CN106440474A - Combined heating and power system - Google Patents

Combined heating and power system Download PDF

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Publication number
CN106440474A
CN106440474A CN201610822196.1A CN201610822196A CN106440474A CN 106440474 A CN106440474 A CN 106440474A CN 201610822196 A CN201610822196 A CN 201610822196A CN 106440474 A CN106440474 A CN 106440474A
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Prior art keywords
generator
solution
absorber
heat exchanger
connect
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CN201610822196.1A
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CN106440474B (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • F25B15/06—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being water vapour evaporated from a salt solution, e.g. lithium bromide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B27/00—Machines, plants or systems, using particular sources of energy
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00—Fluid-circulation arrangements
    • F25B41/40—Fluid line arrangements
    • 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
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00—Climate change mitigation technologies for sector-wide applications
    • Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
    • Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

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

Abstract

The invention provides a combined heating and power system and belongs to the technical field of CCHP (combined cooling, heating and power) and absorption heat pumps. An absorption solution circulation process is formed by means of an absorber, a second absorber, a generator, a second generator, a condenser, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger, wherein a power machine communicates with the outside through a new steam channel and an exhaust steam channel, provides low-temperature heat load for the second generator through the exhaust steam channel and provides steam for the absorber through a first steam channel, the generator communicates with the outside through a high-temperature heat medium channel, the absorber and the condenser communicate with the outside through heated medium channels, the second absorber communicates with the outside through a cooling medium channel, the second generator communicates with the outside through a condensate channel I, the condenser communicates with the outside through a condensate channel II, and the combined heating and power system is formed.

Description

The dynamic co-feeding system of heat
Technical field：
The invention belongs to heat-electricity-cold combined supply and absorption type heat pump technical field.
Background technology：
In Steam Power Equipment, though the temperature difference is little between engine steam discharge and environment, heat is huge, winter season more so, The temperature difference between the low pressure exhaust steam of Steam Power Equipment discharge and environment is often difficult by；Steam power dress with coal as fuel Put, between combustion gas and power cycle steam, there is the heat transfer temperature difference being difficult to effectively utilizes, lead to the comprehensive energy of the dynamic co-feeding system of heat Source utilization rate is not high, and to clean energy resource in the dynamic co-feeding system of heat using bringing a definite limitation.
The present invention is premised on heat energy efficient utilization, warm between engine steam discharge or low-pressure steam and environment to make full use of Difference is core, takes into account lifting power machine job security and heat energy is converted into the efficiency of mechanical energy, and considers to adapt to the dynamic alliance of heat The utilization of clean energy resource in system, proposes as low-temperature heat source and to combine absorption heat pump with engine end steam discharge or low-pressure pumping steam The series of heat of technology moves co-feeding system.
Content of the invention：
Present invention is primarily intended to will provide heat dynamic co-feeding system, concrete content of the invention subitem is described below：
1. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine or also exhaust passage and ft connection, engine also has exhaust passage to connect it with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has exhaust passage to connect with absorber, and absorber is also Have weak solution pipeline to connect with the second absorber through solution heat exchanger, the second absorber also have weak solution pipeline through solution pump and Second solution heat exchanger is connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and the second generation Device connects, and the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, generator Steam channel is also had to connect with condenser, the second generator also has steam channel to connect with the second absorber, and condenser is also cold Lime set pipeline and ft connection, absorber and condenser also have heated medium passage and ft connection, the second absorber respectively Also have coolant guiding channel and ft connection, generator also has high temperature thermal medium passage and ft connection, form the dynamic alliance system of heat System.
2. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine also has exhaust passage and ft connection, and engine also has the first steam channel to connect with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has the first steam channel to connect with absorber, inhales Receiving device also has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through molten Liquid pump and the second solution heat exchanger are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and Two generator connections, the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, Generator also has steam channel to connect with condenser, and the second generator also has steam channel to connect with the second absorber, condenser Also have condensed fluid pipeline and ft connection, absorber and condenser also have heated medium passage and ft connection respectively, second Absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, forms heat dynamic Co-feeding system.
3. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine or also exhaust passage and ft connection, engine also has exhaust passage to connect it with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has the first steam channel to connect with absorber, absorbs Device also has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through solution Pump and the second solution heat exchanger are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and second Generator connects, and the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, sends out Raw device also has steam channel to connect with condenser, and the second generator also has steam channel to connect with the second absorber, and condenser is also Condensed fluid pipeline and ft connection, absorber and condenser is had also to have heated medium passage and ft connection, the second suction respectively Receive device and also have coolant guiding channel and ft connection, generator also has high temperature thermal medium passage and ft connection, form the dynamic connection of heat For system.
4. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine also has exhaust passage and ft connection, and engine also has the first steam channel to connect with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has the second steam channel to connect with absorber, inhales Receiving device also has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through molten Liquid pump and the second solution heat exchanger are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and Two generator connections, the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, Generator also has steam channel to connect with condenser, and the second generator also has steam channel to connect with the second absorber, condenser Also have condensed fluid pipeline and ft connection, absorber and condenser also have heated medium passage and ft connection respectively, second Absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, forms heat dynamic Co-feeding system.
5. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine or also exhaust passage and ft connection, engine also has exhaust passage to connect it with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has exhaust passage to connect with absorber, and absorber is also Have weak solution pipeline to connect with the second absorber through solution heat exchanger, the second absorber also have weak solution pipeline through solution pump and Second solution heat exchanger is connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and the second generation Device connects, and the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, generator Steam channel is also had to connect with condenser, the second generator also has steam channel to connect with the second absorber, and condenser is also cold Through the second generator and ft connection, absorber and condenser also have heated medium passage and outside to connect to lime set pipeline respectively Logical, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, shape Become the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine also has exhaust passage and ft connection, and engine also has the first steam channel to connect with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has the first steam channel to connect with absorber, inhales Receiving device also has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through molten Liquid pump and the second solution heat exchanger are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and Two generator connections, the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, Generator also has steam channel to connect with condenser, and the second generator also has steam channel to connect with the second absorber, condenser Also has condensed fluid pipeline through the second generator and ft connection, absorber and condenser also have heated medium passage respectively with outward Portion connects, and the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and outside to connect Logical, form the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine or also exhaust passage and ft connection, engine also has exhaust passage to connect it with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has the first steam channel to connect with absorber, absorbs Device also has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through solution Pump and the second solution heat exchanger are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and second Generator connects, and the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, sends out Raw device also has steam channel to connect with condenser, and the second generator also has steam channel to connect with the second absorber, and condenser is also There is condensed fluid pipeline through the second generator and ft connection, absorber and condenser also have heated medium passage and outside respectively Connection, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, Form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution Pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine have live steam passage with Ft connection, engine also has exhaust passage and ft connection, and engine also has the first steam channel to connect with the second generator Second generator has condensed fluid passage and ft connection more afterwards, and engine also has the second steam channel to connect with absorber, inhales Receiving device also has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through molten Liquid pump and the second solution heat exchanger are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and Two generator connections, the second generator also has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution pump, Generator also has steam channel to connect with condenser, and the second generator also has steam channel to connect with the second absorber, condenser Also has condensed fluid pipeline through the second generator and ft connection, absorber and condenser also have heated medium passage respectively with outward Portion connects, and the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and outside to connect Logical, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, is that any hot described in 1-8 item moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber is had weak solution pipeline through solution pump and second Solution heat exchanger is connected with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump and the second solution heat exchange Device is connected with the 3rd absorber, and the 3rd absorber has weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and to send out again Raw device connection, generator is had concentrated solution pipeline to connect with the second generator through the second solution heat exchanger and is adjusted to generator and has Concentrated solution pipeline is connected with the 3rd generator through the 3rd solution heat exchanger, and the 3rd generator has concentrated solution pipeline molten through second again Liquid heat exchanger is connected with the second generator, and the 3rd generator also has steam channel to connect with the 3rd absorber, the 3rd generator Also have high temperature thermal medium passage and ft connection, the 3rd absorber also has heated medium passage and ft connection, form heat dynamic Co-feeding system.
