline to be connected through solution heat exchanger 6, solution choke valve 7 and generation-evaporator 1 with a point steam chest 8, Point steam chest 8 also have refrigerant steam channel connected with generator 12 after generator 12 have cryogen liquid pipeline again through the second cryogen liquid pump 19 connect with evaporator 13, and evaporator 13 also has refrigerant steam channel to be connected with absorber 2;Generator 12 also has concentrated solution pipeline Connected through the second solution pump 15 and the second solution heat exchanger 16 with the second absorber 14, the second absorber 14 also has weak solution pipe The second solution heat exchanger of road 16 is connected with generator 12, and generator 12 also has refrigerant steam channel to be connected with condenser 3, cold Condenser 3 also have cryogen liquid pipeline connected through cryogen liquid pump 5 with generation-evaporator 1 after generation-evaporator 1 have refrigerant vapour again Passage is connected with the second absorber 14, and condenser 3 also has cooling medium pipeline and ft connection, the absorber of absorber 2 and second 14 also have heated medium pipeline and ft connection respectively, and heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to evaporator 13, the second steam in evaporator 13 heat release into after condensate liquid through the second condensate liquid tubes rows Go out, engine 10 provides steam discharge to generation-evaporator 1, all or part of steam discharge in generation-evaporator 1 heat release into condensate liquid Externally discharge;The concentrated solution of steam chest 8 is divided to enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and put Heat flows through hair in heated medium, the weak solution of absorber 2 after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 Life-evaporator 1, heat absorbing part vaporization enter a point steam chest 8, and point release refrigerant vapour of steam chest 8 is simultaneously supplied to generator 12 to drive Thermal medium;The concentrated solution of generator 12 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, inhaled Receive refrigerant vapour and heat release is in heated medium, the weak solution of the second absorber 14 enters through the second solution heat exchanger 16 to be occurred Device 12, the solution that refrigerant vapour flows through generator 12, heating enters in it discharges and provides refrigerant vapour, condensation to condenser 3 The refrigerant vapour heat release of device 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 flows through hair after being pressurizeed through cryogen liquid pump 5 Life-evaporator 1, absorb heat into refrigerant vapour and provided to the second absorber 14, flow through the refrigerant vapour heat release Cheng Leng of generator 12 Enter evaporator 13 through the pressurization of the second cryogen liquid pump 19 after agent liquid, absorb heat into refrigerant vapour and provided to absorber 2, form heat Dynamic co-feeding system.
Heat shown in Figure 13 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, the second generator, the second cryogen liquid pump and the second evaporator are constituted;Engine 10 connects working machine 11, power Machine 10 has live steam passage and ft connection, and engine 10 also has exhaust passage to be connected with generator 12, and generator 12, which also has, to be condensed Liquid pipeline and ft connection, engine 10 also have the second steam channel to be sequentially communicated after the evaporator 20 of evaporator 13 and second the Two evaporators 20 have the second condensate liquid pipeline and ft connection again, and engine 10 also has the 3rd steam channel to connect with heat exchanger 9 Logical, heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection;Steam chest 8 is divided to have concentrated solution pipeline through solution pump 4 and solution heat Exchanger 6 is connected with absorber 2, and absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 and generator 12 connect with a point steam chest 8, point steam chest 8 also have refrigerant steam channel connected with the second generator 18 after the second generator 18 have again Cryogen liquid pipeline is connected through the second cryogen liquid pump 19 with evaporator 13, and evaporator 13 also has refrigerant steam channel to connect with absorber 2 It is logical;Second generator 18 also has concentrated solution pipeline through the second solution pump 15 and the second solution heat exchanger 16 and the second absorber 14 Connection, the second absorber 14 also has weak solution pipeline to be connected through the second solution heat exchanger 16 with the second generator 18, the second hair Raw device 18 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline to be steamed through cryogen liquid pump 5 and second Hair device 20 is connected, and the second evaporator 20 also has refrigerant steam channel to be connected with the second absorber 14, and condenser 3 also has cooling medium Pipeline and ft connection, the absorber 14 of absorber 2 and second also have heated medium pipeline and ft connection, heat exchanger respectively 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 The second steam is provided to the evaporator 20 of evaporator 13 and second, the second steam flows through the evaporator 20 of evaporator 13 and second, progressively Heat release through the second condensate liquid pipeline into discharging after condensate liquid, and engine 10 provides steam discharge, all or part of row to generator 12 Vapour heat release in generator 12 is externally discharged into condensate liquid;The concentrated solution of steam chest 8 is divided to enter through solution pump 4 and solution heat exchanger 6 Enter absorber 2, absorb refrigerant vapour and heat release in heated medium, the weak solution of absorber 2 through the cooling of solution heat exchanger 6 and Solution choke valve 7 flows through generator 12, heat absorbing part vaporization and enters a point steam chest 8 after being depressured, point release of steam chest 8 refrigerant vapour is simultaneously It is supplied to the second generator 18 to make driving thermal medium;The concentrated solution of second generator 18 is through the second solution pump 15 and the second solution heat Exchanger 16 enters the second absorber 14, absorbs refrigerant vapour and heat release is in heated medium, the weak solution of the second absorber 14 Enter the second generator 18 through the second solution heat exchanger 16, refrigerant vapour flows through the second generator 18, heating and entered in it Solution is discharged and provides refrigerant vapour to condenser 3, and the refrigerant vapour heat release of condenser 3, into cryogen liquid, is condensed in cooling medium The cryogen liquid of device 3 enters the second evaporator 20 through the pressurization of cryogen liquid pump 5, absorbs heat into refrigerant vapour and carried to the second absorber 14 For flowing through the refrigerant vapour heat release of the second generator 18 into entering evaporator through the pressurization of the second cryogen liquid pump 19 after cryogen liquid 13rd, absorb heat into refrigerant vapour and provided to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Figure 14 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, the second generator, the second cryogen liquid pump and the second evaporator are constituted;Engine 10 connects working machine 11, power Machine 10 has live steam passage and ft connection, and engine 10 also has exhaust passage to be connected with generator 12, and generator 12, which also has, to be condensed Liquid pipeline and ft connection, engine 10 also have the second steam channel connected with the second evaporator 20 after the second evaporator 20 again There are the second condensate liquid pipeline and ft connection, engine 10 also has the finisher 13 that the 3rd steam channel is connected with evaporator 13 There are the 3rd condensate liquid pipeline and ft connection again, engine 10 also has the 4th steam channel to be connected with heat exchanger 9, heat exchanger 9 also have the 4th condensate liquid pipeline and ft connection;Steam chest 8 is divided to have concentrated solution pipeline through solution pump 4 and solution heat exchanger 6 with inhaling Receive device 2 to connect, absorber 2 also has weak solution pipeline through solution heat exchanger 6, solution choke valve 7 and generator 12 and a point steam chest 8 Connection, point steam chest 8 also have refrigerant steam channel connected with the second generator 18 after the second generator 18 have cryogen liquid pipeline again Connected through the second cryogen liquid pump 19 with evaporator 13, evaporator 13 also has refrigerant steam channel to be connected with absorber 2;Second occurs Device 18 also has concentrated solution pipeline to be connected through the second solution pump 15 and the second solution heat exchanger 16 with the second absorber 14, and second inhales Receiving device 14 also has weak solution pipeline to be connected through the second solution heat exchanger 16 with the second generator 18, and the second generator 18 is also cold Agent steam channel is connected with condenser 3, and condenser 3 also has cryogen liquid pipeline to be connected through cryogen liquid pump 5 with the second evaporator 20, Second evaporator 20 also has refrigerant steam channel to be connected with the second absorber 14, and condenser 3 also has cooling medium pipeline and outside Connection, the absorber 14 of absorber 2 and second also has heated medium pipeline and ft connection respectively, and heat exchanger 9, which also has, to be added Heat medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 4th steam, the Four steam in heat exchanger 9 heat release in heated medium into being discharged through the 4th condensate liquid pipeline after condensate liquid, engine 10 There is provided the 3rd steam to evaporator 13, the 3rd steam in evaporator 13 heat release into after condensate liquid through the 3rd condensate liquid tubes rows Go out, engine 10 to the second evaporator 20 provide the second steam, the second steam in the second evaporator 20 heat release into condensate liquid it Discharged by the second condensate liquid pipeline, engine 10 provides steam discharge to generator 12, and all or part of steam discharge is in generator 12 Heat release is externally discharged into condensate liquid;The concentrated solution of steam chest 8 is divided to enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb Simultaneously heat release is in heated medium for refrigerant vapour, and the weak solution of absorber 2 drops through the cooling of solution heat exchanger 6 and solution choke valve 7 Generator 12, heat absorbing part vaporization are flowed through after pressure and enters a point steam chest 8, point release refrigerant vapour of steam chest 8 is simultaneously supplied to the second hair Raw device 18 makees driving thermal medium;The concentrated solution of second generator 18 enters through the second solution pump 15 and the second solution heat exchanger 16 Second absorber 14, absorption refrigerant vapour and heat release are in heated medium, and the weak solution of the second absorber 14 is through the second solution heat Exchanger 16 enter the second generator 18, refrigerant vapour flow through the second generator 18, heating enter its in solution release and to Condenser 3 provides refrigerant vapour, and the refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 is passed through The pressurization of cryogen liquid pump 5 enters the second evaporator 20, absorbs heat into refrigerant vapour and provided to the second absorber 14, flows through the second generation The refrigerant vapour heat release of device 18 is into entering evaporator 13 through the pressurization of the second cryogen liquid pump 19 after cryogen liquid, absorb heat into refrigerant vapour And provided to absorber 2, form the dynamic co-feeding system of heat.
Heat shown in Figure 15 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, the second generator and the second cryogen liquid pump and constituted;Engine 10 connects working machine 11, and engine 10 has live steam Passage and ft connection, engine 10 also have exhaust passage to be connected with generator 12, and generator 12 also has condensate liquid pipeline and outer Portion is connected, engine 10 also have the finisher 13 that is connected with evaporator 13 of the second steam channel have again the second condensate liquid pipeline and Ft connection, engine 10 also has the 3rd steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline With ft connection;Steam chest 8 is divided to have concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorber 2 is also There is weak solution pipeline to be connected through solution heat exchanger 6, solution choke valve 7 and generator 12 with a point steam chest 8, point steam chest 8 is also cold After agent steam channel is connected with the second generator 18 second generator 18 have again cryogen liquid pipeline through the second cryogen liquid pump 19 with Evaporator 13 is connected;Second generator 18 also has concentrated solution pipeline through the second solution pump 15 and the second solution heat exchanger 16 and the Two absorbers 14 are connected, and the second absorber 14 also has weak solution pipeline to connect through the second solution heat exchanger 16 with the second generator 18 Logical, the second generator 18 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline through cryogen liquid pump 5 Connected with evaporator 13, evaporator 13 also has refrigerant steam channel to be connected respectively with the absorber 14 of absorber 2 and second, condenser 3 also have cooling medium pipeline and ft connection, and the absorber 14 of absorber 2 and second also has heated medium pipeline and outside respectively Connection, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to evaporator 13, the second steam in evaporator 13 heat release into after condensate liquid through the second condensate liquid tubes rows Go out, engine 10 provides steam discharge to generator 12, the heat release in generator 12 of all or part of steam discharge is externally arranged into condensate liquid Go out;The concentrated solution of steam chest 8 is divided to enter absorber 2, absorption refrigerant vapour and heat release in quilt through solution pump 4 and solution heat exchanger 6 Heat medium, the weak solution of absorber 2 flowed through after being depressured through the cooling of solution heat exchanger 6 and solution choke valve 7 generator 12, Heat absorbing part vaporization enters a point steam chest 8, and point release refrigerant vapour of steam chest 8 is simultaneously supplied to the second generator 18 to make driving thermal medium; The concentrated solution of second generator 18 enters the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorbs cold Simultaneously heat release is in heated medium for agent steam, and the weak solution of the second absorber 14 enters second through the second solution heat exchanger 16 to be occurred Device 18, the solution that refrigerant vapour flows through the second generator 18, heating enters in it discharges and provides refrigerant vapour to condenser 3, The refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 enters through the pressurization of cryogen liquid pump 5 to be steamed Device 13 is sent out, the refrigerant vapour heat release of the second generator 18 is flowed through into entering evaporation through the pressurization of the second cryogen liquid pump 19 after cryogen liquid Device 13, the cryogen liquid of evaporator 13 absorbs heat into refrigerant vapour and provided respectively to the absorber 14 of absorber 2 and second, forms heat dynamic Co-feeding system.
