CN104654658B - The dynamic co-feeding system of heat - Google Patents
The dynamic co-feeding system of heat Download PDFInfo
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- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
Abstract
The 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
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.
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CN106322832B (en) * | 2016-05-30 | 2020-01-31 | 李华玉 | Combined heat and power system |
CN106352591B (en) * | 2016-05-30 | 2020-01-31 | 李华玉 | Combined heat and power system |
CN106403350B (en) * | 2016-05-30 | 2020-04-21 | 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 |
CN106524561B (en) * | 2016-06-15 | 2020-03-17 | 李华玉 | Combined heat and power system |
CN106440470B (en) * | 2016-06-15 | 2020-03-17 | 李华玉 | Combined heat and power system |
CN106403351B (en) * | 2016-06-15 | 2020-03-17 | 李华玉 | Combined heat and power system |
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