10. the dynamic co-feeding system of heat, is that any hot described in 1-8 item moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, by generator have steam channel connect with condenser be adjusted to send out Raw device has steam channel to connect with the 3rd absorber, and the 3rd absorber also has weak solution pipeline through the 3rd solution pump and the 3rd solution Heat exchanger is connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the 3rd solution heat exchanger and the 3rd absorption Device connects, and the 3rd generator also has steam channel to connect with condenser, and the 3rd generator also has high temperature thermal medium passage and outside Connection, the 3rd absorber also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 11. heat, are that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and choke valve, the second absorber sets up weak solution pipeline through the 3rd solution pump and the 3rd Solution heat exchanger is connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the 3rd solution heat exchanger and second Generator connect, by generator have steam channel connect with condenser be adjusted to generator have steam channel and the 3rd generator company After logical, the 3rd generator has condensed fluid pipeline warp knuckle stream valve to connect with condenser again, the 3rd generator also have steam channel with cold Condenser connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 12. heat, are that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers and choke valve, the second absorber is had weak solution pipeline through solution pump and the second solution heat exchanger and to send out Raw device connection is adjusted to the second absorber has weak solution pipeline through solution pump, the second solution heat exchanger and the 3rd solution heat exchange Device is connected with generator, by generator have concentrated solution pipeline connect with the second generator through the second solution heat exchanger be adjusted to send out Raw device has concentrated solution pipeline to connect with the 3rd generator through the 3rd solution heat exchanger, and the 3rd generator has concentrated solution pipeline warp again Second solution heat exchanger is connected with the second generator, generator is had steam channel to connect with condenser and is adjusted to generator and has After steam channel is connected with the 3rd generator, the 3rd generator has condensed fluid pipeline warp knuckle stream valve to connect with condenser again, and the 3rd Generator also has steam channel to connect with condenser, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 13. heat, are that any hot described in 1-4 item moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and choke valve, the second absorber is had weak solution pipeline through solution pump and the second solution Heat exchanger connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump and the second solution heat exchanger with 3rd generator connection, the 3rd generator has concentrated solution pipeline again through the 3rd solution pump and the 3rd solution heat exchanger and generator Connection, by generator have concentrated solution pipeline connect with the second generator through the second solution heat exchanger be adjusted to generator have dense molten Liquid pipeline is connected with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger, and generator is had steam channel Connect with condenser and be adjusted to the 3rd generator after generator has steam channel to connect with the 3rd generator and have condensate line again Road is connected with condenser through choke valve, and the 3rd generator also has steam channel to connect with condenser, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 14. heat, are that any hot described in 5-8 item moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and heater, the second absorber sets up weak solution pipeline through the 3rd solution pump and the 3rd Solution heat exchanger is connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the 3rd solution heat exchanger and second Generator connect, by generator have steam channel connect with condenser be adjusted to generator have steam channel and the 3rd generator company After logical, the 3rd generator has condensed fluid pipeline again through heater and the second generator and ft connection, and the 3rd generator also has steaming Vapour passage is connected with condenser, and heater also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 15. heat, are that any hot described in 5-8 item moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers and heater, the second absorber is had weak solution pipeline through solution pump and the second solution heat exchanger and to send out Raw device connection is adjusted to the second absorber has weak solution pipeline through solution pump, the second solution heat exchanger and the 3rd solution heat exchange Device is connected with generator, by generator have concentrated solution pipeline connect with the second generator through the second solution heat exchanger be adjusted to send out Raw device has concentrated solution pipeline to connect with the 3rd generator through the 3rd solution heat exchanger, and the 3rd generator has concentrated solution pipeline warp again Second solution heat exchanger is connected with the second generator, generator is had steam channel to connect with condenser and is adjusted to generator and has After steam channel is connected with the 3rd generator, the 3rd generator has condensed fluid pipeline through heater and the second generator with outward again Portion connects, and the 3rd generator also has steam channel to connect with condenser, and heater also has heated medium passage and ft connection, Form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 16. heat, are that any hot described in 5-8 item moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and heater, the second absorber is had weak solution pipeline through solution pump and the second solution Heat exchanger connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump and the second solution heat exchanger with 3rd generator connection, the 3rd generator has concentrated solution pipeline again through the 3rd solution pump and the 3rd solution heat exchanger and generator Connection, by generator have concentrated solution pipeline connect with the second generator through the second solution heat exchanger be adjusted to generator have dense molten Liquid pipeline is connected with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger, and generator is had steam channel Connect with condenser and be adjusted to the 3rd generator after generator has steam channel to connect with the 3rd generator and have condensate line again Road also has steam channel to connect with condenser through heater and the second generator and ft connection, the 3rd generator, and heater is also There are heated medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is that any hot described in 11-16 item moves in co-feeding system, the 3rd generator is set up High temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 18. heat, are that any hot described at the 1st, 3 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and Two absorber connections are adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd suction Receiving device has weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had dense Solution line is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline warp Solution heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat Exchanger is connected with absorber, and after engine is had exhaust passage to connect with the second generator, the second generator has condensed fluid again Passage and ft connection are adjusted to engine has exhaust passage to be sequentially communicated the 3rd after the second generator and the 3rd generator Raw device has condensed fluid passage and ft connection again, and the 3rd generator also has steam channel to connect with the 3rd absorber, the 3rd absorption Device also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or by engine there are exhaust passage and second After generator connection, the second generator has condensed fluid passage and ft connection to be adjusted to engine again has exhaust passage to connect successively After logical 3rd generator and the second generator, the second generator has condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 19. heat, are that any hot described at the 2nd, 4 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and Two absorber connections are adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd suction Receiving device has weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had dense Solution line is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline warp Solution heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat Exchanger is connected with absorber, after engine is had the first steam channel to connect with the second generator the second generator have again cold Lime set passage and ft connection be adjusted to engine have the first steam channel be sequentially communicated the second generator and the 3rd generator it 3rd generator has condensed fluid passage and ft connection more afterwards, and the 3rd generator also has steam channel to connect with the 3rd absorber, 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or by engine there is the first steaming After vapour passage is connected with the second generator, the second generator has condensed fluid passage and ft connection to be adjusted to engine to have the again After one steam channel is sequentially communicated the 3rd generator and the second generator, the second generator has condensed fluid passage and outside to connect again Logical.
The dynamic co-feeding systems of 20. heat, are that any hot described at the 4th moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and second Absorber connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd absorption Device has weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had dense molten Liquid pipeline is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline through molten Liquid heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline to hand over through the second solution pump and the 3rd solution heat again Parallel operation is connected with absorber, and engine is had exhaust passage and ft connection to be adjusted to engine exhaust passage and the 3rd generation After device connection, the 3rd generator has condensed fluid passage and ft connection again, and the 3rd generator also has steam channel and the 3rd absorption Device connects, and the 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or engine increase If the 3rd generator has condensed fluid passage and ft connection again after exhaust passage is connected with the 3rd generator.
The dynamic co-feeding systems of 21. heat, are that any hot described at the 5th, 7 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and Two absorber connections are adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd suction Receiving device has weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had dense Solution line is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline warp Solution heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat Exchanger is connected with absorber, and the second generator is had condensed fluid pipeline and ft connection to be adjusted to the second generator condensed fluid , through the 3rd generator and ft connection, after engine is had exhaust passage to connect with the second generator, the second generator is again for pipeline Have condensed fluid passage and ft connection be adjusted to engine have exhaust passage be sequentially communicated the second generator and the 3rd generator it 3rd generator has condensed fluid passage and ft connection more afterwards, and the 3rd generator also has steam channel to connect with the 3rd absorber, 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or by engine there is the first steaming After vapour passage is connected with the second generator, the second generator has condensed fluid passage and ft connection to be adjusted to engine to have the again After one steam channel is sequentially communicated the 3rd generator and the second generator, the second generator has condensed fluid passage and outside to connect again Logical.
The dynamic co-feeding system of 22. heat, is that the heat described at the 6th, 8 is moved in co-feeding system, increases the 3rd generator, the 3rd suction Receive device, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and the second suction Receipts device connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd absorber There is weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had concentrated solution Pipeline is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline through solution Heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat exchange Device is connected with absorber, and the second generator is had condensed fluid pipeline and ft connection to be adjusted to the second generator condensed fluid pipeline Through the 3rd generator and ft connection, after engine is had the first steam channel to connect with the second generator, the second generator is again Having condensed fluid passage and ft connection to be adjusted to engine has the first steam channel to be sequentially communicated the second generator and the 3rd generation After device, the 3rd generator has condensed fluid passage and ft connection again, and the 3rd generator also has steam channel and the 3rd absorber even Logical, the 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or by engine have After one steam channel is connected with the second generator, the second generator has condensed fluid passage and ft connection to be adjusted to engine again After having the first steam channel to be sequentially communicated the 3rd generator and the second generator, the second generator has condensed fluid passage again with outward Portion connects.
The dynamic co-feeding system of 23. heat, is that the heat described at the 8th is moved in co-feeding system, increases the 3rd generator, the 3rd absorption Device, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and the second absorption Device connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, and the 3rd absorber is again There is weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump, the second generator is had concentrated solution pipe Road the second solution pump connect with absorber with solution heat exchanger be adjusted to the second generator have concentrated solution pipeline through solution heat Exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat exchanger Connect with absorber, the second generator is had condensed fluid pipeline and ft connection to be adjusted to the second generator condensed fluid pipeline warp 3rd generator and ft connection, engine is had exhaust passage and ft connection to be adjusted to engine exhaust passage and the 3rd After generator connection, the 3rd generator has condensed fluid passage and ft connection again, and the 3rd generator also has steam channel and the 3rd Absorber connects, and the 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or power The 3rd generator after exhaust passage is connected set up with the 3rd generator by machine condensed fluid passage and ft connection again.
The dynamic co-feeding system of 24. heat, is to move in co-feeding system in the described any hot of 1-23 item, cancels generator and connected with outside Logical high temperature thermal medium passage, generator after high-temperature steam passage is connected set up with generator by engine high temperature condensed fluid again Passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 25. heat, is that any hot described in 9-10 item moves in co-feeding system, cancels generator and the 3rd The generator high temperature thermal medium passage with ft connection respectively, engine is set up high-temperature steam passage and is sequentially communicated generator and After three generators, the 3rd generator has high temperature condensed fluid passage and ft connection again, forms the dynamic co-feeding system of heat.