Heat shown in Figure 16 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution Heat exchanger, the second cryogen liquid pump and the 3rd absorber are constituted;Engine 10 connects working machine 11, and engine 10 has live steam to lead to Road and ft connection, engine 10 also have exhaust passage to be connected with generation-evaporator 1, and generation-evaporator 1 also has condensate line Road and ft connection, engine 10 also have the second steam channel to be connected with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid Pipeline and ft connection;Divide steam chest 8 to there is concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorb Device 2 also has weak solution pipeline to be connected with the 3rd absorber 21, and the 3rd absorber 21 also has weak solution pipeline through the second solution pump 15 Connected with the second solution heat exchanger 16 with the second absorber 14, the second absorber 14 also has weak solution pipeline through the second solution heat Exchanger 16, solution heat exchanger 6, solution choke valve 7 and generation-evaporator 1 are connected with a point steam chest 8, and point steam chest 8 also has cryogen Steam channel is connected with condenser 3, and condenser 3 also has after cryogen liquid pipeline connects through cryogen liquid pump 5 with generation-evaporator 1 Generation-evaporator 1 has refrigerant steam channel to be connected respectively with the absorber 21 of absorber 2 and the 3rd again, and condenser 3 also has cryogen liquid The 3rd absorber 21 has refrigerant steam channel and second again after pipeline is connected through the second cryogen liquid pump 19 with the 3rd absorber 21 Absorber 14 is connected, and condenser 3 also has cooling medium pipeline and ft connection, and the absorber 14 of absorber 2 and second also has respectively Heated medium pipeline and ft connection, heat exchanger 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the second steam, the Two steam in heat exchanger 9 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 10 Steam discharge is provided to generation-evaporator 1, the heat release in generation-evaporator 1 of all or part of steam discharge is externally discharged into condensate liquid;Point The concentrated solution of steam chest 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorbs refrigerant vapour and heat release is in heated Jie Matter, the weak solution of absorber 2 enters the 3rd absorber 21, absorbs refrigerant vapour and heat release is in cryogen liquid, the 3rd absorber 21 Weak solution enter the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in Heated medium;The weak solution of second absorber 14 is through the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve Generation-evaporator 1 is flowed through after 7 and vaporization of absorbing heat enters a point steam chest 8, a point steam chest 8 discharges and provides cryogen to condenser 3 and steams Vapour;The refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 is divided into two-way --- the first via Generation-evaporator 1 is flowed through after being pressurizeed through cryogen liquid pump 5, absorb heat into refrigerant vapour and respectively to the absorber of absorber 2 and the 3rd 21 provide, and flow through the 3rd absorber 21 after the pressurization of second tunnel the second cryogen liquid pump 19, absorb heat into refrigerant vapour and to second Absorber 14 is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 17 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, the second cryogen liquid pump and the 3rd absorber are constituted;Engine 10 connects working machine 11, and engine 10 has live steam to lead to Road and ft connection, engine 10 also have exhaust passage to be connected with generator 12, and generator 12 also has condensate liquid pipeline and outside Connection, the finisher 13 that engine 10 also has the second steam channel to be connected with evaporator 13 has the second condensate liquid pipeline and outer again Portion connect, engine 10 also have the 3rd steam channel connected with heat exchanger 9, heat exchanger 9 also have the 3rd condensate liquid pipeline and Ft connection;Steam chest 8 is divided to have concentrated solution pipeline to be connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorber 2 also has Weak solution pipeline is connected with the 3rd absorber 21, and the 3rd absorber 21 also has weak solution pipeline molten through the second solution pump 15 and second Liquid heat exchanger 16 is connected with the second absorber 14, and the second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16th, solution heat exchanger 6, solution choke valve 7 and generator 12 are connected with a point steam chest 8, point steam chest 8 also have refrigerant steam channel with Condenser 3 is connected, and condenser 3 also has cryogen liquid pipeline to be connected through cryogen liquid pump 5 with evaporator 13, and evaporator 13 also has cryogen to steam Vapour passage is connected with the absorber 21 of absorber 2 and the 3rd respectively, condenser 3 also have cryogen liquid pipeline through the second cryogen liquid pump 19 with The 3rd absorber 21 has refrigerant steam channel to be connected with the second absorber 14 again after the connection of 3rd absorber 21, and condenser 3 is also There are cooling medium pipeline and ft connection, the absorber 14 of absorber 2 and second also has heated medium pipeline to connect with outside respectively Logical, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to evaporator 13, the second steam in evaporator 13 heat release into after condensate liquid through the second condensate liquid tubes rows Go out, engine 10 provides steam discharge to generator 12, the heat release in generator 12 of all or part of steam discharge is externally discharged into condensate liquid; The concentrated solution of steam chest 8 is divided to enter absorber 2, absorption refrigerant vapour and heat release in heated through solution pump 4 and solution heat exchanger 6 Medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorbs refrigerant vapour and heat release is in cryogen liquid, the 3rd absorber 21 Weak solution enter the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release In heated medium;The weak solution of second absorber 14 throttles through the second solution heat exchanger 16, solution heat exchanger 6 and solution Generator 12 is flowed through after valve 7, enters a point steam chest 8 after heat absorbing part vaporization, a point steam chest 8 discharges and provides cold to condenser 3 Agent steam;The refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 is divided into two-way --- the Enter evaporator 13 through the pressurization of cryogen liquid pump 5 all the way, absorb heat into refrigerant vapour and carried respectively to the absorber 21 of absorber 2 and the 3rd For flowing through the 3rd absorber 21 after the pressurization of second tunnel the second cryogen liquid pump 19, absorbing heat into refrigerant vapour and absorbed to second Device 14 is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 18 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, evaporator, the second absorber, the second solution pump, the Two solution heat exchangers, the second cryogen liquid pump, the 3rd absorber, the 3rd cryogen liquid pump and the second solution choke valve are constituted;It is dynamic Power machine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10 also has exhaust passage and generation-steaming Hair device 1 is connected, and generation-evaporator 1 also has condensate liquid pipeline and ft connection, and engine 10 also has the second steam channel and evaporation The finisher 13 of the connection of device 13 has the second condensate liquid pipeline and ft connection again, and engine 10 also has the 3rd steam channel and heat Exchanger 9 is connected, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection;Steam chest 8 is divided to have concentrated solution pipeline through solution pump 4 and solution heat exchanger 6 connected with absorber 2, absorber 2 also has weak solution pipeline through the second solution choke valve 23 and the 3rd suction Receive device 21 to connect, the 3rd absorber 21 also has weak solution pipeline through the second solution pump 15 and the second solution heat exchanger 16 and the Two absorbers 14 are connected, the second absorber 14 also have weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, Solution choke valve 7 and generation-evaporator 1 are connected with a point steam chest 8, and point steam chest 8 also has refrigerant steam channel to be connected with condenser 3, Condenser 3 also has cryogen liquid pipeline to be connected through cryogen liquid pump 5 with evaporator 13, and evaporator 13 also has refrigerant steam channel with absorbing Device 2 is connected, the 3rd absorber after the also cryogen liquid pipeline of condenser 3 is connected through the second cryogen liquid pump 19 with the 3rd absorber 21 21 have refrigerant steam channel to be connected with the second absorber 14 again, condenser 3 also have cryogen liquid pipeline through the 3rd cryogen liquid pump 22 with Generation-evaporator 1 has refrigerant steam channel to be connected with the 3rd absorber 21 again after generation-evaporator 1 is connected, and condenser 3 is also There are cooling medium pipeline and ft connection, the absorber 14 of absorber 2 and second also has heated medium pipeline to connect with outside respectively Logical, heat exchanger 9 also has heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to evaporator 13, the second steam in evaporator 13 heat release into after condensate liquid through the second condensate liquid tubes rows Go out, engine 10 provides steam discharge to generation-evaporator 1, all or part of steam discharge in generation-evaporator 1 heat release into condensate liquid Discharge;The concentrated solution of point steam chest 8 enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release in Heated medium, the weak solution of absorber 2 enters the 3rd absorber 21 after the reducing pressure by regulating flow of the second solution choke valve 23, absorbed Simultaneously heat release is in cryogen liquid for refrigerant vapour, and the weak solution of the 3rd absorber 21 is through the second solution pump 15 and the second solution heat exchanger 16 Into the second absorber 14, absorption refrigerant vapour and heat release in heated medium;The weak solution of second absorber 14 is molten through second Generation-evaporator 1 is flowed through after liquid heat exchanger 16, solution heat exchanger 6 and solution choke valve 7, after heat absorbing part vaporization Into a point steam chest 8, a point steam chest 8 discharges and provides refrigerant vapour to condenser 3;The refrigerant vapour heat release of condenser 3 is situated between in cooling Matter is divided into three tunnels into cryogen liquid, the cryogen liquid of condenser 3 --- and the first via enters evaporator 13, heat absorption through the pressurization of cryogen liquid pump 5 There is provided into refrigerant vapour and to absorber 2, the 3rd absorber 21, heat absorption are flowed through after the pressurization of second tunnel the second cryogen liquid pump 19 There is provided into refrigerant vapour and to the second absorber 14, generation-evaporator is flowed through after the pressurization of the cryogen liquid pump 22 of the 3rd tunnel the 3rd 1st, absorb heat into refrigerant vapour and provided to the 3rd absorber 21, form the dynamic co-feeding system of heat.
Heat shown in Figure 19 moves what co-feeding system was realized in:
(1) in structure, it is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution Heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat Exchanger is constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10, which also has, to be arranged Vapour passage is connected with generation-evaporator 1, and generation-evaporator 1 also has condensate liquid pipeline and ft connection, and engine 10 also has the Two steam channels are connected with heat exchanger 9, and heat exchanger 9 also has the second condensate liquid pipeline and ft connection;Steam chest 8 is divided to have dense molten Liquid pipeline is connected through solution pump 4 and solution heat exchanger 6 with absorber 2, and absorber 2 also has weak solution pipeline and the 3rd absorber 21 connections, the 3rd absorber 21 also has weak solution pipeline to be absorbed through the second solution pump 15 and the second solution heat exchanger 16 and second Device 14 is connected, and the second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, solution section Stream valve 7 and generation-evaporator 1 are connected with a point steam chest 8, and point steam chest 8 also has refrigerant steam channel to be connected with the 4th absorber 24, the Four absorbers 24 also have weak solution pipeline through the 3rd solution pump 25, the 3rd solution heat exchanger 26 and generation-evaporator 1 and second Steam chest 17 is divided to connect, second point of steam chest 17 also has concentrated solution pipeline to connect through the 3rd solution heat exchanger 26 and the 4th absorber 24 Logical, second point of steam chest 17 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline through cryogen liquid pump 5 After being connected with generation-evaporator 1 generation-evaporator 1 have again refrigerant steam channel respectively with the absorber 21 of absorber 2 and the 3rd Connection, the 3rd absorber 21 after the also cryogen liquid pipeline of condenser 3 is connected through the second cryogen liquid pump 19 with the 3rd absorber 21 There is refrigerant steam channel to be connected with the second absorber 14 again, the absorber 24 of condenser 3 and the 4th also has cooling medium pipeline respectively With ft connection, the absorber 14 of absorber 2 and second also has heated medium pipeline and ft connection respectively, and heat exchanger 9 is also There are heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the second steam, the Two steam in heat exchanger 9 heat release in heated medium into being discharged through the second condensate liquid pipeline after condensate liquid, engine 10 Steam discharge is provided to generation-evaporator 1, the heat release in generation-evaporator 1 of all or part of steam discharge is discharged into condensate liquid;Divide steam chest 8 Concentrated solution enter absorber 2 through solution pump 4 and solution heat exchanger 6, absorb refrigerant vapour and heat release is in heated medium, inhale The weak solution for receiving device 2 enters the 3rd absorber 21, absorption refrigerant vapour and heat release in cryogen liquid, the weak solution of the 3rd absorber 21 Enter the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release is in heated Medium;The weak solution of second absorber 14 is after the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve 7 Generation-evaporator 1 is flowed through, heat absorbing part vaporization enters a point steam chest 8, and a point steam chest 8 discharges and provides cryogen to the 4th absorber 24 Steam;The weak solution of 4th absorber 24 flows through generation-evaporation after the 3rd solution pump 25 and the 3rd solution heat exchanger 26 Enter second point of steam chest 17 after device 1, heat absorbing part vaporization, the concentrated solution of second point of steam chest 17 is through the 3rd solution heat exchanger 26 Into the 4th absorber 24, absorbing refrigerant vapour, simultaneously heat release is in cooling medium, and second point of steam chest 17 discharges and provided to condenser 3 Refrigerant vapour;The refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 is divided into two-way --- the Generation-evaporator 1 is flowed through after being pressurizeed all the way through cryogen liquid pump 5, absorb heat into refrigerant vapour and respectively to the suction of absorber 2 and the 3rd Receive device 21 provide, second tunnel the second cryogen liquid pump 19 pressurization after flow through the 3rd absorber 21, absorb heat into refrigerant vapour and to Second absorber 14 is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 20 moves what co-feeding system was realized in:
(1) in structure, it is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat Exchanger is constituted;Engine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10, which also has, to be arranged Vapour passage is connected with generator 12, and generator 12 also has condensate liquid pipeline and ft connection, and engine 10 also has the second steam to lead to The finisher 13 that road is connected with evaporator 13 has the second condensate liquid pipeline and ft connection again, and engine 10 also has the 3rd steam Passage is connected with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection;Steam chest 8 is divided to have concentrated solution pipeline Connected through solution pump 4 and solution heat exchanger 6 with absorber 2, absorber 2 also has weak solution pipeline to connect with the 3rd absorber 21 Logical, the 3rd absorber 21 also has weak solution pipeline through the second solution pump 15 and the second solution heat exchanger 16 and the second absorber 14 Connection, the second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16, solution heat exchanger 6, solution choke valve 7 Connected with generator 12 with a point steam chest 8, point steam chest 8 also has refrigerant steam channel to be connected with the 4th absorber 24, the 4th absorber 24 also have weak solution pipeline to connect through the 3rd solution pump 25, the 3rd solution heat exchanger 26 and generator 12 and second point of steam chest 17 Logical, second point of steam chest 17 also has concentrated solution pipeline to be connected through the 3rd solution heat exchanger 26 with the 4th absorber 24, second point of vapour Room 17 also has refrigerant steam channel to be connected with condenser 3, and condenser 3 also has cryogen liquid pipeline through cryogen liquid pump 5 and evaporator 13 Connection, evaporator 13 also has refrigerant steam channel to be connected respectively with the absorber 21 of absorber 2 and the 3rd, and condenser 3 also has cryogen The 3rd absorber 21 has refrigerant steam channel and the again after liquid pipeline is connected through the second cryogen liquid pump 19 with the 3rd absorber 21 Two absorbers 14 are connected, and the absorber 24 of condenser 3 and the 4th also has cooling medium pipeline and ft connection, the He of absorber 2 respectively Second absorber 14 also has heated medium pipeline and ft connection respectively, and heat exchanger 9 also has heated medium pipeline and outer Portion is connected.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 There is provided the second steam to evaporator 13, the second steam in evaporator 13 heat release into after condensate liquid through the second condensate liquid tubes rows Go out, engine 10 provides steam discharge to generator 12, the heat release in generator 12 of all or part of steam discharge is discharged into condensate liquid;Divide vapour The concentrated solution of room 8 enters absorber 2 through solution pump 4 and solution heat exchanger 6, absorbs refrigerant vapour and heat release is in heated Jie Matter, the weak solution of absorber 2 enters the 3rd absorber 21, absorbs refrigerant vapour and heat release is in cryogen liquid, the 3rd absorber 21 Weak solution enter the second absorber 14 through the second solution pump 15 and the second solution heat exchanger 16, absorb refrigerant vapour and heat release in Heated medium;The weak solution of second absorber 14 is through the second solution heat exchanger 16, solution heat exchanger 6 and solution choke valve Generator 12 is flowed through after 7, enters a point steam chest 8 after heat absorbing part vaporization, a point steam chest 8 discharges and provided to the 4th absorber 24 Refrigerant vapour;The weak solution of 4th absorber 24 flows through generator after the 3rd solution pump 25 and the 3rd solution heat exchanger 26 12nd, heat absorbing part vaporization enters second point of steam chest 17, and the concentrated solution of second point of steam chest 17 enters through the 3rd solution heat exchanger 26 4th absorber 24, absorption refrigerant vapour and heat release are in cooling medium, and second point of steam chest 17 discharges and provide cryogen to condenser 3 Steam;The refrigerant vapour heat release of condenser 3 is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 is divided into two-way --- and first Road enters evaporator 13 through the pressurization of cryogen liquid pump 5, absorbs heat into refrigerant vapour and carried respectively to the absorber 21 of absorber 2 and the 3rd For flowing through the 3rd absorber 21 after the pressurization of second tunnel the second cryogen liquid pump 19, absorbing heat into refrigerant vapour and absorbed to second Device 14 is provided, and forms the dynamic co-feeding system of heat.
Heat shown in Figure 21 moves what co-feeding system was realized in:
(1) in structure, it mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, second occur Device, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Power Machine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10 also has exhaust passage and second to occur Device 18 is connected, and the second generator 18 also has condensate liquid pipeline and ft connection, and engine 10 also has the second steam channel to connect successively The finisher 13 of logical generator 12 and evaporator 13 has the second condensate liquid pipeline and ft connection again, and engine 10 also has the 3rd Steam channel is connected with heat exchanger 9, and heat exchanger 9 also has the 3rd condensate liquid pipeline and ft connection;Generator 12 is also dense Solution line is connected through solution pump 4 and solution heat exchanger 6 with absorber 2, and absorber 2 also has weak solution pipeline and the 3rd to absorb Device 21 is connected, and the 3rd absorber 21 also has weak solution pipeline to be inhaled through the second solution pump 15 and the second solution heat exchanger 16 and second Receive device 14 to connect, the second absorber 14 also has weak solution pipeline through the second solution heat exchanger 16 and solution heat exchanger 6 and hair Raw device 12 is connected, and generator 12 also has refrigerant steam channel to be connected with the 4th absorber 24, and the 4th absorber 24 also has weak solution Pipeline is connected through the 3rd solution pump 25, the 3rd solution heat exchanger 26 and the second generator 18 with a point steam chest 8, and a point steam chest 8 also has Concentrated solution pipeline is connected through the 3rd solution heat exchanger 26 with the 4th absorber 24, point steam chest 8 also have refrigerant steam channel with it is cold Condenser 3 is connected, and condenser 3 also has cryogen liquid pipeline to be connected through cryogen liquid pump 5 with evaporator 13, and evaporator 13 also has refrigerant vapour Passage is connected with the absorber 21 of absorber 2 and the 3rd respectively, and condenser 3 also has cryogen liquid pipeline through the second cryogen liquid pump 19 and the The 3rd absorber 21 has refrigerant steam channel to be connected with the second absorber 14 again after the connection of three absorbers 21, condenser 3 and the Four absorbers 24 also have cooling medium pipeline and ft connection respectively, and the absorber 14 of absorber 2 and second also has heated respectively Medium pipeline and ft connection, heat exchanger 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 3rd steam, the Three steam in heat exchanger 9 heat release in heated medium into being discharged through the 3rd condensate liquid pipeline after condensate liquid, engine 10 The second steam is provided to generator 12 and evaporator 13, and the second steam flows through generator 12 and evaporator 13, progressively heat release Cheng Leng Discharged after lime set through the second condensate liquid pipeline, engine 10 provides steam discharge to the second generator 18, all or part of steam discharge exists Heat release is discharged into condensate liquid in second generator 18;The concentrated solution of generator 12 enters through solution pump 4 and solution heat exchanger 6 inhales Device 2 is received, refrigerant vapour is absorbed and heat release is in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorbs cryogen Simultaneously heat release is in cryogen liquid for steam, and the weak solution of the 3rd absorber 21 enters through the second solution pump 15 and the second solution heat exchanger 16 Second absorber 14, absorption refrigerant vapour and heat release are in heated medium;The weak solution of second absorber 14 is through the second solution heat Exchanger 16 and solution heat exchanger 6 enter generator 12, heat absorption release refrigerant vapour and provided to the 4th absorber 24;4th The weak solution of absorber 24 flows through the second generator 18, endothermic section after the 3rd solution pump 25 and the 3rd solution heat exchanger 26 Vaporization is divided to enter a point steam chest 8, a point steam chest 8 discharges and to the offer refrigerant vapour of condenser 3, and the concentrated solution of point steam chest 8 is molten through the 3rd Liquid heat exchanger 26 enters the 4th absorber 24, absorbs refrigerant vapour and heat release is in cooling medium;The refrigerant vapour of condenser 3 is put Heat is in cooling medium into cryogen liquid, and the cryogen liquid of condenser 3 is divided into two-way --- and the first via enters evaporation through the pressurization of cryogen liquid pump 5 Device 13, absorb heat into refrigerant vapour and provided respectively to the absorber 21 of absorber 2 and the 3rd, second tunnel the second cryogen liquid pump 19 plus The 3rd absorber 21 is flowed through after pressure, refrigerant vapour is absorbed heat into and provided to the second absorber 14, the dynamic co-feeding system of heat is formed.
Heat shown in Figure 22 moves what co-feeding system was realized in:
(1) in structure, it mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, second occur Device, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Power Machine 10 connects working machine 11, and engine 10 has live steam passage and ft connection, and engine 10 also has exhaust passage and second to occur Device 18 is connected, and the second generator 18 also has condensate liquid pipeline and ft connection, and engine 10 also has the second steam channel with occurring Generator 12 has the second condensate liquid pipeline and ft connection again after device 12 is connected, and engine 10 also has the 3rd steam channel with steaming The finisher 13 of the hair connection of device 13 has the 3rd condensate liquid pipeline and a ft connection again, engine 10 also have the 4th steam channel and Heat exchanger 9 is connected, and heat exchanger 9 also has the 4th condensate liquid pipeline and ft connection;Generator 12 also has concentrated solution pipeline warp Solution pump 4 and solution heat exchanger 6 are connected with absorber 2, and absorber 2 also has weak solution pipeline to be connected with the 3rd absorber 21, 3rd absorber 21 also has weak solution pipeline to connect through the second solution pump 15 and the second solution heat exchanger 16 with the second absorber 14 Logical, the second absorber 14 also has weak solution pipeline to connect through the second solution heat exchanger 16 and solution heat exchanger 6 with generator 12 Logical, generator 12 also has refrigerant steam channel to be connected with the 4th absorber 24, and the 4th absorber 24 also weak solution pipeline is through the Three solution pumps 25, the 3rd solution heat exchanger 26 and the second generator 18 are connected with a point steam chest 8, and point steam chest 8 also has concentrated solution pipe The solution heat exchangers 26 of Lu Jing tri- are connected with the 4th absorber 24, and point steam chest 8 also has refrigerant steam channel to connect with condenser 3 Logical, condenser 3 also has cryogen liquid pipeline to be connected through cryogen liquid pump 5 with evaporator 13, and evaporator 13 also has refrigerant steam channel point Do not connected with the absorber 21 of absorber 2 and the 3rd, condenser 3 also has cryogen liquid pipeline to be absorbed through the second cryogen liquid pump 19 and the 3rd The 3rd absorber 21 has refrigerant steam channel to be connected with the second absorber 14 again after device 21 is connected, and condenser 3 and the 4th absorbs Device 24 also has cooling medium pipeline and ft connection respectively, and the absorber 14 of absorber 2 and second also has heated medium pipe respectively Road and ft connection, heat exchanger 9 also have heated medium pipeline and ft connection.
(2) in flow, live steam enters engine 10 and is depressured work done, and the heat exchanger 9 of engine 10 provides the 4th steam, the Four steam in heat exchanger 9 heat release in heated medium into being discharged through the 4th condensate liquid pipeline after condensate liquid, engine 10 There is provided the 3rd steam to evaporator 13, the 3rd steam in evaporator 13 heat release into after condensate liquid through the 3rd condensate liquid tubes rows Go out, engine 10 provides the second steam to generator 12, the second steam in generator 12 heat release into after condensate liquid through second Condensate liquid pipeline is discharged, and engine 10 provides steam discharge to the second generator 18, and all or part of steam discharge is in the second generator 18 Heat release is externally discharged into condensate liquid;The concentrated solution of generator 12 enters absorber 2 through solution pump 4 and solution heat exchanger 6, inhaled Receive refrigerant vapour and heat release is in heated medium, the weak solution of absorber 2 enters the 3rd absorber 21, absorbs refrigerant vapour and put Heat enters second through the second solution pump 15 and the second solution heat exchanger 16 and absorbed in cryogen liquid, the weak solution of the 3rd absorber 21 Device 14, absorption refrigerant vapour and heat release are in heated medium;The weak solution of second absorber 14 is through the second solution heat exchanger 16 Enter generator 12, heat absorption release refrigerant vapour with solution heat exchanger 6 and provided to the 4th absorber 24;4th absorber 24 Weak solution flowed through after the 3rd solution pump 25 and the 3rd solution heat exchanger 26 second generator 18, heat absorbing part vaporize into Enter a point steam chest 8, a point steam chest 8 discharges and provides refrigerant vapour to condenser 3, and the concentrated solution of point steam chest 8 is through the 3rd solution heat exchange Device 26 enters the 4th absorber 24, absorbs refrigerant vapour and heat release is in cooling medium;The refrigerant vapour heat release of condenser 3 is in cooling Medium is divided into two-way into cryogen liquid, the cryogen liquid of condenser 3 --- and the first via enters evaporator 13 through the pressurization of cryogen liquid pump 5, inhaled Heat is provided into refrigerant vapour and respectively to the absorber 21 of absorber 2 and the 3rd, after the pressurization of second tunnel the second cryogen liquid pump 19 The 3rd absorber 21 is flowed through, refrigerant vapour is absorbed heat into and provided to the second absorber 14, the dynamic co-feeding system of heat is formed.
The effect that the technology of the present invention can be realized --- heat proposed by the invention move co-feeding system have the effect that and Advantage:
(1) temperature difference between engine outlet steam discharge and cold environment is utilized, and realizes the conjunction of total system heat energy utilization Physics and chemistry.
(2) the first work done (generating) of high-grade steam, is used for heat supply after grade reduction, meets thermal energy step and utilize principle.
(3) a variety of concrete technical schemes are provided, numerous different actual states is coped with, there is the wider scope of application.
(4) during variable working condition, second-kind absorption-type heat pump heat supply flow can be preferentially used, the thermic load of heat exchanger has Adjust space, it is ensured that system it is efficient and flexible.
(5) steam discharge and engine intermediate extraction are combined the thermal source for absorption heat pump flow, to meet different user Considerable flexibility is brought with duty requirements.
(6) there is the double dominant of extraction for heat supply and condensing heat supply, heating demand change is largely avoided to generating electricity Influence.
(7) generation-evaporator can be used as the condensing unit of engine simultaneously, be that the layout of single unit system brings spirit Activity.
(8) type of the dynamic co-feeding system of heat is enriched, the application of second-kind absorption-type heat pump is extended, is conducive to more Making full use of for the temperature difference is realized using second-kind absorption-type heat pump well.