Brief description：
Fig. 1 is according to heat provided by the present invention dynamic co-feeding system the 1st kind of structure and schematic flow sheet.
Fig. 2 is according to heat provided by the present invention dynamic co-feeding system the 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to heat provided by the present invention dynamic co-feeding system the 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to heat provided by the present invention dynamic co-feeding system the 4th kind of structure and schematic flow sheet.
Fig. 5 is according to heat provided by the present invention dynamic co-feeding system the 5th kind of structure and schematic flow sheet.
Fig. 6 is according to heat provided by the present invention dynamic co-feeding system the 6th kind of structure and schematic flow sheet.
Fig. 7 is according to heat provided by the present invention dynamic co-feeding system the 7th kind of structure and schematic flow sheet.
Fig. 8 is according to heat provided by the present invention dynamic co-feeding system the 8th kind of structure and schematic flow sheet.
Fig. 9 is according to heat provided by the present invention dynamic co-feeding system the 9th kind of structure and schematic flow sheet.
Figure 10 is according to heat provided by the present invention dynamic co-feeding system the 10th kind of structure and schematic flow sheet.
Figure 11 is according to heat provided by the present invention dynamic co-feeding system the 11st kind of structure and schematic flow sheet.
Figure 12 is according to heat provided by the present invention dynamic co-feeding system the 12nd kind of structure and schematic flow sheet.
Figure 13 is according to heat provided by the present invention dynamic co-feeding system the 13rd kind of structure and schematic flow sheet.
Figure 14 is according to heat provided by the present invention dynamic co-feeding system the 14th kind of structure and schematic flow sheet.
Figure 15 is according to heat provided by the present invention dynamic co-feeding system the 15th kind of structure and schematic flow sheet.
Figure 16 is according to heat provided by the present invention dynamic co-feeding system the 16th kind of structure and schematic flow sheet.
Figure 17 is according to heat provided by the present invention dynamic co-feeding system the 17th kind of structure and schematic flow sheet.
Figure 18 is according to heat provided by the present invention dynamic co-feeding system the 18th kind of structure and schematic flow sheet.
Figure 19 is according to heat provided by the present invention dynamic co-feeding system the 19th kind of structure and schematic flow sheet.
In figure, 1- absorber, 2- second absorber, 3- generator, 4- second generator, 5- condenser, 6- solution pump, 7- Second solution pump, 8- solution heat exchanger, 9- second solution heat exchanger, 10- engine, 11- the 3rd generator, 12- the 3rd Absorber, 13- the 3rd solution pump, 14- the 3rd solution heat exchanger, 15- choke valve, 16- heater.
Specific embodiment：
First it is noted that in the statement of structure and flow process, inessential in the case of do not repeat；To apparent Flow process do not state.To describe the present invention with example in detail below in conjunction with the accompanying drawings.
Heat shown in Fig. 1 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, Second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine 10 has live steam passage with outward Portion connects, and after engine 10 also has exhaust passage to connect with the second generator 4, the second generator 4 has condensed fluid passage again with outward Portion connects, and engine 10 also has exhaust passage to connect with absorber 1, and absorber 1 also has weak solution pipeline through solution heat exchanger 8 Connect with the second absorber 2, the second absorber 2 also has weak solution pipeline through solution pump 6 and the second solution heat exchanger 9 and generation Device 3 connects, and generator 3 also has concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 9, the second generator 4 Also have concentrated solution pipeline connect with absorber 1 with solution heat exchanger 8 through the second solution pump 7, generator 3 also have steam channel and Condenser 5 connects, and the second generator 4 also has steam channel to connect with the second absorber 2, condenser 5 also have condensed fluid pipeline and Ft connection, absorber 1 and condenser 5 also have heated medium passage and ft connection respectively, and the second absorber 2 also has cooling Medium channel and ft connection, generator 3 also has high temperature thermal medium passage and ft connection.
(2) in flow process, live steam enters engine 10 blood pressure lowering work done, and the steam discharge of engine 10 is divided into the two-way first via and enters Enter absorber 1 and absorbed by solution, the second road is externally discharged after flowing through the second generator 4 exothermic condensation；Absorber 1 dilute molten Liquid enters the second absorber 2, absorbs steam through solution heat exchanger 8 and heat release is in cooling medium, the weak solution of the second absorber 2 Enter generator 3 through solution pump 6 and the second solution heat exchanger 9, high temperature thermal medium flows through generator 3, it is interior to heat entrance Solution release steam simultaneously provides to condenser 5, and the concentrated solution of generator 3 enters the second generator through the second solution heat exchanger 9 4th, heat absorption discharges steam and provides to the second absorber 2, and the concentrated solution of the second generator 4 is handed over through the second solution pump 7 and solution heat Parallel operation 8 enters absorber 1, absorbs steam and heat release is in heated medium, and the steam heat release of condenser 5 is in heated medium Cheng Leng Lime set is simultaneously externally discharged, and forms the dynamic co-feeding system of heat.
Heat shown in Fig. 2 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, Second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine 10 has live steam passage with outward Portion connects, and engine 10 also has exhaust passage and ft connection, and engine 10 also has the first steam channel and the second generator 4 even After logical, the second generator 4 has condensed fluid passage and ft connection again, and engine 10 also has the first steam channel with absorber 1 even Logical, absorber 1 also has weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 8, and the second absorber 2 also has dilute molten Liquid pipeline is connected with generator 3 with the second solution heat exchanger 9 through solution pump 6, and generator 3 also has concentrated solution pipeline molten through second Liquid heat exchanger 9 is connected with the second generator 4, and the second generator 4 also has concentrated solution pipeline to hand over through the second solution pump 7 and solution heat Parallel operation 8 is connected with absorber 1, and generator 3 also has steam channel to connect with condenser 5, the second generator 4 also have steam channel and Second absorber 2 connects, and condenser 5 also has condensed fluid pipeline and ft connection, and absorber 1 and condenser 5 also have respectively and added Hot media channel and ft connection, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high warm Medium channel and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing Live steam is divided into three tunnels after entering engine 10 blood pressure lowering work done, and the first via is directly entered absorber 1 quilt by the first steam channel Solution absorbs, and secondary route first steam channel is externally discharged after being supplied to the second generator 4 exothermic condensation, and the 3rd road completes Externally discharge after blood pressure lowering work done, 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 mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, Second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine 10 has live steam passage with outward Portion connects, and engine 10 also has exhaust passage and ft connection, and engine 10 also has exhaust passage to connect it with the second generator 4 Second generator 4 has condensed fluid passage and ft connection more afterwards, and engine 10 also has the first steam channel to connect with absorber 1, Absorber 1 also has weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 8, and the second absorber 2 also has weak solution pipe Road is connected with generator 3 with the second solution heat exchanger 9 through solution pump 6, and generator 3 also has concentrated solution pipeline through the second solution heat Exchanger 9 is connected with the second generator 4, and the second generator 4 also has concentrated solution pipeline through the second solution pump 7 and solution heat exchanger 8 are connected with absorber 1, and generator 3 also has steam channel to connect with condenser 5, and the second generator 4 also has steam channel and second Absorber 2 connects, and condenser 5 also has condensed fluid pipeline and ft connection, absorber 1 and condenser 5 also to have heated Jie respectively Matter passage and ft connection, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high temperature thermal medium Passage and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing Live steam is divided into three tunnels after entering engine 10 blood pressure lowering work done, and the steam for relative outlet with elevated pressures passes through the first steaming Vapour passage is directly entered absorber 1 and is absorbed by solution, completes a part of steam discharge after blood pressure lowering work done and is supplied to the second generation Device 4 exothermic condensation is simultaneously externally discharged, and completes another part steam discharge after blood pressure lowering work done and externally discharges, and forms the dynamic alliance system of heat System.
Heat shown in Fig. 4 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, Second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine 10 has live steam passage with outward Portion connects, and engine 10 also has exhaust passage and ft connection, and engine 10 also has the first steam channel and the second generator 4 even After logical, the second generator 4 has condensed fluid passage and ft connection again, and engine 10 also has the second steam channel with absorber 1 even Logical, absorber 1 also has weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 8, and the second absorber 2 also has dilute molten Liquid pipeline is connected with generator 3 with the second solution heat exchanger 9 through solution pump 6, and generator 3 also has concentrated solution pipeline molten through second Liquid heat exchanger 9 is connected with the second generator 4, and the second generator 4 also has concentrated solution pipeline to hand over through the second solution pump 7 and solution heat Parallel operation 8 is connected with absorber 1, and generator 3 also has steam channel to connect with condenser 5, the second generator 4 also have steam channel and Second absorber 2 connects, and condenser 5 also has condensed fluid pipeline and ft connection, and absorber 1 and condenser 5 also have respectively and added Hot media channel and ft connection, the second absorber 2 also has coolant guiding channel and ft connection, and generator 3 also has high warm Medium channel and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing After live steam enters engine 10 blood pressure lowering work done, it is supplied to absorber 1 and through the first steam channel through the second steam channel respectively It is supplied to the second generator 4, remaining steam continues to complete work done and externally discharges；Second steam enters absorber 1 and by solution Absorb, the first steam is externally discharged after flowing through the second generator 4 exothermic condensation, form the dynamic co-feeding system of heat.