Claims (49)

1. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchange Device, solution choke valve, point steam chest, heat exchanger, engine and a working machine are constituted;Engine (10) connection working machine (11), Engine (10) has live steam passage and ft connection, also engine (10) or exhaust passage and ft connection, engine (10) Also exhaust passage is connected with generation-evaporator (1), and generation-evaporator (1) also has condensate liquid pipeline and ft connection, power Machine (10) also has the second steam channel to be connected with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline to connect with outside It is logical;Steam chest (8) is divided to have concentrated solution pipeline to be connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) Also weak solution pipeline is connected through solution heat exchanger (6), solution choke valve (7) and generation-evaporator (1) with a point steam chest (8), Steam chest (8) is divided to also have refrigerant steam channel to be connected with condenser (3), condenser (3) also has cryogen liquid pipeline through cryogen liquid pump (5) Generation-evaporator (1) has refrigerant steam channel to be connected with absorber (2) again after being connected with generation-evaporator (1), condenser (3) there are cooling medium pipeline and ft connection, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) there are heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, is that in the heat described in claim 1 moves co-feeding system, condenser (3) is had into cryogen liquid pipeline Generation-evaporator (1) has refrigerant steam channel and absorber again after being connected through cryogen liquid pump (5) with generation-evaporator (1) (2) connection, which is adjusted to condenser (3), has cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, and engine (10) sets up steam discharge Passage is connected with absorber (2), forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator and an evaporator are constituted;Engine (10) connects working machine (11), engine (10) has live steam passage and ft connection, also engine (10) or exhaust passage and ft connection, engine (10) exhaust passage is connected with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) finisher (13) for also having the second steam channel to be connected with evaporator (13) has the second condensate liquid pipeline to connect with outside again Logical, engine (10) also has the 3rd steam channel to be connected with heat exchanger (9), and heat exchanger (9) also has the 3rd condensate liquid pipeline With ft connection;Steam chest (8) is divided to have concentrated solution pipeline to be connected through solution pump (4) and solution heat exchanger (6) with absorber (2), Absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) and generator (12) and a point steam chest (8) Connection, a point steam chest (8) also has refrigerant steam channel to be connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cryogen liquid Pump (5) is connected with evaporator (13), and evaporator (13) also has refrigerant steam channel to be connected with absorber (2), and condenser (3) also has Cooling medium pipeline and ft connection, absorber (2) also have heated medium pipeline and ft connection, and heat exchanger (9) also has Heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, is in the heat described in claim 3 moves co-feeding system, to cancel evaporator, by engine (10) The finisher (13) for having the second steam channel to be connected with evaporator (13) has the second condensate liquid pipeline and ft connection, evaporation again Device (13) has refrigerant steam channel to connect with absorber (2) to be adjusted to engine (10) in the lump and have the second steam channel and absorber (2) connect, there is cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13) condenser (3) and be adjusted to condenser (3) and have Cryogen liquid pipeline forms the dynamic co-feeding system of heat through cryogen liquid pump (5) and ft connection.
5. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchange Device, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution heat Exchanger and second point of steam chest are constituted;Engine (10) connection working machine (11), engine (10) has live steam passage and outside Connection, engine (10) or also exhaust passage and ft connection, engine (10) also has exhaust passage and generation-evaporator (1) connect, generation-evaporator (1) also has condensate liquid pipeline and ft connection, engine (10) also have the second steam channel with Heat exchanger (9) is connected, and heat exchanger (9) also has the second condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipeline Connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) also has weak solution pipeline to be handed over through solution heat Parallel operation (6), solution choke valve (7) and generation-evaporator (1) are connected with a point steam chest (8), and a point steam chest (8) also has refrigerant vapour to lead to Road is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline through the second solution pump (15), the second solution Heat exchanger (16) and generation-evaporator (1) are connected with second point of steam chest (17), and second point of steam chest (17) also has concentrated solution pipeline Connected through the second solution heat exchanger (16) with the second absorber (14), second point of steam chest (17) also have refrigerant steam channel with it is cold Condenser (3) connect, condenser (3) also have cryogen liquid pipeline connected through cryogen liquid pump (5) with generation-evaporator (1) after generation- Evaporator (1) has refrigerant steam channel to be connected with absorber (2) again, and condenser (3) and the second absorber (14) also have cold respectively But medium pipeline and ft connection, absorber (2) also have heated medium pipeline and ft connection, and heat exchanger (9) also has quilt Medium pipeline and ft connection are heated, the dynamic co-feeding system of heat is formed.
6. the dynamic co-feeding system of heat, is that in the heat described in claim 5 moves co-feeding system, condenser (3) is had into cryogen liquid pipeline Generation-evaporator (1) has refrigerant steam channel and absorber again after being connected through cryogen liquid pump (5) with generation-evaporator (1) (2) connection, which is adjusted to condenser (3), has cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, and engine (10) sets up steam discharge Passage is connected with absorber (2), forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger and second point of steam chest are constituted;Engine (10) connection working machine (11), engine (10) has live steam passage and outer Portion is connected, and engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage and generator (12) Connection, generator (12) also has condensate liquid pipeline and ft connection, and engine (10) also has the second steam channel and evaporator (13) finisher (13) of connection has the second condensate liquid pipeline and ft connection again, and engine (10) also has the 3rd steam channel Connected with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipe Road is connected through solution pump (4) and solution heat exchanger (6) with absorber (2), and absorber (2) also has weak solution pipeline through solution heat Exchanger (6), solution choke valve (7) and generator (12) are connected with a point steam chest (8), and a point steam chest (8) also has refrigerant steam channel Connected with the second absorber (14), the second absorber (14) also has weak solution pipeline through the second solution pump (15), the second solution heat Exchanger (16) and generator (12) are connected with second point of steam chest (17), and second point of steam chest (17) also has concentrated solution pipeline through second Solution heat exchanger (16) is connected with the second absorber (14), and second point of steam chest (17) also has refrigerant steam channel and condenser (3) connect, condenser (3) also has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13), and evaporator (13) is also cold Agent steam channel is connected with absorber (2), and condenser (3) and the second absorber (14) also have cooling medium pipeline and outside respectively Connection, absorber (2) also has heated medium pipeline and ft connection, and heat exchanger (9) also has heated medium pipeline and outer Portion is connected, and forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is in the heat described in claim 7 moves co-feeding system, to cancel evaporator, by engine (10) The finisher (13) for having the second steam channel to be connected with evaporator (13) has the second condensate liquid pipeline and ft connection, evaporation again Device (13) has refrigerant steam channel to connect with absorber (2) to be adjusted to engine (10) in the lump and have refrigerant steam channel and absorber (2) connect, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, mainly by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat exchange Device, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, second Solution heat exchanger and second point of steam chest are constituted;Engine (10) connection working machine (11), engine (10) has live steam passage With ft connection, also engine (10) or exhaust passage and ft connection, engine (10) also has exhaust passage and generator (12) connecting, generator (12) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam channel and occurs- Evaporator (1) is connected, and generation-evaporator (1) also has the second condensate liquid pipeline and ft connection, and engine (10) also has the 3rd steaming Vapour passage is connected with heat exchanger (9), and heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Steam chest (8) is divided to have dense Solution line is connected through solution pump (4) and solution heat exchanger (6) with absorber (2), and absorber (2) also has weak solution pipeline warp Solution heat exchanger (6), solution choke valve (7) and generation-evaporator (1) are connected with a point steam chest (8), and point steam chest (8) is also cold Agent steam channel is connected with the second absorber (14), the second absorber (14) also have weak solution pipeline through the second solution pump (15), Second solution heat exchanger (16) and generator (12) are connected with second point of steam chest (17), and second point of steam chest (17) also has concentrated solution Pipeline is connected through the second solution heat exchanger (16) with the second absorber (14), and second point of steam chest (17) also has refrigerant steam channel Connected with condenser (3), condenser (3) also has after cryogen liquid pipeline connects through cryogen liquid pump (5) with generation-evaporator (1) Generation-evaporator (1) has refrigerant steam channel to be connected with absorber (2) again, and condenser (3) and the second absorber (14) are also distinguished There are cooling medium pipeline and ft connection, absorber (2) also has heated medium pipeline and ft connection, and heat exchanger (9) is also 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 that in the heat described in claim 9 moves co-feeding system, condenser (3) is had into cryogen liquid pipeline Generation-evaporator (1) has refrigerant steam channel and absorber again after being connected through cryogen liquid pump (5) with generation-evaporator (1) (2) connection, which is adjusted to condenser (3), has cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, and engine (10) sets up second Steam channel is connected with absorber (2), forms the dynamic co-feeding system of heat.
11. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution heat exchanger and Second generator is constituted;Engine (10) connection working machine (11), engine (10) has live steam passage and ft connection, power Machine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage to be connected with generator (12), generator (12) there are condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be sequentially communicated the second generator (18) There are the second condensate liquid pipeline and ft connection again with the finisher (13) of evaporator (13), engine (10) also has the 3rd steam Passage is connected with heat exchanger (9), and heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Second generator (18) Also concentrated solution pipeline is connected through solution pump (4) and solution heat exchanger (6) with absorber (2), and absorber (2) also has weak solution Pipeline is connected through solution heat exchanger (6) with the second generator (18), and the second generator (18) also has refrigerant steam channel and the Two absorbers (14) are connected, and the second absorber (14) also has weak solution pipeline through the second solution pump (15), the second solution heat exchange Device (16) and generator (12) are connected with a point steam chest (8), and a point steam chest (8) also has concentrated solution pipeline through the second solution heat exchanger (16) connected with the second absorber (14), a point steam chest (8) also has refrigerant steam channel to be connected with condenser (3), condenser (3) is also There is cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13), evaporator (13) also has refrigerant steam channel and absorber (2) connect, condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, and absorber (2) also has Heated medium pipeline and ft connection, heat exchanger (9) also have heated medium pipeline and ft connection, form the dynamic alliance of heat System.
12. the dynamic co-feeding system of heat, is in the heat described in claim 11 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for having the second steam channel to be sequentially communicated the second generator (18) and evaporator (13) has second cold again Lime set pipeline and ft connection be adjusted to engine (10) have the second steam channel connected with the second generator (18) after second Generator (18) has the second condensate liquid pipeline and ft connection again, and evaporator (13) is had into refrigerant steam channel and absorber (2) Connection is adjusted to engine (10) and sets up the second steam channel to connect with absorber (2), has cryogen liquid pipeline to pass through condenser (3) Cryogen liquid pump (5) is connected with evaporator (13) to be adjusted to condenser (3) and has cryogen liquid pipeline to connect through cryogen liquid pump (5) with outside It is logical, form the dynamic co-feeding system of heat.
13. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, second point of steam chest and the second generator are constituted;Engine (10) connection working machine (11), engine (10) has newly Vapour passage and ft connection, engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage with Generator (12) is connected, and generator (12) also has condensate liquid pipeline and ft connection, and engine (10) also has the second steam channel Connected with the second generator (18), the second generator (18) also has the second condensate liquid pipeline and ft connection, and engine (10) is also The finisher (13) for having the 3rd steam channel to be connected with evaporator (13) has the 3rd condensate liquid pipeline and ft connection, power again Machine (10) also has the 4th steam channel to be connected with heat exchanger (9), and heat exchanger (9) also has the 4th condensate liquid pipeline to connect with outside It is logical;Steam chest (8) is divided to have concentrated solution pipeline to be connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) Also weak solution pipeline is connected through solution heat exchanger (6), solution choke valve (7) and the second generator (18) with a point steam chest (8), Steam chest (8) is divided to also have refrigerant steam channel to be connected with the second absorber (14), the second absorber (14) also has weak solution pipeline warp Second solution pump (15), the second solution heat exchanger (16) and generator (12) are connected with second point of steam chest (17), second point of vapour Room (17) also has concentrated solution pipeline to be connected through the second solution heat exchanger (16) with the second absorber (14), second point of steam chest (17) Also refrigerant steam channel is connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cryogen liquid pump (5) and evaporator (13) connect, evaporator (13) also has refrigerant steam channel to be connected with absorber (2), condenser (3) and the second absorber (14) Also there are cooling medium pipeline and ft connection respectively, absorber (2) also has heated medium pipeline and ft connection, heat exchanger (9) there are heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
14. the dynamic co-feeding system of heat, is in the heat described in claim 13 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the 3rd steam channel to be connected with evaporator (13) have again the 3rd condensate liquid pipeline and ft connection, Evaporator (13) have refrigerant steam channel connected with absorber (2) be adjusted in the lump engine (10) have the 3rd steam channel with suction Device (2) connection is received, has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13) condenser (3) and is adjusted to condenser (3) there is cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
15. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution heat exchanger and Second generator is constituted;Engine (10) connection working machine (11), engine (10) has live steam passage and ft connection, power Machine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage to be connected with generator (12), generator (12) there are condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to connect it with the second generator (18) The second generator (18) has the second condensate liquid pipeline and ft connection again afterwards, and engine (10) also has the 3rd steam channel and evaporation The finisher (13) of device (13) connection has the 3rd condensate liquid pipeline and ft connection again, and engine (10) also has the 4th steam to lead to Road is connected with heat exchanger (9), and heat exchanger (9) also has the 4th condensate liquid pipeline and ft connection;Second generator (18) is also There is concentrated solution pipeline to be connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) also has weak solution pipe Road is connected through solution heat exchanger (6) with the second generator (18), and the second generator (18) also has refrigerant steam channel and second Absorber (14) is connected, and the second absorber (14) also has weak solution pipeline through the second solution pump (15), the second solution heat exchanger (16) connected with generator (12) with a point steam chest (8), a point steam chest (8) also has concentrated solution pipeline through the second solution heat exchanger (16) Connected with the second absorber (14), a point steam chest (8) also has refrigerant steam channel to be connected with condenser (3), and condenser (3) also has Cryogen liquid pipeline is connected through cryogen liquid pump (5) with evaporator (13), and evaporator (13) also has refrigerant steam channel and absorber (2) Connection, condenser (3) and the second absorber (14) also have cooling medium pipeline and ft connection respectively, and absorber (2) also has quilt Medium pipeline and ft connection are heated, heat exchanger (9) also has heated medium pipeline and ft connection, form the dynamic alliance system of heat System.
16. the dynamic co-feeding system of heat, is in the heat described in claim 15 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the 3rd steam channel to be connected with evaporator (13) have again the 3rd condensate liquid pipeline and ft connection, Evaporator (13) have refrigerant steam channel connected with absorber (2) be adjusted in the lump engine (10) have the 3rd steam channel with suction Device (2) connection is received, has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13) condenser (3) and is adjusted to condenser (3) there is cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
17. the dynamic co-feeding system of heat, is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump and second point of vapour Room is constituted;Engine (10) connection working machine (11), engine (10) has live steam passage and a ft connection, engine (10) or Also exhaust passage and ft connection, engine (10) also have exhaust passage to be connected with generation-evaporator (1), generation-evaporator (1) there are condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be connected with heat exchanger (9), heat is handed over Parallel operation (9) also has the second condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipeline through solution pump (4) and solution heat Exchanger (6) is connected with absorber (2), and absorber (2) also has weak solution pipeline through solution heat exchanger (6) and the second absorber (14) connect, the second absorber (14) also has weak solution pipeline through the second solution pump (15) and generation-evaporator (1) and second point Steam chest (17) is connected, and second point of steam chest (17) also has concentrated solution pipeline through solution choke valve (7) and generation-evaporator (1) with dividing Steam chest (8) is connected, and a point steam chest (8) also has refrigerant steam channel to be connected with the second absorber (14), and second point of steam chest (17) also has Refrigerant steam channel is connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cryogen liquid pump (5) and generation-evaporator (1) generation-evaporator (1) has refrigerant steam channel to be connected with absorber (2) again after connecting, and condenser (3) and second absorbs Device (14) also has cooling medium pipeline and ft connection respectively, and absorber (2) also has heated medium pipeline and ft connection, heat Exchanger (9) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
18. the dynamic co-feeding system of heat, is that in the heat described in claim 17 moves co-feeding system, condenser (3) is had into cryogen liquid pipe Generation-evaporator (1) has refrigerant steam channel and absorber again after road is connected through cryogen liquid pump (5) with generation-evaporator (1) (2) connection, which is adjusted to condenser (3), has cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, and engine (10) sets up steam discharge Passage is connected with absorber (2), forms the dynamic co-feeding system of heat.
19. the dynamic co-feeding system of heat, is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat are handed over Parallel operation and second point of steam chest are constituted;Engine (10) connection working machine (11), engine (10) has live steam passage to connect with outside Logical, engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage to be connected with generator (12), Generator (12) also has condensate liquid pipeline and ft connection, and engine (10) also has the second steam channel generation-evaporator (1) even Logical, generation-evaporator (1) also has the second condensate liquid pipeline and ft connection, and engine (10) also has the 3rd steam channel and heat Exchanger (9) is connected, and heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipeline warp Solution pump (4) and solution heat exchanger (6) are connected with absorber (2), and absorber (2) also has weak solution pipeline through solution heat exchange Device (6) is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline through the second solution pump (15), second molten Liquid heat exchanger (16) and generation-evaporator (1) are connected with second point of steam chest (17), and second point of steam chest (17) also has concentrated solution Pipeline is connected through the second solution heat exchanger (17) and generator (12) with a point steam chest (8), and a point steam chest (8) also has refrigerant vapour to lead to Road is connected with the second absorber (14), and second point of steam chest (17) also has refrigerant steam channel to be connected with condenser (3), condenser (3) also have cryogen liquid pipeline connected through cryogen liquid pump (5) with generation-evaporator (1) after generation-evaporator (1) have cryogen again Steam channel is connected with absorber (2), and condenser (3) and the second absorber (14) also have cooling medium pipeline to connect with outside respectively Logical, absorber (2) also has heated medium pipeline and ft connection, and heat exchanger (9) also has heated medium pipeline and outside Connection, forms the dynamic co-feeding system of heat.
20. the dynamic co-feeding system of heat, is that in the heat described in claim 19 moves co-feeding system, condenser (3) is had into cryogen liquid pipe Generation-evaporator (1) has refrigerant steam channel and absorber again after road is connected through cryogen liquid pump (5) with generation-evaporator (1) (2) connection, which is adjusted to condenser (3), has cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, and engine (10) sets up second Steam channel is connected with absorber (2), forms the dynamic co-feeding system of heat.
21. the dynamic co-feeding system of heat, is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the Two solution heat exchangers and the second cryogen liquid pump are constituted;Engine (10) connection working machine (11), engine (10) has live steam Passage and ft connection, engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage and hair Life-evaporator (1) is connected, and generation-evaporator (1) also has condensate liquid pipeline and ft connection, and engine (10) also has the second steaming Vapour passage is connected with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection;Steam chest (8) is divided to have dense Solution line is connected through solution pump (4) and solution heat exchanger (6) with absorber (2), and absorber (2) also has weak solution pipeline warp Solution heat exchanger (6), solution choke valve (7) and generation-evaporator (1) are connected with a point steam chest (8), and point steam chest (8) is also cold Generator (12) has cryogen liquid pipeline to be connected with the second cryogen liquid pump (19) again after agent steam channel is connected with generator (12), Second cryogen liquid pump (19) also have cryogen liquid pipeline connected with generation-evaporator (1) after generation-evaporator (1) have cryogen again Steam channel is connected with absorber (2);Generator (12) also has concentrated solution pipeline through the second solution pump (15) and the second solution heat Exchanger (16) is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16) connected with generator (12), generator (12) also has refrigerant steam channel to be connected with condenser (3), condenser (3) also has Generation-evaporator (1) has refrigerant steam channel again after cryogen liquid pipeline is connected through cryogen liquid pump (5) with generation-evaporator (1) Connected with the second absorber (14), condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and second absorb Device (14) also has heated medium pipeline and ft connection respectively, and heat exchanger (9) also has heated medium pipeline to connect with outside It is logical, form the dynamic co-feeding system of heat.
22. the dynamic co-feeding system of heat, is that in the heat described in claim 21 moves co-feeding system, the second cryogen liquid pump (19) is had into cold Generation-evaporator (1) has refrigerant steam channel to be connected with absorber (2) again after agent liquid pipeline is connected with generation-evaporator (1) Being adjusted to the second cryogen liquid pump (19) has cryogen liquid pipeline and ft connection, and engine (10) sets up exhaust passage and absorber (2) connect, form the dynamic co-feeding system of heat.
23. the dynamic co-feeding system of heat, is that in the heat described in claim 21 moves co-feeding system, the second cryogen liquid pump (19) is had into cold Generation-evaporator (1) has refrigerant steam channel to be connected with absorber (2) again after agent liquid pipeline is connected with generation-evaporator (1) Being adjusted to the second cryogen liquid pump (19) has cryogen liquid pipeline and ft connection, and condenser (3) is had into cryogen liquid pipeline through cryogen liquid Generation-evaporator (1) has refrigerant steam channel to connect with the second absorber (14) again after pump (5) is connected with generation-evaporator (1) Logical to be adjusted to condenser (3) and have cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, engine (10) sets up exhaust passage point Do not connected with absorber (2) and the second absorber (14), form the dynamic co-feeding system of heat.
24. the dynamic co-feeding system of heat, is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat It is parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, second molten Liquid pump, the second solution heat exchanger and the second cryogen liquid pump are constituted;Engine (10) connection working machine (11), engine (10) There are live steam passage and ft connection, also engine (10) or exhaust passage and ft connection, engine (10) also has steam discharge to lead to Road is connected with generation-evaporator (1), and generation-evaporator (1) also has condensate liquid pipeline and ft connection, and engine (10) also has The finisher (13) that second steam channel is connected with evaporator (13) has the second condensate liquid pipeline and ft connection, engine again (10) the 3rd steam channel is connected with heat exchanger (9), heat exchanger (9) also has the 3rd condensate liquid pipeline to connect with outside It is logical;Steam chest (8) is divided to have concentrated solution pipeline to be connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) Also weak solution pipeline is connected through solution heat exchanger (6), solution choke valve (7) and generation-evaporator (1) with a point steam chest (8), Point steam chest (8) also have refrigerant steam channel connected with generator (12) after generator (12) have cryogen liquid pipeline cold through second again Agent liquid pump (19) is connected with evaporator (13), and evaporator (13) also has refrigerant steam channel to be connected with absorber (2);Generator (12) concentrated solution pipeline is connected through the second solution pump (15) and the second solution heat exchanger (16) with the second absorber (14), Second absorber (14) also has weak solution pipeline to be connected through the second solution heat exchanger (16) with generator (12), generator (12) Also refrigerant steam channel is connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cryogen liquid pump (5) and generation-steaming Generation-evaporator (1) has refrigerant steam channel to be connected with the second absorber (14) again after hair device (1) connection, and condenser (3) is also There are cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and outer respectively Portion is connected, and heat exchanger (9) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
25. the dynamic co-feeding system of heat, is in the heat described in claim 24 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the second steam channel to be connected with evaporator (13) have again the second condensate liquid pipeline and ft connection, Evaporator (13) have refrigerant steam channel connected with absorber (2) be adjusted in the lump engine (10) have the second steam channel with suction Device (2) connection is received, has cryogen liquid pipeline to be connected through the second cryogen liquid pump (19) with evaporator (13) in generator (12) and is adjusted to Generator (12) has cryogen liquid pipeline through the second cryogen liquid pump (19) and ft connection, forms the dynamic co-feeding system of heat.
26. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, the second generator, the second cryogen liquid pump and the second evaporator are constituted;Engine (10) connection working machine (11), Engine (10) has live steam passage and ft connection, also engine (10) or exhaust passage and ft connection, engine (10) Also exhaust passage is connected with generator (12), and generator (12) also has condensate liquid pipeline and ft connection, and engine (10) is also Have the second steam channel to be sequentially communicated the second evaporator (20) after evaporator (13) and the second evaporator (20) has second cold again Lime set pipeline and ft connection, engine (10) also have the 3rd steam channel to be connected with heat exchanger (9), and heat exchanger (9) is also There are the 3rd condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipeline through solution pump (4) and solution heat exchanger (6) Connected with absorber (2), absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) and occurred Device (12) connect with a point steam chest (8), and a point steam chest (8) also has refrigerant steam channel second to be sent out after being connected with the second generator (18) Raw device (18) has cryogen liquid pipeline to be connected through the second cryogen liquid pump (19) with evaporator (13) again, and evaporator (13) also has cryogen steaming Vapour passage is connected with absorber (2);Second generator (18) also has concentrated solution pipeline through the second solution pump (15) and the second solution Heat exchanger (16) is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline through the second solution heat exchange Device (16) is connected with the second generator (18), and the second generator (18) also has refrigerant steam channel to be connected with condenser (3), condensation Device (3) also has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with the second evaporator (20), and the second evaporator (20) also has cryogen steaming Vapour passage is connected with the second absorber (14), and condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and Two absorbers (14) also have heated medium pipeline and a ft connection respectively, heat exchanger (9) also have heated medium pipeline with Ft connection, forms the dynamic co-feeding system of heat.
27. the dynamic co-feeding system of heat, is in the heat described in claim 26 moves co-feeding system, to cancel evaporator, by engine (10) have the second steam channel to be sequentially communicated the second evaporator (20) after evaporator (13) and the second evaporator (20) has the again Two condensate liquid pipelines and ft connection, which are adjusted to engine (10), to be had after the second steam channel connects with the second evaporator (20) Second evaporator (20) has the second condensate liquid pipeline and ft connection again, and evaporator (13) is had into refrigerant steam channel and absorber (2) connection is adjusted to engine (10) and sets up the second steam channel to connect with absorber (2), and the second generator (18) is had into cryogen Liquid pipeline is connected through the second cryogen liquid pump (19) with evaporator (13) to be adjusted to the second generator (18) and has cryogen liquid pipeline through Two cryogen liquid pumps (19) and ft connection, form the dynamic co-feeding system of heat.
28. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, the second generator, the second cryogen liquid pump and the second evaporator are constituted;Engine (10) connection working machine (11), Engine (10) has live steam passage and ft connection, also engine (10) or exhaust passage and ft connection, engine (10) Also exhaust passage is connected with generator (12), and generator (12) also has condensate liquid pipeline and ft connection, and engine (10) is also Have the second steam channel connected with the second evaporator (20) after the second evaporator (20) have again the second condensate liquid pipeline with it is outside Connection, the finisher (13) that engine (10) also has the 3rd steam channel to be connected with evaporator (13) has the 3rd condensate line again Road and ft connection, engine (10) also have the 4th steam channel to be connected with heat exchanger (9), and heat exchanger (9) also has the 4th Condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipeline through solution pump (4) and solution heat exchanger (6) with absorbing Device (2) is connected, and absorber (2) also has weak solution pipeline through solution heat exchanger (6), solution choke valve (7) and generator (12) Connect with a point steam chest (8), divide a steam chest (8) also have refrigerant steam channel connected with the second generator (18) after the second generator (18) cryogen liquid pipeline is connected through the second cryogen liquid pump (19) with evaporator (13) again, evaporator (13) also has refrigerant vapour to lead to Road is connected with absorber (2);Second generator (18) also has concentrated solution pipeline to be handed over through the second solution pump (15) and the second solution heat Parallel operation (16) is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16) connected with the second generator (18), the second generator (18) also has refrigerant steam channel to be connected with condenser (3), condenser (3) cryogen liquid pipeline is connected through cryogen liquid pump (5) with the second evaporator (20), the second evaporator (20) also has refrigerant vapour Passage is connected with the second absorber (14), and condenser (3) also has cooling medium pipeline and ft connection, absorber (2) and second Absorber (14) also has heated medium pipeline and ft connection respectively, and heat exchanger (9) also has heated medium pipeline and outer Portion is connected, and forms the dynamic co-feeding system of heat.
29. the dynamic co-feeding system of heat, is in the heat described in claim 28 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the 3rd steam channel to be connected with evaporator (13) have again the 3rd condensate liquid pipeline and ft connection, Evaporator (13) have refrigerant steam channel connected with absorber (2) be adjusted in the lump engine (10) have the 3rd steam channel with suction Device (2) connection is received, has cryogen liquid pipeline to connect tune with evaporator (13) through the second cryogen liquid pump (19) in the second generator (18) Whole is that the second generator (18) has cryogen liquid pipeline through the second cryogen liquid pump (19) and ft connection, forms the dynamic co-feeding system of heat.
30. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution It is valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, second molten Liquid heat exchanger, the second generator and the second cryogen liquid pump are constituted;Engine (10) connection working machine (11), engine (10) There are live steam passage and ft connection, also engine (10) or exhaust passage and ft connection, engine (10) also has steam discharge to lead to Road is connected with generator (12), and generator (12) also has condensate liquid pipeline and ft connection, and engine (10) also has the second steam The finisher (13) that passage is connected with evaporator (13) has the second condensate liquid pipeline and ft connection again, and engine (10) also has 3rd steam channel is connected with heat exchanger (9), and heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Divide steam chest (8) concentrated solution pipeline is connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) also has dilute molten Liquid pipeline is connected through solution heat exchanger (6), solution choke valve (7) and generator (12) with a point steam chest (8), and point steam chest (8) is also Have refrigerant steam channel connected with the second generator (18) after the second generator (18) have cryogen liquid pipeline again through the second cryogen Liquid pump (19) is connected with evaporator (13);Second generator (18) also has concentrated solution pipeline molten through the second solution pump (15) and second Liquid heat exchanger (16) is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline to be handed over through the second solution heat Parallel operation (16) is connected with the second generator (18), and the second generator (18) also has refrigerant steam channel to be connected with condenser (3), cold Condenser (3) also has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13), and evaporator (13) also has refrigerant steam channel Connect, condenser (3) also has cooling medium pipeline and ft connection, absorb with absorber (2) and the second absorber (14) respectively Device (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, and heat exchanger (9) also has heated Jie Matter pipeline and ft connection, form the dynamic co-feeding system of heat.
31. the dynamic co-feeding system of heat, is in the heat described in claim 30 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the second steam channel to be connected with evaporator (13) have again the second condensate liquid pipeline and ft connection, Evaporator (13) has refrigerant steam channel to connect with absorber (2) and the second absorber (14) respectively and be adjusted to engine in the lump (10) there is the second steam channel to be connected respectively with absorber (2) and the second absorber (14), condenser (3) is had into cryogen liquid pipeline Connected through cryogen liquid pump (5) with evaporator (13) and be adjusted to condenser (3) and there is cryogen liquid pipeline to connect through cryogen liquid pump (5) with outside It is logical, there is cryogen liquid pipeline to be connected through the second cryogen liquid pump (19) with evaporator (13) in the second generator (18) and be adjusted to the second hair Raw device (18) has cryogen liquid pipeline through the second cryogen liquid pump (19) and ft connection, forms the dynamic co-feeding system of heat.
32. the dynamic co-feeding system of heat, is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution Heat exchanger, the second cryogen liquid pump and the 3rd absorber are constituted;Engine (10) connection working machine (11), engine (10) has Live steam passage and ft connection, engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage Connected with generation-evaporator (1), generation-evaporator (1) also has condensate liquid pipeline and ft connection, engine (10) also has Two steam channels are connected with heat exchanger (9), and heat exchanger (9) also has the second condensate liquid pipeline and ft connection;Divide steam chest (8) There is concentrated solution pipeline to be connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) also has weak solution pipe The absorbers of Lu Yu tri- (21) are connected, and the 3rd absorber (21) also has weak solution pipeline through the second solution pump (15) and the second solution Heat exchanger (16) is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline through the second solution heat exchange Device (16), solution heat exchanger (6), solution choke valve (7) and generation-evaporator (1) are connected with a point steam chest (8), point steam chest (8) Also refrigerant steam channel is connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cryogen liquid pump (5) and generation-steaming Hair device (1) connection after generation-evaporator (1) have again refrigerant steam channel respectively with absorber (2) and the 3rd absorber (21) Connection, condenser (3) also have cryogen liquid pipeline connected through the second cryogen liquid pump (19) with the 3rd absorber (21) after the 3rd suction Receive device (21) has refrigerant steam channel to be connected with the second absorber (14) again, and condenser (3) also has cooling medium pipeline and outside Connection, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, and heat exchanger (9) is also There are heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
33. the dynamic co-feeding system of heat, is that in the heat described in claim 32 moves co-feeding system, condenser (3) is had into cryogen liquid pipe After road is connected through cryogen liquid pump (5) with generation-evaporator (1) generation-evaporator (1) have again refrigerant steam channel respectively with suction Receive device (2) and the connection of the 3rd absorber (21) is adjusted to condenser (3) and has cryogen liquid pipeline to connect through cryogen liquid pump (5) with outside Logical, engine (10) is set up exhaust passage and connected respectively with absorber (2) and the 3rd absorber (21), forms the dynamic alliance system of heat System.
34. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, the second cryogen liquid pump and the 3rd absorber are constituted;Engine (10) connection working machine (11), engine (10) has Live steam passage and ft connection, engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage Connected with generator (12), generator (12) also has condensate liquid pipeline and ft connection, engine (10) also has the second steam to lead to The finisher (13) that road is connected with evaporator (13) has the second condensate liquid pipeline and ft connection again, and engine (10) also has Three steam channels are connected with heat exchanger (9), and heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Divide steam chest (8) There is concentrated solution pipeline to be connected through solution pump (4) and solution heat exchanger (6) with absorber (2), absorber (2) also has weak solution pipe The absorbers of Lu Yu tri- (21) are connected, and the 3rd absorber (21) also has weak solution pipeline through the second solution pump (15) and the second solution Heat exchanger (16) is connected with the second absorber (14), and the second absorber (14) also has weak solution pipeline through the second solution heat exchange Device (16), solution heat exchanger (6), solution choke valve (7) and generator (12) are connected with a point steam chest (8), and a point steam chest (8) also has Refrigerant steam channel is connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cryogen liquid pump (5) and evaporator (13) Connection, evaporator (13) also has refrigerant steam channel to be connected respectively with absorber (2) and the 3rd absorber (21), condenser (3) The 3rd absorber (21) has cold again after also cryogen liquid pipeline is connected through the second cryogen liquid pump (19) with the 3rd absorber (21) Agent steam channel is connected with the second absorber (14), and condenser (3) also has cooling medium pipeline and ft connection, absorber (2) Also there are heated medium pipeline and ft connection respectively with the second absorber (14), heat exchanger (9) also has heated medium pipe Road and ft connection, form the dynamic co-feeding system of heat.
35. the dynamic co-feeding system of heat, is in the heat described in claim 34 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the second steam channel to be connected with evaporator (13) have again the second condensate liquid pipeline and ft connection, Evaporator (13) has refrigerant steam channel to connect with absorber (2) and the 3rd absorber (21) respectively and be adjusted to engine in the lump (10) there is the second steam channel to be connected respectively with absorber (2) and the 3rd absorber (21), condenser (3) is had into cryogen liquid pipeline Connected through cryogen liquid pump (5) with evaporator (13) and be adjusted to condenser (3) and there is cryogen liquid pipeline to connect through cryogen liquid pump (5) with outside It is logical, form the dynamic co-feeding system of heat.
36. the dynamic co-feeding system of heat, is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, evaporator, the second absorber, the second solution pump, the Two solution heat exchangers, the second cryogen liquid pump, the 3rd absorber, the 3rd cryogen liquid pump and the second solution choke valve are constituted;It is dynamic Power machine (10) connection working machine (11), engine (10) has live steam passage and ft connection, and engine (10) or also steam discharge lead to Road and ft connection, engine (10) also have exhaust passage to be connected with generation-evaporator (1), and generation-evaporator (1) is also cold Lime set pipeline and ft connection, engine (10) also have finisher (13) that the second steam channel connects with evaporator (13) again There are the second condensate liquid pipeline and ft connection, engine (10) also has the 3rd steam channel to be connected with heat exchanger (9), heat exchange Device (9) also has the 3rd condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipeline to be handed over through solution pump (4) and solution heat Parallel operation (6) is connected with absorber (2), and absorber (2) also has weak solution pipeline to be absorbed through the second solution choke valve (23) with the 3rd Device (21) is connected, and the 3rd absorber (21) also has weak solution pipeline through the second solution pump (15) and the second solution heat exchanger (16) Connected with the second absorber (14), the second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16), solution Heat exchanger (6), solution choke valve (7) and generation-evaporator (1) are connected with a point steam chest (8), and a point steam chest (8) also has cryogen steaming Vapour passage is connected with condenser (3), and condenser (3) also has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13), is steamed Hair device (13) also has refrigerant steam channel to be connected with absorber (2), and condenser (3) also has cryogen liquid pipeline through the second cryogen liquid pump (19) the 3rd absorber (21) has refrigerant steam channel to connect with the second absorber (14) again after being connected with the 3rd absorber (21) It is logical, condenser (3) also have cryogen liquid pipeline connected through the 3rd cryogen liquid pump (22) with generation-evaporator (1) after generation-evaporation Device (1) has refrigerant steam channel to be connected with the 3rd absorber (21) again, and condenser (3) also has cooling medium pipeline to connect with outside Logical, absorber (2) and the second absorber (14) also have heated medium pipeline and ft connection respectively, and heat exchanger (9) also has Heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
37. the dynamic co-feeding system of heat, is in the heat described in claim 36 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the second steam channel to be connected with evaporator (13) have again the second condensate liquid pipeline and ft connection, Evaporator (13) have refrigerant steam channel connected with absorber (2) be adjusted in the lump engine (10) have the second steam channel with suction Device (2) connection is received, has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13) condenser (3) and is adjusted to condenser (3) there is cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
38. the dynamic co-feeding system of heat, is in the heat described in claim 36 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the second steam channel to be connected with evaporator (13) have again the second condensate liquid pipeline and ft connection, Evaporator (13) have refrigerant steam channel connected with absorber (2) be adjusted in the lump engine (10) have the second steam channel with suction Device (2) connection is received, has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13) condenser (3) and is adjusted to condenser (3) there is cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, condenser (3) is had into cryogen liquid pipeline through the 3rd cryogen liquid pump (22) generation-evaporator (1) has refrigerant steam channel to connect with the 3rd absorber (21) again after being connected with generation-evaporator (1) Logical to be adjusted to condenser (3) and have cryogen liquid pipeline through the 3rd cryogen liquid pump (22) and ft connection, engine (10) sets up steam discharge Passage is connected with the 3rd absorber (21), forms the dynamic co-feeding system of heat.