Heat shown in Fig. 5 moves what co-feeding system was realized in：
Heat shown in Fig. 1 is moved in co-feeding system, and condenser 5 is had condensed fluid pipeline and ft connection to be adjusted to condenser 5 have condensed fluid pipeline through the second generator 4 and ft connection；The condensed fluid of condenser 5 discharge flows through the second generator 4 and puts Heat, externally discharges afterwards, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 6 moves what co-feeding system was realized in：
Heat shown in Fig. 2 is moved in co-feeding system, and condenser 5 is had condensed fluid pipeline and ft connection to be adjusted to condenser 5 have condensed fluid pipeline through the second generator 4 and ft connection；The condensed fluid of condenser 5 discharge flows through the second generator 4 and puts Heat, externally discharges afterwards, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 7 moves what co-feeding system was realized in：
Heat shown in Fig. 3 is moved in co-feeding system, and condenser 5 is had condensed fluid pipeline and ft connection to be adjusted to condenser 5 have condensed fluid pipeline through the second generator 4 and ft connection；The condensed fluid of condenser 5 discharge flows through the second generator 4 and puts Heat, externally discharges afterwards, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 8 moves what co-feeding system was realized in：
Heat shown in Fig. 4 is moved in co-feeding system, and condenser 5 is had condensed fluid pipeline and ft connection to be adjusted to condenser 5 have condensed fluid pipeline through the second generator 4 and ft connection；The condensed fluid of condenser 5 discharge flows through the second generator 4 and puts Heat, externally discharges afterwards, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 9 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, the second absorber 2 is had weak solution pipeline through solution pump 6 and the second solution heat exchanger 9 Connect with generator 3 and be adjusted to the second absorber 2 and have weak solution pipeline through solution pump 6 and the second solution heat exchanger 9 and the 3rd Absorber 12 connects, and the 3rd absorber 12 has weak solution pipeline through the 3rd solution pump 13 and the 3rd solution heat exchanger 14 and to send out again Raw device 3 connects, and generator 3 is had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 9 and is adjusted to generation Device 3 has concentrated solution pipeline to connect with the 3rd generator 11 through the 3rd solution heat exchanger 14, and the 3rd generator 11 has concentrated solution again Pipeline is connected with the second generator 4 through the second solution heat exchanger 9, and the 3rd generator 11 also has steam channel and the 3rd absorber 12 connections, the 3rd generator 11 also has high temperature thermal medium passage and ft connection, and the 3rd absorber 12 also has heated medium to lead to Road and ft connection.
(2), in flow process, the weak solution of the second absorber 2 enters the 3rd absorption through solution pump 6 and the second solution heat exchanger 9 , in heated medium, the weak solution of the 3rd absorber 12 is through the 3rd solution pump 13 and the 3rd solution for device 12, absorption steam heat release Heat exchanger 14 enters generator 3, and the concentrated solution of generator 3 enters the 3rd generator 11 through the 3rd solution heat exchanger 14, high Warm flows through the 3rd generator 11, heating enters its interior solution release steam and provides to the 3rd absorber 12, the 3rd The concentrated solution of generator 11 enters the second generator 4 through the second solution heat exchanger 9, forms the dynamic co-feeding system of heat.
Heat shown in Figure 10 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 7 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, generator 3 are had steam channel to connect with condenser 5 and are adjusted to generator 3 and have steam to lead to Road is connected with the 3rd absorber 12, and the 3rd absorber 12 also has weak solution pipeline through the 3rd solution pump 13 and the 3rd solution heat exchange Device 14 is connected with the 3rd generator 11, and the 3rd generator 11 also has concentrated solution pipeline through the 3rd solution heat exchanger 14 and the 3rd suction Receive device 12 to connect, the 3rd generator 11 also has steam channel to connect with condenser 5, the 3rd generator 11 also has high temperature thermal medium to lead to Road and ft connection, the 3rd absorber 12 also has heated medium passage and ft connection.
(2) in flow process, the steam that generator 3 produces enters the 3rd absorber 12, and the weak solution of the 3rd absorber 12 is through the Three solution pumps 13 and the 3rd solution heat exchanger 14 enter the 3rd generator 11, and high temperature thermal medium flows through the 3rd generator 11, adds Heat enters its interior solution release steam and provides to condenser 5, and the concentrated solution of the 3rd generator 11 is through the 3rd solution heat exchange Device 14 enters the 3rd absorber 12, absorbs steam and heat release is in heated medium, forms the dynamic co-feeding system of heat.
Heat shown in Figure 11 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger and choke valve, the second absorber 2 sets up weak solution pipeline through the 3rd solution pump 13 and the 3rd solution heat exchanger 14 are connected with the 3rd generator 11, and the 3rd generator 11 also has concentrated solution pipeline through the 3rd solution heat exchanger 14 and the second generation Device 4 connects, and generator 3 is had steam channel to connect with condenser 5 and is adjusted to generator 3 and has steam channel and the 3rd generator 11 After connection, the 3rd generator 11 has condensed fluid pipeline warp knuckle stream valve 15 to connect with condenser 5 again, and the 3rd generator 11 also has steaming Vapour passage is connected with condenser 5.
(2), in flow process, the steam that generator 3 produces is supplied to the 3rd generator 11 and makees to drive thermal medium, the second absorber 2 Part weak solution enter the 3rd generator 11 through the 3rd solution pump 13 and the 3rd solution heat exchanger 14, steam flows through the 3rd Raw device 11, heating enter its interior solution release steam and provide to condenser 5, and the concentrated solution of the 3rd generator 11 is molten through the 3rd Liquid heat exchanger 14 enters the second generator 4；The steam heat release flowing through the 3rd generator 11 becomes condensed fluid, and condensed fluid flows through second Enter condenser 5 after choke valve 15 reducing pressure by regulating flow, form the dynamic co-feeding system of heat.
Heat shown in Figure 12 moves what co-feeding system was realized in：
(1), in structure, heat shown in Fig. 3 is moved in co-feeding system, increase the 3rd generator, the 3rd solution heat exchanger and Choke valve, the second absorber 2 is had weak solution pipeline to connect adjustment with the second solution heat exchanger 9 with generator 3 through solution pump 6 Weak solution pipeline is had through solution pump 6, the second solution heat exchanger 9 and the 3rd solution heat exchanger 14 and to send out for the second absorber 2 Raw device 3 connects, and generator 3 is had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 9 and is adjusted to generation Device 3 has concentrated solution pipeline to connect with the 3rd generator 11 through the 3rd solution heat exchanger 14, and the 3rd generator 11 has concentrated solution again Pipeline is connected with the second generator 4 through the second solution heat exchanger 9, and generator 3 is had steam channel to connect adjustment with condenser 5 After having steam channel to connect with the 3rd generator 11 for generator 3, the 3rd generator 11 has condensed fluid pipeline warp knuckle stream valve 15 again Connect with condenser 5, the 3rd generator 11 also has steam channel to connect with condenser 5, the 3rd generator 11 also has high warm to be situated between Matter passage and ft connection.
(2), in flow process, the steam that generator 3 produces and high temperature thermal medium are supplied to the 3rd generator 11 and make to drive heat to be situated between Matter, the weak solution of the second absorber 2 enters through solution pump 6, the second solution heat exchanger 9 and the 3rd solution heat exchanger 14 and occurs Device 3, the concentrated solution of generator 3 enters the 3rd generator 11 through the 3rd solution heat exchanger 14, and steam and high temperature thermal medium are respectively Flow through the 3rd generator 11, heating enters its interior solution release steam and provides to condenser 5, the 3rd generator 11 dense molten Liquid enters the second generator 4 through the second solution heat exchanger 9；The steam heat release flowing through the 3rd generator 11 becomes condensed fluid, condensation Liquor stream, through entering condenser 5 after second throttle 15 reducing pressure by regulating flow, forms the dynamic co-feeding system of heat.
Heat shown in Figure 13 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger and choke valve, the second absorber 2 is had weak solution pipeline through solution pump 6 and the second solution heat exchanger 9 and to send out Raw device 3 connection is adjusted to the second absorber 2 has weak solution pipeline through solution pump 6 and the second solution heat exchanger 9 and the 3rd generation Device 11 connects, and the 3rd generator 11 has concentrated solution pipeline again through the 3rd solution pump 13 and the 3rd solution heat exchanger 14 and generator 3 connections, generator 3 are had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 9 and are adjusted to generator 3 Concentrated solution pipeline is had to connect with the second generator 4 with the second solution heat exchanger 9 through the 3rd solution heat exchanger 14, by generator 3 have steam channel to connect with condenser 5 is adjusted to the 3rd generation after generator 3 has steam channel to connect with the 3rd generator 11 Device 11 has condensed fluid pipeline warp knuckle stream valve 15 to connect with condenser 5 again, and the 3rd generator 11 also has steam channel with condenser 5 even Logical.
(2), in flow process, the steam that generator 3 produces is supplied to the 3rd generator 11 and makees to drive thermal medium, the second absorber 2 Weak solution enter the 3rd generator 11 through solution pump 6 and the second solution heat exchanger 9, steam flow through the 3rd generator 11, plus Heat enters its interior solution release steam and provides to condenser 5, and the concentrated solution of the 3rd generator 11 is through the 3rd solution pump 13 He 3rd solution heat exchanger 14 enters generator 3, and the concentrated solution of generator 3 is through the 3rd solution heat exchanger 14 and the second solution heat Exchanger 9 enters the second generator 4；The steam heat release flowing through the 3rd generator 11 becomes condensed fluid, and condensed fluid flows through the second throttling Enter condenser 5 after valve 15 reducing pressure by regulating flow, form the dynamic co-feeding system of heat.
Heat shown in Figure 14 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 7 is moved in co-feeding system, increases the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger and heater, the second absorber 2 sets up weak solution pipeline through the 3rd solution pump 13 and the 3rd solution heat exchanger 14 are connected with the 3rd generator 11, and the 3rd generator 11 also has concentrated solution pipeline through the 3rd solution heat exchanger 14 and the second generation Device 4 connects, and generator 3 is had steam channel to connect with condenser 5 and is adjusted to generator 3 and has steam channel and the 3rd generator 11 After connection, the 3rd generator 11 has condensed fluid pipeline again through heater 16 and the second generator 4 and ft connection, the 3rd generation Device 11 also has steam channel to connect with condenser 5, and heater 16 also has heated medium passage and ft connection.
(2), in flow process, the steam that generator 3 produces is supplied to the 3rd generator 11 and makees to drive thermal medium, the second absorber 2 Part weak solution enter the 3rd generator 11 through the 3rd solution pump 13 and the 3rd solution heat exchanger 14, steam flows through the 3rd Raw device 11, heating enter its interior solution release steam and provide to condenser 5, and the concentrated solution of the 3rd generator 11 is molten through the 3rd Liquid heat exchanger 14 enters the second generator 4；The steam heat release flowing through the 3rd generator 11 becomes condensed fluid, and condensed fluid flows through heat supply Device 16 and the second generator 4 progressively externally discharge after heat release, form the dynamic co-feeding system of heat.
Heat shown in Figure 15 moves what co-feeding system was realized in：
(1), in structure, heat shown in Fig. 7 is moved in co-feeding system, increase the 3rd generator, the 3rd solution heat exchanger and Heater, the second absorber 2 is had weak solution pipeline to connect adjustment with the second solution heat exchanger 9 with generator 3 through solution pump 6 Weak solution pipeline is had through solution pump 6, the second solution heat exchanger 9 and the 3rd solution heat exchanger 14 and to send out for the second absorber 2 Raw device 3 connects, and generator 3 is had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 9 and is adjusted to generation Device 3 has concentrated solution pipeline to connect with the 3rd generator 11 through the 3rd solution heat exchanger 14, and the 3rd generator 11 has concentrated solution again Pipeline is connected with the second generator 4 through the second solution heat exchanger 9, and generator 3 is had steam channel to connect adjustment with condenser 5 After having steam channel to connect with the 3rd generator 11 for generator 3, the 3rd generator 11 has condensed fluid pipeline again through heater 16 With the second generator 4 and ft connection, also steam channel is connected the 3rd generator 11 with condenser 5, and heater 16 also has quilt Heating medium passage and ft connection, the 3rd generator 11 also has high temperature thermal medium passage and ft connection.
(2), in flow process, the steam that generator 3 produces and high temperature thermal medium are supplied to the 3rd generator 11 and make to drive heat to be situated between Matter, the weak solution of the second absorber 2 enters through solution pump 6, the second solution heat exchanger 9 and the 3rd solution heat exchanger 14 and occurs Device 3, the concentrated solution of generator 3 enters the 3rd generator 11 through the 3rd solution heat exchanger 14, and steam and high temperature thermal medium are respectively Flow through the 3rd generator 11, heating enters its interior solution release steam and provides to condenser 5, the 3rd generator 11 dense molten Liquid enters the second generator 4 through the second solution heat exchanger 9；The steam heat release flowing through the 3rd generator 11 becomes condensed fluid, condensation Liquor stream is externally discharged through after heater 16 and the second generator 4 progressively heat release, forms the dynamic co-feeding system of heat.
Heat shown in Figure 16 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 7 is moved in co-feeding system, increases the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger and heater, the second absorber 2 is had weak solution pipeline through solution pump 6 and the second solution heat exchanger 9 and to send out Raw device 3 connection is adjusted to the second absorber 2 has weak solution pipeline through solution pump 6 and the second solution heat exchanger 9 and the 3rd generation Device 11 connects, and the 3rd generator 11 has concentrated solution pipeline again through the 3rd solution pump 13 and the 3rd solution heat exchanger 14 and generator 3 connections, generator 3 are had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 9 and are adjusted to generator 3 Concentrated solution pipeline is had to connect with the second generator 4 with the second solution heat exchanger 9 through the 3rd solution heat exchanger 14, by generator 3 have steam channel to connect with condenser 5 is adjusted to the 3rd generation after generator 3 has steam channel to connect with the 3rd generator 11 Device 11 has condensed fluid pipeline again through heater 16 and the second generator 4 and ft connection, and the 3rd generator 11 also has steam channel Connect with condenser 5, heater 16 also has heated medium passage and ft connection.
(2), in flow process, the steam that generator 3 produces is supplied to the 3rd generator 11 and makees to drive thermal medium, the second absorber 2 Weak solution enter the 3rd generator 11 through solution pump 6 and the second solution heat exchanger 9, steam flow through the 3rd generator 11, plus Heat enters its interior solution release steam and provides to condenser 5, and the concentrated solution of the 3rd generator 11 is through the 3rd solution pump 13 He 3rd solution heat exchanger 14 enters generator 3, and the concentrated solution of generator 3 is through the 3rd solution heat exchanger 14 and the second solution heat Exchanger 9 enters the second generator 4；The steam heat release flowing through the 3rd generator 11 becomes condensed fluid, and condensed fluid flows through heater 16 Externally discharge with after the second generator 4 progressively heat release, form the dynamic co-feeding system of heat.
Heat shown in Figure 17 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, absorber 1 is had weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 8 Being adjusted to absorber 1 has weak solution pipeline to connect with the 3rd absorber 12 through the 3rd solution heat exchanger 14, the 3rd absorber 12 There is weak solution pipeline to connect with the second absorber 2 with solution heat exchanger 8 through the 3rd solution pump 13 again, the second generator 4 is had Concentrated solution pipeline is connected with absorber 1 through the second solution pump 7 and solution heat exchanger 8 and is adjusted to the second generator 4 and has concentrated solution Pipeline is connected with the 3rd generator 11 through solution heat exchanger 8, and the 3rd generator 11 has concentrated solution pipeline again through the second solution pump 7 Connect with absorber 1 with the 3rd solution heat exchanger 14, after engine 10 is had exhaust passage to connect with the second generator 4 Two generators 4 have condensed fluid passage and ft connection to be adjusted to engine 10 again has exhaust passage to be sequentially communicated the 3rd generator 11 There are condensed fluid passage and ft connection with the second generator 4 after the second generator 4 again, the 3rd generator 11 also has steam channel Connect with the 3rd absorber 12, the 3rd absorber 12 also has coolant guiding channel and ft connection.
(2), in flow process, live steam is divided into three tunnels after entering engine 10 blood pressure lowering work done, and the steam with elevated pressures passes through First steam channel is supplied to absorber 1 and is absorbed by solution, completes a part of steam discharge after blood pressure lowering work done and is supplied to the 3rd Generator 11 and the second generator 4 exothermic condensation are simultaneously externally discharged, and complete another part steam discharge after blood pressure lowering work done and externally arrange Put；The weak solution of absorber 1 enters the 3rd absorber 12, absorbs steam through the 3rd solution heat exchanger 14 and heat release is situated between in cooling Matter, the weak solution of the 3rd absorber 12 enters the second absorber 2 through the 3rd solution pump 13 and solution heat exchanger 8；Second generation The concentrated solution of device 4 enters the 3rd generator 11 through solution heat exchanger 8, heat absorption discharges steam and provides to the 3rd absorber 12, The concentrated solution of the 3rd generator 11 enters absorber 1 through the second solution pump 7 and the 3rd solution heat exchanger 14, forms the dynamic alliance of heat System.
Heat shown in Figure 18 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 7 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, absorber 1 is had weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 8 Being adjusted to absorber 1 has weak solution pipeline to connect with the 3rd absorber 12 through the 3rd solution heat exchanger 14, the 3rd absorber 12 There is weak solution pipeline to connect with the second absorber 2 with solution heat exchanger 8 through the 3rd solution pump 13 again, the second generator 4 is had Concentrated solution pipeline is connected with absorber 1 through the second solution pump 7 and solution heat exchanger 8 and is adjusted to the second generator 4 and has concentrated solution Pipeline is connected with the 3rd generator 11 through solution heat exchanger 8, and the 3rd generator 11 has concentrated solution pipeline again through the second solution pump 7 Connect with absorber 1 with the 3rd solution heat exchanger 14, the second generator 4 is had condensed fluid pipeline and ft connection to be adjusted to the Two generators 4 have condensed fluid pipeline through the 3rd generator 11 and ft connection, and engine 10 is had exhaust passage and the second generation After device 4 connection, the second generator 4 has condensed fluid passage and ft connection to be adjusted to engine 10 again has exhaust passage to connect successively After logical 3rd generator 11 and the second generator 4, the second generator 4 has condensed fluid passage and ft connection again, the 3rd generator 11 also have steam channel to connect with the 3rd absorber 12, and the 3rd absorber 12 also has coolant guiding channel and ft connection.
(2), in flow process, live steam is divided into three tunnels after entering engine 10 blood pressure lowering work done, and the steam with elevated pressures passes through First steam channel is supplied to absorber 1 and is absorbed by solution, completes a part of steam discharge after blood pressure lowering work done and is supplied to the 3rd Generator 11 and the second generator 4 exothermic condensation are simultaneously externally discharged, and complete another part steam discharge after blood pressure lowering work done and externally arrange Put；The condensed fluid of condenser 5 flows through the second generator 4 and the 3rd generator 11 progressively heat release, externally discharges afterwards；Absorber 1 Weak solution enter the 3rd absorber 12, absorb steam heat release in cooling medium through the 3rd solution heat exchanger 14, the 3rd suction The weak solution receiving device 12 enters the second absorber 2 through the 3rd solution pump 13 and solution heat exchanger 8；Second generator 4 dense molten Liquid enters the 3rd generator 11 through solution heat exchanger 8, heat absorption discharges steam and provides to the 3rd absorber 12, the 3rd generator 11 concentrated solution enters absorber 1 through the second solution pump 7 and the 3rd solution heat exchanger 14, forms the dynamic co-feeding system of heat.
Heat shown in Figure 19 moves what co-feeding system was realized in：
Heat shown in Fig. 8 moves the high temperature thermal medium passage cancelling generator 3 and ft connection in co-feeding system, power Generator 3 after high-temperature steam passage is connected set up with generator 3 by machine 10 high temperature condensed fluid passage and ft connection again；Power Machine 10 passes through high-temperature steam passage respectively to be provided to absorber 1 to generator 3 offer driving thermic load, by the second steam channel Steam and provide low temperature thermic load to the second generator 4 by the first steam channel, forms the dynamic co-feeding system of heat.
Effect that the technology of the present invention can be realized heat proposed by the invention moves co-feeding system, have the effect that and Advantage：
(1) high-grade steam elder generation work done, low-grade steam is used for heat supply, meets heat energy efficient utilization principle.
(2) provide low temperature thermic load from engine steam discharge or the first steam to generator, by steam discharge, the first steam or second Steam directly provides steam to absorber, and combines the second generator and the second absorber, realizes Steam Power Equipment end row The effectively utilizes of the temperature difference between vapour or low-pressure pumping steam and cold environment.
(3) release cleaning or high efficient energy sources and move the application restriction in co-feeding system in conventional thermal.
(4) with engine end steam for the dynamic alliance low-temperature heat source of heat, be conducive to improving the thermal efficiency and the equipment of engine The safety running.
(5) enrich the type of the dynamic co-feeding system of heat, extend the range of application of absorption heat pump, be conducive to preferably adopting Improve heat utilization rate with absorption heat pump technology.

Claims (25)

1. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, engine (10) or also exhaust passage and ft connection, and engine (10) also has exhaust passage and the second generator (4) after connecting, the second generator (4) has condensed fluid passage and ft connection again, and engine (10) also has exhaust passage and absorption Device (1) connects, and absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), the second suction Receiving device (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), generator (3) concentrated solution pipeline is also had to connect with the second generator (4) through the second solution heat exchanger (9), the second generator (4) is also dense Solution line is connected with absorber (1) with solution heat exchanger (8) through the second solution pump (7), and generator (3) also has steam channel Connect with condenser (5), the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) is also cold Lime set pipeline and ft connection, absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, and second Absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium passage and ft connection, shape Become the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, and engine (10) also has exhaust passage and ft connection, and engine (10) also has the first steam channel and the second generation After device (4) connection, the second generator (4) has condensed fluid passage and ft connection again, and engine (10) also has the first steam channel Connect with absorber (1), absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), Second absorber (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), sends out Raw device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (9), and the second generator (4) is also Concentrated solution pipeline is had to connect with absorber (1) with solution heat exchanger (8) through the second solution pump (7), generator (3) also has steam Passage is connected with condenser (5), and the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) is also Condensed fluid pipeline and ft connection, absorber (1) and condenser (5) is had also to have heated medium passage and ft connection respectively, Second absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium passage to connect with outside Logical, form the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, engine (10) or also exhaust passage and ft connection, and engine (10) also has exhaust passage and the second generator (4) connect after the second generator (4) have condensed fluid passage and ft connection again, engine (10) also have the first steam channel with Absorber (1) connects, and absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), the Two absorbers (2) also have weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), occur Device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (9), and the second generator (4) also has Concentrated solution pipeline is connected with absorber (1) with solution heat exchanger (8) through the second solution pump (7), and generator (3) also has steam to lead to Road is connected with condenser (5), and the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) also has Condensed fluid pipeline and ft connection, absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, the Two absorbers (2) also have coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium passage and ft connection, Form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, and engine (10) also has exhaust passage and ft connection, and engine (10) also has the first steam channel and the second generation After device (4) connection, the second generator (4) has condensed fluid passage and ft connection again, and engine (10) also has the second steam channel Connect with absorber (1), absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), Second absorber (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), sends out Raw device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (9), and the second generator (4) is also Concentrated solution pipeline is had to connect with absorber (1) with solution heat exchanger (8) through the second solution pump (7), generator (3) also has steam Passage is connected with condenser (5), and the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) is also Condensed fluid pipeline and ft connection, absorber (1) and condenser (5) is had also to have heated medium passage and ft connection respectively, Second absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium passage to connect with outside Logical, form the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, engine (10) or also exhaust passage and ft connection, and engine (10) also has exhaust passage and the second generator (4) after connecting, the second generator (4) has condensed fluid passage and ft connection again, and engine (10) also has exhaust passage and absorption Device (1) connects, and absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), the second suction Receiving device (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), generator (3) concentrated solution pipeline is also had to connect with the second generator (4) through the second solution heat exchanger (9), the second generator (4) is also dense Solution line is connected with absorber (1) with solution heat exchanger (8) through the second solution pump (7), and generator (3) also has steam channel Connect with condenser (5), the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) is also cold Through the second generator (4) and ft connection, absorber (1) and condenser (5) also have heated medium passage to lime set pipeline respectively With ft connection, the second absorber (2) also coolant guiding channel and ft connection, generator (3) also has high temperature thermal medium to lead to Road and ft connection, form the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, and engine (10) also has exhaust passage and ft connection, and engine (10) also has the first steam channel and the second generation After device (4) connection, the second generator (4) has condensed fluid passage and ft connection again, and engine (10) also has the first steam channel Connect with absorber (1), absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), Second absorber (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), sends out Raw device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (9), and the second generator (4) is also Concentrated solution pipeline is had to connect with absorber (1) with solution heat exchanger (8) through the second solution pump (7), generator (3) also has steam Passage is connected with condenser (5), and the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) is also There is condensed fluid pipeline through the second generator (4) and ft connection, absorber (1) and condenser (5) also have heated medium respectively Passage and ft connection, the second absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high warm to be situated between Matter passage and ft connection, form the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, engine (10) or also exhaust passage and ft connection, and engine (10) also has exhaust passage and the second generator (4) connect after the second generator (4) have condensed fluid passage and ft connection again, engine (10) also have the first steam channel with Absorber (1) connects, and absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), the Two absorbers (2) also have weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), occur Device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (9), and the second generator (4) also has Concentrated solution pipeline is connected with absorber (1) with solution heat exchanger (8) through the second solution pump (7), and generator (3) also has steam to lead to Road is connected with condenser (5), and the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) also has Through the second generator (4) and ft connection, absorber (1) and condenser (5) also have heated medium to lead to condensed fluid pipeline respectively Road and ft connection, the second absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high temperature thermal medium Passage and ft connection, form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, solution pump, the Two solution pumps, solution heat exchanger, the second solution heat exchanger and engine are formed；Engine (10) has live steam passage with outward Portion connects, and engine (10) also has exhaust passage and ft connection, and engine (10) also has the first steam channel and the second generation After device (4) connection, the second generator (4) has condensed fluid passage and ft connection again, and engine (10) also has the second steam channel Connect with absorber (1), absorber (1) also has weak solution pipeline to connect with the second absorber (2) through solution heat exchanger (8), Second absorber (2) also has weak solution pipeline to connect with generator (3) with the second solution heat exchanger (9) through solution pump (6), sends out Raw device (3) also has concentrated solution pipeline to connect with the second generator (4) through the second solution heat exchanger (9), and the second generator (4) is also Concentrated solution pipeline is had to connect with absorber (1) with solution heat exchanger (8) through the second solution pump (7), generator (3) also has steam Passage is connected with condenser (5), and the second generator (4) also has steam channel to connect with the second absorber (2), and condenser (5) is also There is condensed fluid pipeline through the second generator (4) and ft connection, absorber (1) and condenser (5) also have heated medium respectively Passage and ft connection, the second absorber (2) also has coolant guiding channel and ft connection, and generator (3) also has high warm to be situated between Matter passage and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, is that any hot described in claim 1-8 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber (2) is had weak solution pipeline through solution pump (6) Connect with generator (3) with the second solution heat exchanger (9) and be adjusted to the second absorber (2) and have weak solution pipeline through solution pump (6) with the second solution heat exchanger (9) is connected with the 3rd absorber (12), and the 3rd absorber (12) has weak solution pipeline again through Three solution pumps (13) are connected with generator (3) with the 3rd solution heat exchanger (14), and generator (3) is had concentrated solution pipeline through Two solution heat exchangers (9) connect with the second generator (4) be adjusted to generator (3) have concentrated solution pipeline through the 3rd solution heat hand over Parallel operation (14) is connected with the 3rd generator (11), and the 3rd generator (11) has concentrated solution pipeline again through the second solution heat exchanger (9) connect with the second generator (4), the 3rd generator (11) also has steam channel to connect with the 3rd absorber (12), the 3rd Raw device (11) also has high temperature thermal medium passage and ft connection, and the 3rd absorber (12) also has heated medium passage to connect with outside Logical, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is that any hot described in claim 1-8 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, generator (3) is had steam channel to connect tune with condenser (5) Whole have steam channel to connect with the 3rd absorber (12) for generator (3), and the 3rd absorber (12) also has weak solution pipeline through the Three solution pumps (13) are connected with the 3rd generator (11) with the 3rd solution heat exchanger (14), and the 3rd generator (11) also has dense molten Liquid pipeline is connected with the 3rd absorber (12) through the 3rd solution heat exchanger (14), the 3rd generator (11) also have steam channel with Condenser (5) connects, and the 3rd generator (11) also has high temperature thermal medium passage and ft connection, and the 3rd absorber (12) also has quilt Heating medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 11. heat, are that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and choke valve, the second absorber (2) sets up weak solution pipeline through the 3rd solution pump (13) Connect with the 3rd generator (11) with the 3rd solution heat exchanger (14), the 3rd generator (11) also has concentrated solution pipeline through the 3rd Solution heat exchanger (14) is connected with the second generator (4), and generator (3) is had steam channel to connect adjustment with condenser (5) After having steam channel to connect with the 3rd generator (11) for generator (3), the 3rd generator (11) has condensed fluid pipeline warp knuckle again Stream valve (15) is connected with condenser (5), and the 3rd generator (11) also has steam channel to connect with condenser (5), forms the dynamic connection of heat For system.
The dynamic co-feeding systems of 12. heat, are that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers and choke valve, the second absorber (2) is had weak solution pipeline through solution pump (6) and the second solution heat exchange Device (9) is connected with generator (3) and is adjusted to the second absorber (2) and has weak solution pipeline through solution pump (6), the second solution heat exchange Device (9) is connected with generator (3) with the 3rd solution heat exchanger (14), and generator (3) is had concentrated solution pipeline through the second solution Heat exchanger (9) is connected with the second generator (4) and is adjusted to generator (3) and has concentrated solution pipeline through the 3rd solution heat exchanger (14) connect with the 3rd generator (11), the 3rd generator (11) have again concentrated solution pipeline through the second solution heat exchanger (9) with Second generator (4) connects, and generator (3) is had steam channel to connect with condenser (5) and is adjusted to generator (3) and has steam logical After road is connected with the 3rd generator (11), the 3rd generator (11) has condensed fluid pipeline warp knuckle stream valve (15) and condenser (5) again Connection, the 3rd generator (11) also has steam channel to connect with condenser (5), forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 13. heat, are that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and choke valve, the second absorber (2) is had weak solution pipeline through solution pump (6) and Two solution heat exchangers (9) connect with generator (3) be adjusted to the second absorber (2) have weak solution pipeline through solution pump (6) and Second solution heat exchanger (9) is connected with the 3rd generator (11), and the 3rd generator (11) has concentrated solution pipeline molten through the 3rd again Liquid pump (13) is connected with generator (3) with the 3rd solution heat exchanger (14), and generator (3) is had concentrated solution pipeline molten through second Liquid heat exchanger (9) is connected with the second generator (4) and is adjusted to generator (3) and has concentrated solution pipeline through the 3rd solution heat exchanger (14) with the second solution heat exchanger (9) is connected with the second generator (4), and generator (3) is had steam channel and condenser (5) Connection is adjusted to the 3rd generator (11) after generator (3) has steam channel to connect with the 3rd generator (11) condensed fluid again Pipeline is connected with condenser (5) through choke valve (15), and the 3rd generator (11) also has steam channel to connect with condenser (5), shape Become the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 14. heat, are that any hot described in claim 5-8 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and heater, the second absorber (2) sets up weak solution pipeline through the 3rd solution pump (13) Connect with the 3rd generator (11) with the 3rd solution heat exchanger (14), the 3rd generator (11) also has concentrated solution pipeline through the 3rd Solution heat exchanger (14) is connected with the second generator (4), and generator (3) is had steam channel to connect adjustment with condenser (5) After having steam channel to connect with the 3rd generator (11) for generator (3), the 3rd generator (11) has condensed fluid pipeline again through supplying Hot device (16) and the second generator (4) and ft connection, the 3rd generator (11) also has steam channel to connect with condenser (5), Heater (16) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 15. heat, are that any hot described in claim 5-8 moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers and heater, the second absorber (2) is had weak solution pipeline through solution pump (6) and the second solution heat exchange Device (9) is connected with generator (3) and is adjusted to the second absorber (2) and has weak solution pipeline through solution pump (6), the second solution heat exchange Device (9) is connected with generator (3) with the 3rd solution heat exchanger (14), and generator (3) is had concentrated solution pipeline through the second solution Heat exchanger (9) is connected with the second generator (4) and is adjusted to generator (3) and has concentrated solution pipeline through the 3rd solution heat exchanger (14) connect with the 3rd generator (11), the 3rd generator (11) have again concentrated solution pipeline through the second solution heat exchanger (9) with Second generator (4) connects, and generator (3) is had steam channel to connect with condenser (5) and is adjusted to generator (3) and has steam logical After road is connected with the 3rd generator (11), the 3rd generator (11) has condensed fluid pipeline again through heater (16) and the second generation Device (4) and ft connection, the 3rd generator (11) also has steam channel to connect with condenser (5), and heater (16) is also added Hot media channel and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 16. heat, are that any hot described in claim 5-8 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and heater, the second absorber (2) is had weak solution pipeline through solution pump (6) and Two solution heat exchangers (9) connect with generator (3) be adjusted to the second absorber (2) have weak solution pipeline through solution pump (6) and Second solution heat exchanger (9) is connected with the 3rd generator (11), and the 3rd generator (11) has concentrated solution pipeline molten through the 3rd again Liquid pump (13) is connected with generator (3) with the 3rd solution heat exchanger (14), and generator (3) is had concentrated solution pipeline molten through second Liquid heat exchanger (9) is connected with the second generator (4) and is adjusted to generator (3) and has concentrated solution pipeline through the 3rd solution heat exchanger (14) with the second solution heat exchanger (9) is connected with the second generator (4), and generator (3) is had steam channel and condenser (5) Connection is adjusted to the 3rd generator (11) after generator (3) has steam channel to connect with the 3rd generator (11) condensed fluid again Pipeline also has steam channel and condenser through heater (16) and the second generator (4) and ft connection, the 3rd generator (11) (5) connect, heater (16) also has heated medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is that any hot described in claim 11-16 moves in co-feeding system, the 3rd generator (11) Set up high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 18. heat, are that any hot described in claim 1,3 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (8) connect with the second absorber (2) and be adjusted to absorber (1) and have weak solution pipeline through the 3rd solution heat exchanger (14) and the 3rd Absorber (12) connects, and the 3rd absorber (12) has weak solution pipeline again through the 3rd solution pump (13) and solution heat exchanger (8) Connect with the second absorber (2), the second generator (4) is had concentrated solution pipeline through the second solution pump (7) and solution heat exchanger (8) connect with absorber (1) be adjusted to the second generator (4) have concentrated solution pipeline through solution heat exchanger (8) with the 3rd generation Device (11) connects, and the 3rd generator (11) has concentrated solution pipeline again through the second solution pump (7) and the 3rd solution heat exchanger (14) Connect with absorber (1), after engine (10) is had exhaust passage to connect with the second generator (4), the second generator (4) is again Having condensed fluid passage and ft connection to be adjusted to engine (10) has exhaust passage to be sequentially communicated the second generator (4) and the 3rd After raw device (11), the 3rd generator (11) has condensed fluid passage and ft connection again, and the 3rd generator (11) also has steam channel Connect with the 3rd absorber (12), the 3rd absorber (12) also has coolant guiding channel and ft connection, form the dynamic alliance system of heat System；Wherein, after or engine (10) being had exhaust passage to connect with the second generator (4), the second generator (4) has condensation again Liquid passage and ft connection are adjusted to engine (10) has exhaust passage to be sequentially communicated the 3rd generator (11) and the second generator (4) after, the second generator (4) has condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 19. heat, are that any hot described in claim 2,4 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (8) connect with the second absorber (2) and be adjusted to absorber (1) and have weak solution pipeline through the 3rd solution heat exchanger (14) and the 3rd Absorber (12) connects, and the 3rd absorber (12) has weak solution pipeline again through the 3rd solution pump (13) and solution heat exchanger (8) Connect with the second absorber (2), the second generator (4) is had concentrated solution pipeline through the second solution pump (7) and solution heat exchanger (8) connect with absorber (1) be adjusted to the second generator (4) have concentrated solution pipeline through solution heat exchanger (8) with the 3rd generation Device (11) connects, and the 3rd generator (11) has concentrated solution pipeline again through the second solution pump (7) and the 3rd solution heat exchanger (14) Connect with absorber (1), the second generator after engine (10) is had the first steam channel to connect with the second generator (4) (4) having condensed fluid passage and ft connection to be adjusted to engine (10) again has the first steam channel to be sequentially communicated the second generator (4) and the 3rd generator (11) after the 3rd generator (11) have condensed fluid passage and ft connection again, the 3rd generator (11) Steam channel is also had to connect with the 3rd absorber (12), the 3rd absorber (12) also has coolant guiding channel and ft connection, shape Become the dynamic co-feeding system of heat；Wherein, second after or engine (10) being had the first steam channel to connect with the second generator (4) Raw device (4) has condensed fluid passage and ft connection to be adjusted to engine (10) again has the first steam channel to be sequentially communicated the 3rd generation After device (11) and the second generator (4), the second generator (4) has condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 20. heat, are that any hot described in claim 4 moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (8) Connect with the second absorber (2) be adjusted to absorber (1) have weak solution pipeline through the 3rd solution heat exchanger (14) with the 3rd suction Receive device (12) connection, the 3rd absorber (12) have weak solution pipeline through the 3rd solution pump (13) and solution heat exchanger (8) again and Second absorber (2) connects, and the second generator (4) is had concentrated solution pipeline through the second solution pump (7) and solution heat exchanger (8) Connect with absorber (1) and be adjusted to the second generator (4) and have concentrated solution pipeline through solution heat exchanger (8) and the 3rd generator (11) connect, the 3rd generator (11) have concentrated solution pipeline through the second solution pump (7) and the 3rd solution heat exchanger (14) again and Absorber (1) connects, and engine (10) is had exhaust passage and ft connection to be adjusted to engine (10) exhaust passage and the After three generators (11) connection, the 3rd generator (11) has condensed fluid passage and ft connection again, and the 3rd generator (11) also has Steam channel is connected with the 3rd absorber (12), and the 3rd absorber (12) also has coolant guiding channel and ft connection, forms heat Dynamic co-feeding system；Wherein, or the 3rd generator after exhaust passage is connected set up with the 3rd generator (11) by engine (10) (11) there are condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 21. heat, are that any hot described in claim 5,7 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (8) connect with the second absorber (2) and be adjusted to absorber (1) and have weak solution pipeline through the 3rd solution heat exchanger (14) and the 3rd Absorber (12) connects, and the 3rd absorber (12) has weak solution pipeline again through the 3rd solution pump (13) and solution heat exchanger (8) Connect with the second absorber (2), the second generator (4) is had concentrated solution pipeline through the second solution pump (7) and solution heat exchanger (8) connect with absorber (1) be adjusted to the second generator (4) have concentrated solution pipeline through solution heat exchanger (8) with the 3rd generation Device (11) connects, and the 3rd generator (11) has concentrated solution pipeline again through the second solution pump (7) and the 3rd solution heat exchanger (14) Connect with absorber (1), by the second generator (4) have condensed fluid pipeline and ft connection be adjusted to the second generator (4) have cold Lime set pipeline, through the 3rd generator (11) and ft connection, engine (10) is had exhaust passage to connect with the second generator (4) Second generator (4) has condensed fluid passage and ft connection to be adjusted to engine (10) more afterwards has exhaust passage to be sequentially communicated the After two generators (4) and the 3rd generator (11), the 3rd generator (11) has condensed fluid passage and ft connection again, the 3rd Raw device (11) also has steam channel to connect with the 3rd absorber (12), and the 3rd absorber (12) also has coolant guiding channel and outside Connection, forms the dynamic co-feeding system of heat；Wherein, or by engine (10) the first steam channel is had to connect it with the second generator (4) Second generator (4) has condensed fluid passage and ft connection to be adjusted to engine (10) more afterwards has the first steam channel to be sequentially communicated After 3rd generator (11) and the second generator (4), the second generator (4) has condensed fluid passage and ft connection again.
The dynamic co-feeding system of 22. heat, is that the heat described in claim 6,8 is moved in co-feeding system, increases the 3rd generator, the 3rd suction Receive device, the 3rd solution pump and the 3rd solution heat exchanger, by absorber (1) have weak solution pipeline through solution heat exchanger (8) with Second absorber (2) connection is adjusted to absorber (1) has weak solution pipeline through the 3rd solution heat exchanger (14) and the 3rd absorption Device (12) connects, and the 3rd absorber (12) has weak solution pipeline again through the 3rd solution pump (13) and solution heat exchanger (8) and the Two absorbers (2) connect, the second generator (4) is had concentrated solution pipeline through the second solution pump (7) and solution heat exchanger (8) and Absorber (1) connection is adjusted to the second generator (4) has concentrated solution pipeline through solution heat exchanger (8) and the 3rd generator (11) Connection, the 3rd generator (11) has concentrated solution pipeline again through the second solution pump (7) and the 3rd solution heat exchanger (14) and absorption Device (1) connects, and the second generator (4) is had condensed fluid pipeline and ft connection to be adjusted to the second generator (4) condensate line Lu Jing tri- generator (11) and ft connection, engine (10) is had the first steam channel to connect it with the second generator (4) Second generator (4) has condensed fluid passage and ft connection to be adjusted to engine (10) more afterwards has the first steam channel to be sequentially communicated After second generator (4) and the 3rd generator (11), the 3rd generator (11) has condensed fluid passage and ft connection again, and the 3rd Generator (11) also has steam channel to connect with the 3rd absorber (12), and the 3rd absorber (12) also has coolant guiding channel with outward Portion connects, and forms the dynamic co-feeding system of heat；Wherein, or by engine (10) the first steam channel is had to connect with the second generator (4) Second generator (4) has condensed fluid passage and ft connection to be adjusted to engine (10) more afterwards has the first steam channel to connect successively After logical 3rd generator (11) and the second generator (4), the second generator (4) has condensed fluid passage and ft connection again.
The dynamic co-feeding system of 23. heat, is that the heat described in claim 8 is moved in co-feeding system, increases the 3rd generator, the 3rd absorption Device, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (8) and the Two absorbers (2) connection is adjusted to absorber (1) has weak solution pipeline through the 3rd solution heat exchanger (14) and the 3rd absorber (12) connect, the 3rd absorber (12) has weak solution pipeline again through the 3rd solution pump (13) and solution heat exchanger (8) and second Absorber (2) connects, and the second generator (4) is had concentrated solution pipeline through the second solution pump (7) and solution heat exchanger (8) and suction Receipts device (1) connection is adjusted to the second generator (4) has concentrated solution pipeline through solution heat exchanger (8) with the 3rd generator (11) even Logical, the 3rd generator (11) has concentrated solution pipeline again through the second solution pump (7) and the 3rd solution heat exchanger (14) and absorber (1) connect, the second generator (4) is had condensed fluid pipeline and ft connection to be adjusted to the second generator (4) condensed fluid pipeline Through the 3rd generator (11) and ft connection, engine (10) is had exhaust passage and ft connection to be adjusted to engine (10) to be had After exhaust passage is connected with the 3rd generator (11), the 3rd generator (11) has condensed fluid passage and ft connection again, the 3rd Raw device (11) also has steam channel to connect with the 3rd absorber (12), and the 3rd absorber (12) also has coolant guiding channel and outside Connection, forms the dynamic co-feeding system of heat；Wherein, or engine (10) is set up after exhaust passage is connected with the 3rd generator (11) Three generators (11) have condensed fluid passage and ft connection again.
24. hot dynamic co-feeding systems, are to move in co-feeding system in any hot described in claim 1-23, cancel generator (3) with outward The high temperature thermal medium passage of portion's connection, generator (3) after high-temperature steam passage is connected set up with generator (3) by engine (10) There are high temperature condensed fluid passage and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 25. heat, are that any hot described in claim 9-10 moves in co-feeding system, cancel generator (3) and 3rd generator (11) the high temperature thermal medium passage with ft connection respectively, engine (10) is set up high-temperature steam passage and is connected successively After logical generator (3) and the 3rd generator (11), the 3rd generator (11) has high temperature condensed fluid passage and ft connection, shape again Become the dynamic co-feeding system of heat.
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CN104654653A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104654652A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104864623A (en) * 2014-01-27 2015-08-26 李华玉 Thermodynamic combined supply system

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US4439999A (en) * 1981-12-09 1984-04-03 Hitachi, Ltd. Absorption type refrigeration system
CN101093118A (en) * 2007-07-08 2007-12-26 李华玉 Single stage composite absorption type compressor
CN102482949A (en) * 2009-06-25 2012-05-30 苏庆泉 Power cycle system and power cycle method
CN102679615A (en) * 2012-05-04 2012-09-19 李华玉 Sectional heat return third-class absorption heat pump
CN104180557A (en) * 2013-07-30 2014-12-03 李华玉 Combined heat power system, combined cooling power system and combined heat-cooling power dual-purpose system
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