39. the dynamic co-feeding system of heat, is mainly handed over by generation-evaporator, absorber, condenser, solution pump, cryogen liquid pump, solution heat Parallel operation, solution choke valve, point steam chest, heat exchanger, engine, working machine, the second absorber, the second solution pump, the second solution Heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat Exchanger is constituted;Engine (10) connection working machine (11), engine (10) has live steam passage and ft connection, engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage to be connected with generation-evaporator (1), occur- Evaporator (1) also has condensate liquid pipeline and ft connection, and engine (10) also has the second steam channel to connect with heat exchanger (9) Logical, heat exchanger (9) also has the second condensate liquid pipeline and ft connection;Point steam chest (8) have concentrated solution pipeline through solution pump (4) and Solution heat exchanger (6) is connected with absorber (2), and absorber (2) also has weak solution pipeline to be connected with the 3rd absorber (21), the Three absorbers (21) also have weak solution pipeline through the second solution pump (15) and the second solution heat exchanger (16) and the second absorber (14) connect, the second absorber (14) also have weak solution pipeline through the second solution heat exchanger (16), solution heat exchanger (6), Solution choke valve (7) and generation-evaporator (1) are connected with a point steam chest (8), and a point steam chest (8) also has refrigerant steam channel and the 4th Absorber (24) is connected, and the 4th absorber (24) also has weak solution pipeline through the 3rd solution pump (25), the 3rd solution heat exchanger (26) connected with generation-evaporator (1) with second point of steam chest (17), second point of steam chest (17) also has concentrated solution pipeline molten through the 3rd Liquid heat exchanger (26) is connected with the 4th absorber (24), and second point of steam chest (17) also has refrigerant steam channel and condenser (3) Connection, condenser (3) also have cryogen liquid pipeline connected through cryogen liquid pump (5) with generation-evaporator (1) after generation-evaporator (1) refrigerant steam channel is connected respectively with absorber (2) and the 3rd absorber (21) again, condenser (3) also has cryogen liquid pipe After road the second cryogen liquid pump (19) is connected with the 3rd absorber (21) the 3rd absorber (21) have again refrigerant steam channel with Second absorber (14) is connected, and condenser (3) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, is inhaled Receive device (2) and the second absorber (14) also has heated medium pipeline and ft connection respectively, and heat exchanger (9) also has heated Medium pipeline and ft connection, form the dynamic co-feeding system of heat.
40. the dynamic co-feeding system of heat, is that in the heat described in claim 39 moves co-feeding system, condenser (3) is had into cryogen liquid pipe After road is connected through cryogen liquid pump (5) with generation-evaporator (1) generation-evaporator (1) have again refrigerant steam channel respectively with suction Receive device (2) and the connection of the 3rd absorber (21) is adjusted to condenser (3) and has cryogen liquid pipeline to connect through cryogen liquid pump (5) with outside Logical, engine (10) is set up exhaust passage and connected respectively with absorber (2) and the 3rd absorber (21), forms the dynamic alliance system of heat System.
41. the dynamic co-feeding system of heat, is mainly throttled by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, solution Valve, point steam chest, heat exchanger, engine, working machine, generator, evaporator, the second absorber, the second solution pump, the second solution Heat exchanger, second point of steam chest, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat Exchanger is constituted;Engine (10) connection working machine (11), engine (10) has live steam passage and ft connection, engine (10) or also exhaust passage and ft connection, engine (10) also have exhaust passage to be connected with generator (12), generator (12) there are condensate liquid pipeline and ft connection, engine (10) also has the second steam channel to be steamed after being connected with evaporator (13) Hair device (13) has the second condensate liquid pipeline and ft connection again, and engine (10) also has the 3rd steam channel and heat exchanger (9) Connection, heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Steam chest (8) is divided to have concentrated solution pipeline through solution pump (4) Connected with solution heat exchanger (6) with absorber (2), absorber (2) also has weak solution pipeline to be connected with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be absorbed through the second solution pump (15) and the second solution heat exchanger (16) with second Device (14) is connected, and the second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16), solution heat exchanger (6), solution choke valve (7) and generator (12) are connected with a point steam chest (8), and a point steam chest (8) also has refrigerant steam channel and the 4th Absorber (24) is connected, and the 4th absorber (24) also has weak solution pipeline through the 3rd solution pump (25), the 3rd solution heat exchanger (26) connected with generator (12) with second point of steam chest (17), second point of steam chest (17) also has concentrated solution pipeline through the 3rd solution heat Exchanger (26) is connected with the 4th absorber (24), and second point of steam chest (17) also has refrigerant steam channel to be connected with condenser (3), Condenser (3) also has cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13), and evaporator (13) also has refrigerant vapour to lead to Road is connected with absorber (2) and the 3rd absorber (21) respectively, and condenser (3) also has cryogen liquid pipeline through the second cryogen liquid pump (19) the 3rd absorber (21) has refrigerant steam channel to connect with the second absorber (14) again after being connected with the 3rd absorber (21) Logical, condenser (3) and the 4th absorber (24) also have cooling medium pipeline and ft connection respectively, and absorber (2) and second inhale Receive device (14) also has heated medium pipeline and ft connection respectively, and heat exchanger (9) also has heated medium pipeline and outside Connection, forms the dynamic co-feeding system of heat.
42. the dynamic co-feeding system of heat, is in the heat described in claim 41 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the second steam channel to be connected with evaporator (13) have again the second condensate liquid pipeline and ft connection, Evaporator (13) has refrigerant steam channel to connect with absorber (2) and the 3rd absorber (21) respectively and be adjusted to engine in the lump (10) there is the second steam channel to be connected respectively with absorber (2) and the 3rd absorber (21), condenser (3) is had into cryogen liquid pipeline Connected through cryogen liquid pump (5) with evaporator (13) be adjusted to condenser (3) have cryogen liquid pipeline through cryogen liquid pump (5) with it is outside Connection, forms the dynamic co-feeding system of heat.
43. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, second occur Device, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Power Machine (10) connection working machine (11), engine (10) has live steam passage and ft connection, also engine (10) or exhaust passage With ft connection, engine (10) also has exhaust passage to be connected with the second generator (18), and the second generator (18) also has condensation Liquid pipeline and ft connection, engine (10) also have the second steam channel to be sequentially communicated after generator (12) and evaporator (13) Evaporator (13) has the second condensate liquid pipeline and ft connection again, and engine (10) also has the 3rd steam channel and heat exchanger (9) connect, heat exchanger (9) also has the 3rd condensate liquid pipeline and ft connection;Generator (12) also has concentrated solution pipeline through molten Liquid pump (4) and solution heat exchanger (6) are connected with absorber (2), and absorber (2) also has weak solution pipeline and the 3rd absorber (21) connect, the 3rd absorber (21) also have weak solution pipeline through the second solution pump (15) and the second solution heat exchanger (16) and Second absorber (14) is connected, and the second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16) and solution heat Exchanger (6) is connected with generator (12), and generator (12) also has refrigerant steam channel to be connected with the 4th absorber (24), and the 4th Absorber (24) also has weak solution pipeline through the 3rd solution pump (25), the 3rd solution heat exchanger (26) and the second generator (18 ) connected with a point steam chest (8), a point steam chest (8) also has concentrated solution pipeline through the 3rd solution heat exchanger (26) and the 4th absorber (24) connect, a point steam chest (8) also has refrigerant steam channel to be connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cold Agent liquid pump (5) is connected with evaporator (13), and evaporator (13) also has refrigerant steam channel to be absorbed respectively with absorber (2) and the 3rd Device (21) is connected, and condenser (3) also has after cryogen liquid pipeline connects through the second cryogen liquid pump (19) with the 3rd absorber (21) 3rd absorber (21) has refrigerant steam channel to be connected with the second absorber (14) again, condenser (3) and the 4th absorber (24) Also there are cooling medium pipeline and ft connection respectively, absorber (2) and the second absorber (14) also have heated medium pipe respectively Road and ft connection, heat exchanger (9) also have heated medium pipeline and ft connection, form the dynamic co-feeding system of heat.
44. the dynamic co-feeding system of heat, is in the heat described in claim 43 moves co-feeding system, to cancel evaporator, by engine (10) have the second steam channel to be sequentially communicated the finisher (13) that generator (12) connects with evaporator (13) has second cold again Lime set pipeline and ft connection be adjusted to engine (10) have the second steam channel connected with generator (12) after generator (12) have the second condensate liquid pipeline and ft connection again, by evaporator (13) have refrigerant steam channel respectively with absorber (2) and 3rd absorber (21) connection be adjusted to engine (10) set up the second steam channel respectively with absorber (2) and the 3rd absorber (21) connect, there is cryogen liquid pipeline to be connected through cryogen liquid pump (5) with evaporator (13) condenser (3) and be adjusted to condenser (3) There is cryogen liquid pipeline through cryogen liquid pump (5) and ft connection, form the dynamic co-feeding system of heat.
45. the dynamic co-feeding system of heat, mainly by absorber, condenser, solution pump, cryogen liquid pump, solution heat exchanger, point steam chest, Heat exchanger, engine, working machine, generator, the second absorber, the second solution pump, the second solution heat exchanger, second occur Device, the second cryogen liquid pump, the 3rd absorber, the 4th absorber, the 3rd solution pump and the 3rd solution heat exchanger are constituted;Power Machine (10) connection working machine (11), engine (10) has live steam passage and ft connection, also engine (10) or exhaust passage With ft connection, engine (10) also has exhaust passage to be connected with the second generator (18), and the second generator (18) also has condensation Liquid pipeline and ft connection, engine (10) also have the second steam channel connected with generator (12) after generator (12) have again Second condensate liquid pipeline and ft connection, engine (10) also have the finisher that the 3rd steam channel is connected with evaporator (13) (13) there are the 3rd condensate liquid pipeline and ft connection again, engine (10) also has the 4th steam channel to be connected with heat exchanger (9), Heat exchanger (9) also has the 4th condensate liquid pipeline and ft connection;Generator (12) also has concentrated solution pipeline through solution pump (4) Connected with solution heat exchanger (6) with absorber (2), absorber (2) also has weak solution pipeline to be connected with the 3rd absorber (21), 3rd absorber (21) also has weak solution pipeline to be absorbed through the second solution pump (15) and the second solution heat exchanger (16) with second Device (14) is connected, and the second absorber (14) also has weak solution pipeline through the second solution heat exchanger (16) and solution heat exchanger (6) connected with generator (12), generator (12) also has refrigerant steam channel to be connected with the 4th absorber (24), the 4th absorber (24) there is weak solution pipeline through the 3rd solution pump (25), the 3rd solution heat exchanger (26) and the second generator (18) with dividing Steam chest (8) is connected, and a point steam chest (8) also has concentrated solution pipeline to connect through the 3rd solution heat exchanger (26) and the 4th absorber (24) Logical, a point steam chest (8) also has refrigerant steam channel to be connected with condenser (3), and condenser (3) also has cryogen liquid pipeline through cryogen liquid pump (5) connected with evaporator (13), evaporator (13) also have refrigerant steam channel respectively with absorber (2) and the 3rd absorber (21) Connection, condenser (3) also have cryogen liquid pipeline connected through the second cryogen liquid pump (19) with the 3rd absorber (21) after the 3rd suction Receive device (21) has refrigerant steam channel to be connected with the second absorber (14) again, and condenser (3) and the 4th absorber (24) are also distinguished There are cooling medium pipeline and ft connection, absorber (2) and the second absorber (14) also have heated medium pipeline and outer respectively Portion is connected, and heat exchanger (9) also has heated medium pipeline and ft connection, forms the dynamic co-feeding system of heat.
46. the dynamic co-feeding system of heat, is in the heat described in claim 45 moves co-feeding system, to cancel evaporator, by engine (10) finisher (13) for thering is the 3rd steam channel to be connected with evaporator (13) have again the 3rd condensate liquid pipeline and ft connection, Evaporator (13) has refrigerant steam channel to connect with absorber (2) and the 3rd absorber (21) respectively and be adjusted to engine in the lump (10) there is the 3rd steam channel to be connected respectively with absorber (2) and the 3rd absorber (21), condenser (3) is had into cryogen liquid pipeline Connected through cryogen liquid pump (5) with evaporator (13) and be adjusted to condenser (3) and there is cryogen liquid pipeline to connect through cryogen liquid pump (5) with outside It is logical, form the dynamic co-feeding system of heat.
47. the dynamic co-feeding system of heat, is moved in any hot described in claim 1-2,5-6,17-18,21-23,32-33,39-40 In co-feeding system, cancel heat exchanger, cancel the heated medium pipeline connected with heat exchanger (9), cancel and heat exchanger (9) the second steam channel of connection, cancels the second condensate liquid pipeline connected with heat exchanger (9), forms the dynamic co-feeding system of heat.
48. the dynamic co-feeding system of heat, is described in claim 3-4,7-12,19-20,24-27,30-31,34-38,41-44 Any hot is moved in co-feeding system, cancels heat exchanger, cancels the heated medium pipeline that connect with heat exchanger (9), cancellation and 3rd steam channel of heat exchanger (9) connection, cancels the 3rd condensate liquid pipeline connected with heat exchanger (9), forms heat dynamic Co-feeding system.
49. the dynamic co-feeding system of heat, is in any hot described in claim 13-16,28-29,45-46 moves co-feeding system, to take Disappear heat exchanger, cancels the heated medium pipeline connected with heat exchanger (9), cancels the 4th connected with heat exchanger (9) Steam channel, cancels the 4th condensate liquid pipeline connected with heat exchanger (9), forms the dynamic co-feeding system of heat.
CN201510043114.9A 2014-01-27 2015-01-23 The dynamic co-feeding system of heat Active CN104654658B (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CN2014100467269 2014-01-27
CN201410046726 2014-01-27
CN201510043114.9A CN104654658B (en) 2014-01-27 2015-01-23 The dynamic co-feeding system of heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510043114.9A CN104654658B (en) 2014-01-27 2015-01-23 The dynamic co-feeding system of heat

Publications (2)

Publication Number Publication Date
CN104654658A CN104654658A (en) 2015-05-27
CN104654658B true CN104654658B (en) 2017-07-21

Family

ID=53246080

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510043114.9A Active CN104654658B (en) 2014-01-27 2015-01-23 The dynamic co-feeding system of heat

Country Status (1)

Country Link
CN (1) CN104654658B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106403350B (en) * 2016-05-30 2020-04-21 李华玉 Combined heat and power system
CN106352591B (en) * 2016-05-30 2020-01-31 李华玉 Combined heat and power system
CN106440469B (en) * 2016-05-30 2020-01-31 李华玉 Combined heat and power system
CN106440466B (en) * 2016-05-30 2020-04-21 李华玉 Combined heat and power system
CN106322832B (en) * 2016-05-30 2020-01-31 李华玉 Combined heat and power system
CN106482380B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system
CN106440470B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system
CN106403351B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system
CN106524561B (en) * 2016-06-15 2020-03-17 李华玉 Combined heat and power system

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11304274A (en) * 1998-04-20 1999-11-05 Kawasaki Thermal Eng Co Ltd Waste heat utilized absorption type water cooling/ heating machine refrigerating machine
JP2000065436A (en) * 1998-08-18 2000-03-03 Kawasaki Thermal Engineering Co Ltd Waste heat utilizing absorption type water heater/cooler refrigerating machine with load variation controlling function
JP2004232921A (en) * 2003-01-29 2004-08-19 Kawasaki Thermal Engineering Co Ltd Triple effect type absorption chiller with waste heat regenerator
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
CN101968286A (en) * 2010-10-10 2011-02-09 李华玉 Double absorption-double generation system and multi-terminal heat supply third kind absorption heat pumps
CN202381129U (en) * 2011-11-01 2012-08-15 北京科技大学 Power supplying system
CN103090581A (en) * 2013-01-16 2013-05-08 李华玉 First kind absorption heat pump which happens step by step

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11304274A (en) * 1998-04-20 1999-11-05 Kawasaki Thermal Eng Co Ltd Waste heat utilized absorption type water cooling/ heating machine refrigerating machine
JP2000065436A (en) * 1998-08-18 2000-03-03 Kawasaki Thermal Engineering Co Ltd Waste heat utilizing absorption type water heater/cooler refrigerating machine with load variation controlling function
JP2004232921A (en) * 2003-01-29 2004-08-19 Kawasaki Thermal Engineering Co Ltd Triple effect type absorption chiller with waste heat regenerator
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
CN101968286A (en) * 2010-10-10 2011-02-09 李华玉 Double absorption-double generation system and multi-terminal heat supply third kind absorption heat pumps
CN202381129U (en) * 2011-11-01 2012-08-15 北京科技大学 Power supplying system
CN103090581A (en) * 2013-01-16 2013-05-08 李华玉 First kind absorption heat pump which happens step by step

Also Published As

Publication number Publication date
CN104654658A (en) 2015-05-27

Similar Documents

Publication Publication Date Title
CN104654658B (en) The dynamic co-feeding system of heat
CN104654652B (en) The dynamic co-feeding system of heat
CN104748439B (en) The dynamic co-feeding system of heat
CN104654653B (en) The dynamic co-feeding system of heat
CN104929706B (en) Combined cycle energy supplying system
CN104963732B (en) Combined cycle energy supplying system
CN103851823B (en) Compound generation first-class absorption type heat pump
CN104864623A (en) Thermodynamic combined supply system
CN104833128B (en) 4th class absorption heat pump
CN104165477B (en) Combined heating and power system, combined cooling and power system and dual-purpose combined heat and power and cooling and power system
WO2012019329A1 (en) Absorption-resorption-generation system and first-type absorption heat pump
CN105019954B (en) Combined cycle energy supplying system
CN104848582B (en) Two stage type double effect type lithium bromide absorption refrigeration/heating machine unit
CN104807235B (en) 5th class absorption heat pump
CN104180557B (en) Cogeneration, combined cooling and power and the dual-purpose co-feeding system of thermoelectric cold electricity
CN104963733B (en) Combined cycle energy supplying system
CN206247691U (en) Superposition type solution series double-effect lithium bromide absorption type refrigerating heat pump unit
CN104807241B (en) 4th class absorption heat pump and the 5th class absorption heat pump
CN105041396B (en) Combined cycle energy supplying system
CN104807238B (en) 4th class absorption heat pump and the 5th class absorption heat pump
CN206247689U (en) Two sections of superposition type double-effect lithium bromide absorption type refrigerating heat pump units
CN106152599B (en) 4th class thermal drivers compressing-absorbing type heat pump
CN104807236B (en) 5th class absorption heat pump
CN106352590A (en) Combined heating and power system
CN206247690U (en) Two sections of independent superposition type double-effect lithium bromide absorption type refrigerating heat pump units

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant