CN106524561A - Combined heat and power supply system - Google Patents

Combined heat and power supply system Download PDF

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Publication number
CN106524561A
CN106524561A CN201610822200.4A CN201610822200A CN106524561A CN 106524561 A CN106524561 A CN 106524561A CN 201610822200 A CN201610822200 A CN 201610822200A CN 106524561 A CN106524561 A CN 106524561A
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China
Prior art keywords
generator
solution
connection
absorber
connect
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CN201610822200.4A
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Chinese (zh)
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CN106524561B (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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • 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
    • F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
    • 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
    • F25B33/00—Boilers; Analysers; Rectifiers
    • 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
    • F25B37/00—Absorbers; Adsorbers
    • 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
    • F25B41/30—Expansion means; Dispositions thereof
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems
    • Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
    • 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)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Power Engineering (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

The invention provides a combined heat and power supply system and belongs to the technical fields of combined cooling, heating and power and heat pumps. An absorber, a generator, a second generator, a condenser, a second condenser, an evaporator, a throttling valve, a refrigerant pump, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger compose an absorption heat pump circulating system. Low-temperature heat load is supplied to the second generator through liquid refrigerant. A power machine supplies low-temperature heat load to the second generator through a steam exhausting channel and supplies low-temperature heat load to the evaporator through a first steam channel. The generator communicates with the outside through a high-temperature medium channel; the absorber and the condenser each communicates with the outside through a heated medium channel; and the second condenser communicates with the outside through a cooling medium channel, so that the combined heat and power supply 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 for being difficult to effectively utilizes, cause the comprehensive energy of the dynamic co-feeding system of heat Source utilization rate is not high, and the utilization to clean energy resource in the dynamic co-feeding system of heat brings 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 the efficiency that lifting power machine job security and heat energy are converted into mechanical energy, and considers to adapt to the dynamic alliance of heat The utilization of clean energy resource in system, proposes with engine end steam discharge or low-pressure pumping steam is as low-temperature heat source and combines absorption heat pump The dynamic co-feeding system of the series of heat of technology.
The 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. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute Composition；Absorber has weak solution pipeline Jing solution pump and solution heat exchanger to connect with generator, and generator also has concentrated solution pipe Road Jing solution heat exchangers and the second solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipeline Jing Second solution pump and the second solution heat exchanger are connected with absorber, and generator also has refrigerant steam channel to connect with condenser, Second generator also has refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline and the second generator to connect After logical, the second generator has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, and the second condenser also has cryogen liquid pipeline Jing Cryogen liquid pump is connected with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, engine have live steam passage with it is outer Portion's connection, also engine or exhaust passage and ft connection, engine also have exhaust passage to be sequentially communicated vaporizer and second After generator, the second generator has condensed fluid passage and ft connection, absorber and condenser also to have heated medium respectively again Passage and ft connection, the second condenser also have coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage With ft connection, the dynamic co-feeding system of heat is formed.
2. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute Composition；Absorber has weak solution pipeline Jing solution pump and solution heat exchanger to connect with generator, and generator also has concentrated solution pipe Road Jing solution heat exchangers and the second solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipeline Jing Second solution pump and the second solution heat exchanger are connected with absorber, and generator also has refrigerant steam channel to connect with condenser, Second generator also has refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline and the second generator to connect After logical, the second generator has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, and the second condenser also has cryogen liquid pipeline Jing Cryogen liquid pump is connected with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage respectively With ft connection and have exhaust passage and ft connection, engine also has the first steam channel to be sequentially communicated vaporizer and second After raw device, the second generator has the first condensed fluid passage and ft connection, absorber and condenser also to have heated Jie respectively again Matter passage and ft connection, the second condenser also have coolant guiding channel and ft connection, and generator also has high temperature thermal medium to lead to Road and ft connection, form the dynamic co-feeding system of heat.
3. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute Composition；Absorber has weak solution pipeline Jing solution pump and solution heat exchanger to connect with generator, and generator also has concentrated solution pipe Road Jing solution heat exchangers and the second solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipeline Jing Second solution pump and the second solution heat exchanger are connected with absorber, and generator also has refrigerant steam channel to connect with condenser, Second generator also has refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline and the second generator to connect After logical, the second generator has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, and the second condenser also has cryogen liquid pipeline Jing Cryogen liquid pump is connected with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, engine have live steam passage with it is outer Portion's connection, also engine or exhaust passage and ft connection, after engine also has exhaust passage to connect with the second generator Second generator is evaporated after having condensed fluid passage and ft connection, engine to also have the first steam channel to be connected with vaporizer again Device has the first condensed fluid passage and ft connection, absorber and condenser also to have heated medium passage to connect with outside respectively again Logical, the second condenser also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, shape Into the dynamic co-feeding system of heat.
4. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, evaporation Device, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute Composition；Absorber has weak solution pipeline Jing solution pump and solution heat exchanger to connect with generator, and generator also has concentrated solution pipe Road Jing solution heat exchangers and the second solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipeline Jing Second solution pump and the second solution heat exchanger are connected with absorber, and generator also has refrigerant steam channel to connect with condenser, Second generator also has refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline and the second generator to connect After logical, the second generator has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, and the second condenser also has cryogen liquid pipeline Jing Cryogen liquid pump is connected with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, and engine has live steam passage respectively With ft connection and have exhaust passage and ft connection, engine also have the first steam channel to connect with the second generator after Two generators are steamed after having the first condensed fluid passage and ft connection, engine to also have the second steam channel to be connected with vaporizer again Sending out device has the second condensed fluid passage and ft connection, absorber and condenser also to have heated medium passage to connect with outside respectively again Logical, the second condenser also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium passage and ft connection, shape Into the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in 1-4 items, increase the 3rd generator, the Absorber is had weak solution pipeline Jing solution pump and solution heat to hand over by two absorbers, the 3rd solution pump and the 3rd solution heat exchanger Parallel operation is connected with generator and is adjusted to absorber and has weak solution pipeline Jing solution pump and solution heat exchanger and the second absorber to connect Logical, the second absorber has the 3rd solution pumps of weak solution pipeline Jing and the 3rd solution heat exchanger to connect with generator again, will occur Device has concentrated solution pipeline Jing solution heat exchangers and the second solution heat exchanger to connect with the second generator to be adjusted to generator and have The 3rd solution heat exchangers of concentrated solution pipeline Jing are connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline Jing solution heat again Exchanger and the second solution heat exchanger are connected with the second generator, and the 3rd generator also has refrigerant steam channel to absorb with second Device is connected, and the 3rd generator also has high temperature thermal medium passage and ft connection, the second absorber also have heated medium passage with Ft connection, forms the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in 1-4 items, increase the 3rd generator, the Generator is had refrigerant steam channel to connect adjustment with condenser by two absorbers, the 3rd solution pump and the 3rd solution heat exchanger Have refrigerant steam channel to connect with the second absorber for generator, the second absorber also have the 3rd solution pumps of weak solution pipeline Jing and 3rd solution heat exchanger is connected with the 3rd generator, the 3rd generator also have the 3rd solution heat exchangers of concentrated solution pipeline Jing with Second absorber is connected, and the 3rd generator also has refrigerant steam channel to connect with condenser, and the 3rd generator also has high warm to be situated between Matter passage and ft connection, the second absorber also have heated medium passage and ft connection, form the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is, in the dynamic co-feeding system of any hot described in 1-6 items, to cancel choke valve, by second Generator has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer to be adjusted to the second generator and have cryogen liquid pipeline and vaporizer to connect It is logical, form the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in 1-4 items, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger, second throttle and heater, absorber set up the 3rd solution pumps of weak solution pipeline Jing Connect with the 3rd generator with the 3rd solution heat exchanger, the 3rd generator also has the 3rd solution heat exchangers of concentrated solution pipeline Jing Connect with the second solution heat exchanger with the second generator, by generator have refrigerant steam channel connect with condenser be adjusted to send out Raw device have refrigerant steam channel to connect with the 3rd generator after the 3rd generator have again cryogen liquid pipeline Jing heaters, second Raw device and second throttle are connected with vaporizer, and the 3rd generator also has refrigerant steam channel to connect with condenser, and heater is also There are heated medium passage and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in 1-4 items, increase the 3rd generator, the Absorber is had weak solution pipeline Jing solution pump and solution heat exchanger by three solution heat exchangers, second throttle and heater Connect with generator be adjusted to absorber have weak solution pipeline Jing solution pumps, solution heat exchanger and the 3rd solution heat exchanger with Generator is connected, and has concentrated solution pipeline Jing solution heat exchangers and the second solution heat exchanger and the second generator to connect in generator Logical to be adjusted to generator and have the 3rd solution heat exchangers of concentrated solution pipeline Jing to connect with the 3rd generator, the 3rd generator has dense again Solution line Jing solution heat exchangers and the second solution heat exchanger are connected with the second generator, have refrigerant vapour to lead in generator Road is connected with condenser and is adjusted to the 3rd generator after generator has refrigerant steam channel to connect with the 3rd generator and has cold again Agent liquid pipeline Jing heaters, the second generator and second throttle are connected with vaporizer, and the 3rd generator also has refrigerant vapour to lead to Road is connected with condenser, and heater also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in 1-4 items, increase the 3rd generator, the Absorber is had weak solution pipeline Jing solution pump and molten by three solution pumps, the 3rd solution heat exchanger, second throttle and heater Liquid heat exchanger is connected with generator and is adjusted to absorber and has weak solution pipeline Jing solution pump and solution heat exchanger and the 3rd Raw device connection, the 3rd generator have the 3rd solution pumps of concentrated solution pipeline Jing and the 3rd solution heat exchanger to connect with generator again, By generator have concentrated solution pipeline Jing solution heat exchangers and the second solution heat exchanger connect with the second generator be adjusted to send out Raw device has the 3rd solution heat exchangers of concentrated solution pipeline Jing, solution heat exchanger and the second solution heat exchanger and the second generator Generator is had refrigerant steam channel to connect with condenser and is adjusted to generator and has refrigerant steam channel and the 3rd generator by connection After connection, the 3rd generator has cryogen liquid pipeline Jing heaters, the second generator and second throttle to connect with vaporizer again, 3rd generator also has refrigerant steam channel to connect with condenser, and heater also has heated medium passage and ft connection, shape Into the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, is that the 3rd generator sets up height in the dynamic co-feeding system of any hot described in 8-10 items Warm passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. heat, is, in the dynamic co-feeding system of any hot described in 8-11 items, to cancel choke valve and second Second generator is had cryogen liquid pipeline warp knuckle stream valve to be connected with vaporizer and is adjusted to the second generator and has cryogen liquid pipe by choke valve Road is connected with vaporizer, is had cryogen liquid pipeline Jing second throttle to connect with vaporizer in the second generator and is adjusted to the second generation Device has cryogen liquid pipeline to connect with vaporizer, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, is, in the dynamic co-feeding system of heat described in the 1st, to increase the 3rd generator, the second absorption Absorber is had weak solution pipeline Jing solution pump and solution heat exchanger to connect tune with generator by device and the 3rd solution heat exchanger Whole to have the 3rd solution heat exchangers of weak solution pipeline Jing to connect with the second absorber for absorber, the second absorber has weak solution again Pipeline Jing solution pump and solution heat exchanger are connected with generator, by the second generator have concentrated solution pipeline Jing the second solution pumps and Second solution heat exchanger connect with absorber be adjusted to the second generator have the second solution heat exchangers of concentrated solution pipeline Jing with 3rd generator is connected, and the 3rd generator has concentrated solution pipeline Jing the second solution pumps and the 3rd solution heat exchanger and absorber again Connection, after having cryogen liquid pipeline to connect with the second generator condenser, the second generator has cryogen liquid pipeline warp knuckle stream valve again Connect with vaporizer and be adjusted to the 3rd generation after condenser there are cryogen liquid pipeline the second generators of Jing to connect with the 3rd generator Device has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, has exhaust passage to be sequentially communicated vaporizer and second in engine After raw device, the second generator has condensed fluid passage to be adjusted to engine with ft connection again has exhaust passage to be sequentially communicated evaporation After device, the second generator and the 3rd generator, the 3rd generator has condensed fluid passage and ft connection again, and the 3rd generator is also There is refrigerant steam channel to connect with the second absorber, the second absorber also has coolant guiding channel and ft connection, form heat dynamic Co-feeding system.
The dynamic co-feeding system of 14. heat, is, in the dynamic co-feeding system of heat described in the 2nd, to increase the 3rd generator, the second absorption Absorber is had weak solution pipeline Jing solution pump and solution heat exchanger to connect tune with generator by device and the 3rd solution heat exchanger Whole to have the 3rd solution heat exchangers of weak solution pipeline Jing to connect with the second absorber for absorber, the second absorber has weak solution again Pipeline Jing solution pump and solution heat exchanger are connected with generator, by the second generator have concentrated solution pipeline Jing the second solution pumps and Second solution heat exchanger connect with absorber be adjusted to the second generator have the second solution heat exchangers of concentrated solution pipeline Jing with 3rd generator is connected, and the 3rd generator has concentrated solution pipeline Jing the second solution pumps and the 3rd solution heat exchanger and absorber again Connection, after having cryogen liquid pipeline to connect with the second generator condenser, the second generator has cryogen liquid pipeline warp knuckle stream valve again Connect with vaporizer and be adjusted to the 3rd generation after condenser there are cryogen liquid pipeline the second generators of Jing to connect with the 3rd generator Device has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, has the first steam channel to be sequentially communicated vaporizer and in engine After two generators, the second generator has the first condensed fluid passage to be adjusted to engine with ft connection again and has the first steam channel After being sequentially communicated vaporizer, the second generator and the 3rd generator, the 3rd generator has the first condensed fluid passage and outside to connect again Logical, the 3rd generator also has refrigerant steam channel to connect with the second absorber, the second absorber also have coolant guiding channel with it is outer Portion connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, is, in the dynamic co-feeding system of heat described in the 3rd, to increase the 3rd generator, the second absorption Absorber is had weak solution pipeline Jing solution pump and solution heat exchanger to connect tune with generator by device and the 3rd solution heat exchanger Whole to have the 3rd solution heat exchangers of weak solution pipeline Jing to connect with the second absorber for absorber, the second absorber has weak solution again Pipeline Jing solution pump and solution heat exchanger are connected with generator, by the second generator have concentrated solution pipeline Jing the second solution pumps and Second solution heat exchanger connect with absorber be adjusted to the second generator have the second solution heat exchangers of concentrated solution pipeline Jing with 3rd generator is connected, and the 3rd generator has concentrated solution pipeline Jing the second solution pumps and the 3rd solution heat exchanger and absorber again Connection, after having cryogen liquid pipeline to connect with the second generator condenser, the second generator has cryogen liquid pipeline warp knuckle stream valve again Connect with vaporizer and be adjusted to the 3rd generation after condenser there are cryogen liquid pipeline the second generators of Jing to connect with the 3rd generator Device has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, after having exhaust passage to connect with the second generator in engine Two generators have condensed fluid passage to be adjusted to engine with ft connection again has the 3rd generators of exhaust passage Jing and second to occur After device connection, the second generator has condensed fluid passage and ft connection again, and the 3rd generator also has refrigerant steam channel and second Absorber is connected, and the second absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or will be dynamic After power machine has exhaust passage to connect with the second generator, the second generator has condensed fluid passage to be adjusted to dynamic with ft connection again After power machine has the second generators of exhaust passage Jing to connect with the 3rd generator, the 3rd generator has condensed fluid passage again with outside Connection.
The dynamic co-feeding system of 16. heat, is, in the dynamic co-feeding system of heat described in the 4th, to increase the 3rd generator, the second absorption Absorber is had weak solution pipeline Jing solution pump and solution heat exchanger to connect tune with generator by device and the 3rd solution heat exchanger Whole to have the 3rd solution heat exchangers of weak solution pipeline Jing to connect with the second absorber for absorber, the second absorber has weak solution again Pipeline Jing solution pump and solution heat exchanger are connected with generator, by the second generator have concentrated solution pipeline Jing the second solution pumps and Second solution heat exchanger connect with absorber be adjusted to the second generator have the second solution heat exchangers of concentrated solution pipeline Jing with 3rd generator is connected, and the 3rd generator has concentrated solution pipeline Jing the second solution pumps and the 3rd solution heat exchanger and absorber again Connection, after having cryogen liquid pipeline to connect with the second generator condenser, the second generator has cryogen liquid pipeline warp knuckle stream valve again Connect with vaporizer and be adjusted to the 3rd generation after condenser there are cryogen liquid pipeline the second generators of Jing to connect with the 3rd generator Device has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, has the first steam channel to connect it with the second generator in engine Second generator has the first condensed fluid passage to be adjusted to engine with ft connection again and has the 3rd generations of the first steam channel Jing afterwards After device is connected with the second generator, the second generator has the first condensed fluid passage and ft connection again, and the 3rd generator is also cold Agent steam channel is connected with the second absorber, and the second absorber also has coolant guiding channel and ft connection, forms the dynamic alliance of heat System；Wherein, after or having the first steam channel to connect with the second generator in engine, the second generator has the first condensation again Liquid passage is adjusted to after engine has first the second generators of steam channel Jing to connect with the 3rd generator with ft connection Three generators have the first condensed fluid passage and ft connection again.
The dynamic co-feeding system of 17. heat, is, in the dynamic co-feeding system of heat described in the 4th, to increase the 3rd generator, the second absorption Absorber is had weak solution pipeline Jing solution pump and solution heat exchanger to connect tune with generator by device and the 3rd solution heat exchanger Whole to have the 3rd solution heat exchangers of weak solution pipeline Jing to connect with the second absorber for absorber, the second absorber has weak solution again Pipeline Jing solution pump and solution heat exchanger are connected with generator, by the second generator have concentrated solution pipeline Jing the second solution pumps and Second solution heat exchanger connect with absorber be adjusted to the second generator have the second solution heat exchangers of concentrated solution pipeline Jing with 3rd generator is connected, and the 3rd generator has concentrated solution pipeline Jing the second solution pumps and the 3rd solution heat exchanger and absorber again Connection, after having cryogen liquid pipeline to connect with the second generator condenser, the second generator has cryogen liquid pipeline warp knuckle stream valve again Connect with vaporizer and be adjusted to the 3rd generation after condenser there are cryogen liquid pipeline the second generators of Jing to connect with the 3rd generator Device has cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer again, has exhaust passage to be adjusted to engine with ft connection in engine After having exhaust passage to connect with the 3rd generator, the 3rd generator has condensed fluid passage and ft connection again, and the 3rd generator is also There is refrigerant steam channel to connect with the second absorber, the second absorber also has coolant guiding channel and ft connection, form heat dynamic Co-feeding system；Wherein, or engine set up the 3rd generator after exhaust passage is connected with the 3rd generator have again condensed fluid lead to Road and ft connection.
The dynamic co-feeding systems of 18. heat, are, in the dynamic co-feeding system of any hot described in 13-17 items, to cancel choke valve, by the Three generators have cryogen liquid pipeline warp knuckle stream valve to connect with vaporizer to be adjusted to the 3rd generator and have cryogen liquid pipeline and vaporizer Connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, is, in the dynamic co-feeding system of heat described in the 3rd, to increase preheater, by the second condenser There is cryogen liquid pipeline Jing cryogens liquid pump to connect with vaporizer to be adjusted to the second condenser and have cryogen liquid pipeline Jing cryogens liquid pump and pre- Hot device is connected with vaporizer, and having condensed fluid passage to be adjusted to the second generator with ft connection in the second generator has condensed fluid to lead to The preheated device in road and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 20. heat, is, in the dynamic co-feeding system of any hot described in 1-19 items, to cancel generator and connect High temperature thermal medium passage, engine set up generator after high-temperature steam passage is connected with generator have again high temperature condensed fluid lead to Road and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, is, in the dynamic co-feeding system of any hot described in 5-6 items, to cancel generator and the 3rd Generator high temperature thermal medium passage respectively with ft connection, engine are set up high-temperature steam passage and are 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.
Description of the drawings：
Fig. 1 is according to cogeneration system provided by the present invention 1st kind of structure and schematic flow sheet.
Fig. 2 is according to cogeneration system provided by the present invention 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to cogeneration system provided by the present invention 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to cogeneration system provided by the present invention 4th kind of structure and schematic flow sheet.
Fig. 5 is according to cogeneration system provided by the present invention 5th kind of structure and schematic flow sheet.
Fig. 6 is according to cogeneration system provided by the present invention 6th kind of structure and schematic flow sheet.
Fig. 7 is according to cogeneration system provided by the present invention 7th kind of structure and schematic flow sheet.
Fig. 8 is according to cogeneration system provided by the present invention 8th kind of structure and schematic flow sheet.
Fig. 9 is according to cogeneration system provided by the present invention 9th kind of structure and schematic flow sheet.
Figure 10 is according to cogeneration system provided by the present invention 10th kind of structure and schematic flow sheet.
Figure 11 is according to cogeneration system provided by the present invention 11st kind of structure and schematic flow sheet.
Figure 12 is according to cogeneration system provided by the present invention 12nd kind of structure and schematic flow sheet.
In figure, 1- absorbers, 2- generators, the second generators of 3-, 4- condensers, the second condensers of 5-, 6- vaporizers, 7- Choke valve, 8- cryogen liquid pumps, 9- solution pumps, 10- the second solution pumps, 11- solution heat exchangers, the second solution heat exchangers of 12-, 13- engines, the 3rd generators of 14-, the second absorbers of 15-, the 3rd solution pumps of 16-, the 3rd solution heat exchangers of 17-, 18- Two choke valves, 19- heaters, 20- preheaters.
Specific embodiment：
First it is noted that in the statement of structure and flow process, it is inessential in the case of do not repeat；To apparent Flow process do not state.Below in conjunction with the accompanying drawings with example describing the present invention in detail.
What the dynamic co-feeding system of heat shown in Fig. 1 was realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute group Into；Absorber 1 has weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 to connect with generator 2, and generator 2 also has dense molten Liquid pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 are connected with the second generator 3, and the second generator 3 is also dense The second solution of solution line Jing pump 10 and the second solution heat exchanger 12 are connected with absorber 1, and generator 2 also has refrigerant vapour to lead to Road is connected with condenser 4, and the second generator 3 also has refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen After liquid pipeline is connected with the second generator 3, the second generator 3 has cryogen liquid pipeline warp knuckle stream valve 7 to connect with vaporizer 6 again, the Two condensers 5 also have cryogen liquid pipeline Jing cryogens liquid pump 8 to connect with vaporizer 6, and vaporizer 6 also has refrigerant steam channel and absorption Device 1 is connected, and engine 13 has live steam passage and a ft connection, and engine 13 also has exhaust passage to be sequentially communicated vaporizer 6 and the After two generators 3, the second generator 3 has condensed fluid passage and ft connection, absorber 1 and condenser 4 also to have respectively again and is added Hot media channel and ft connection, the second condenser 5 also have coolant guiding channel and ft connection, and generator 2 also has high warm Medium channel and ft connection.
(2) in flow process, live steam enters 13 blood pressure lowering work done of engine, and the steam discharge of engine 13 flows through vaporizer 6 and second Raw device 3 progressively heat release is condensed, and is externally discharged afterwards；The weak solution Jing solution pump 9 of absorber 1 and solution heat exchanger 11 are entered Generator 2, high temperature thermal medium flow through generator 2, heating into the solution release refrigerant vapour in which and provide to condenser 4, The concentrated solution Jing solution heat exchanger 11 of generator 2 and the second solution heat exchanger 12 enter the second generator 3, heat absorption and discharge cold Agent steam is simultaneously provided to the second condenser 5, the second solution of concentrated solution Jing pump 10 of the second generator 3 and the second solution heat exchanger 12 enter absorber 1, absorption refrigerant vapour heat release in heated medium；The refrigerant vapour heat release of condenser 4 is in heated Jie Matter flows through the second generator 3 heat release into cryogen liquid, the cryogen liquid of condenser 4, flows through 7 reducing pressure by regulating flow of choke valve afterwards and enters and steams Device 6 is sent out, refrigerant vapour is absorbed heat into and is provided to absorber 1, the refrigerant vapour heat release of the second condenser 5 is in cooling medium into cryogen Liquid, the cryogen liquid of the second condenser 5 flow through and enter vaporizer 6 after cryogen liquid pump 8 pressurizes, absorb heat into refrigerant vapour and to absorption Device 1 is provided, and forms the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 2 was realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute group Into；Absorber 1 has weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 to connect with generator 2, and generator 2 also has dense molten Liquid pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 are connected with the second generator 3, and the second generator 3 is also dense The second solution of solution line Jing pump 10 and the second solution heat exchanger 12 are connected with absorber 1, and generator 2 also has refrigerant vapour to lead to Road is connected with condenser 4, and the second generator 3 also has refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen After liquid pipeline is connected with the second generator 3, the second generator 3 has cryogen liquid pipeline warp knuckle stream valve 7 to connect with vaporizer 6 again, the Two condensers 5 also have cryogen liquid pipeline Jing cryogens liquid pump 8 to connect with vaporizer 6, and vaporizer 6 also has refrigerant steam channel and absorption Device 1 is connected, and engine 13 has live steam passage and ft connection respectively and has exhaust passage and ft connection, engine 13 also the After one steam channel is sequentially communicated vaporizer 6 and the second generator 3, the second generator 3 has the first condensed fluid passage again with outside Connection, absorber 1 and condenser 4 also have heated medium passage and ft connection respectively, and the second condenser 5 also has cooling medium Passage and ft connection, generator 2 also have high temperature thermal medium passage and ft connection.
(2), in flow process, compare with the dynamic co-feeding system workflow of heat shown in Fig. 1, in place of the flow process for changing be Live steam is divided into two-way into after 13 blood pressure lowering work done of engine, and the first via is supplied to vaporizer 6 and by the first steam channel Externally discharge after two generators, 3 exothermic condensation, the second road is externally discharged after completing blood pressure lowering work done, form the dynamic alliance system of heat System.
What the dynamic co-feeding system of heat shown in Fig. 3 was realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute group Into；Absorber 1 has weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 to connect with generator 2, and generator 2 also has dense molten Liquid pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 are connected with the second generator 3, and the second generator 3 is also dense The second solution of solution line Jing pump 10 and the second solution heat exchanger 12 are connected with absorber 1, and generator 2 also has refrigerant vapour to lead to Road is connected with condenser 4, and the second generator 3 also has refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen After liquid pipeline is connected with the second generator 3, the second generator 3 has cryogen liquid pipeline warp knuckle stream valve 7 to connect with vaporizer 6 again, the Two condensers 5 also have cryogen liquid pipeline Jing cryogens liquid pump 8 to connect with vaporizer 6, and vaporizer 6 also has refrigerant steam channel and absorption Device 1 is connected, and engine 13 has live steam passage and ft connection, and engine 13 also has exhaust passage and ft connection, engine 13 After also exhaust passage is connected with the second generator 3, the second generator 3 has condensed fluid passage and ft connection, engine 13 again The finisher 6 that also the first steam channel is connected with vaporizer 6 has the first condensed fluid passage and ft connection, absorber 1 again Also there are heated medium passage and ft connection respectively with condenser 4, the second condenser 5 also has coolant guiding channel to connect with outside Logical, generator 2 also has high temperature thermal medium passage and ft connection.
(2), in flow process, compare with the dynamic co-feeding system workflow of heat shown in Fig. 1, in place of the flow process for changing be Live steam is divided into three tunnels into after 13 blood pressure lowering work done of engine, and for relative outlet, the steam with elevated pressures is steamed by first Vapour passage is externally discharged after being supplied to 6 exothermic condensation of vaporizer, is completed a part of steam discharge after blood pressure lowering work done and is supplied to Two generators, 3 exothermic condensation is simultaneously externally discharged, and is completed another part steam discharge after blood pressure lowering work done and is externally discharged, and forms the dynamic connection of heat For system.
What the dynamic co-feeding system of heat shown in Fig. 4 was realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine institute group Into；Absorber 1 has weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 to connect with generator 2, and generator 2 also has dense molten Liquid pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 are connected with the second generator 3, and the second generator 3 is also dense The second solution of solution line Jing pump 10 and the second solution heat exchanger 12 are connected with absorber 1, and generator 2 also has refrigerant vapour to lead to Road is connected with condenser 4, and the second generator 3 also has refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen After liquid pipeline is connected with the second generator 3, the second generator 3 has cryogen liquid pipeline warp knuckle stream valve 7 to connect with vaporizer 6 again, the Two condensers 5 also have cryogen liquid pipeline Jing cryogens liquid pump 8 to connect with vaporizer 6, and vaporizer 6 also has refrigerant steam channel and absorption Device 1 is connected, and engine 13 has live steam passage and ft connection respectively and has exhaust passage and ft connection, engine 13 also the After one steam channel is connected with the second generator 3, the second generator 3 has the first condensed fluid passage and ft connection, engine again 13 also have the finisher 6 that the second steam channel is connected with vaporizer 6 to have the second condensed fluid passage and ft connection, absorber again 1 and condenser 4 also have heated medium passage and ft connection respectively, the second condenser 5 also have coolant guiding channel with it is outside Connection, generator 2 also have high temperature thermal medium passage and ft connection.
(2), in flow process, compare with the dynamic co-feeding system workflow of heat shown in Fig. 1, in place of the flow process for changing be After live steam enters 13 blood pressure lowering work done of engine, the second steam channels of Jing are supplied to the first steam channel of vaporizer 6 and Jing respectively It is supplied to the second generator 3, remaining steam to continue to complete work done and externally discharge；First steam flows through 3 heat release of the second generator Externally discharge after condensation, the second steam is externally discharged after flowing through 6 exothermic condensation of vaporizer, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 5 was realized in：
(1) in structure, in the dynamic co-feeding system of heat shown in Fig. 3, increase the 3rd generator, the second absorber, the 3rd molten Absorber 1 is had weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 and generator by liquid pump and the 3rd solution heat exchanger 2 connections are adjusted to absorber 1 has weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 to connect with the second absorber 15, the Two absorbers 15 have the 3rd solution pumps 16 of weak solution pipeline Jing and the 3rd solution heat exchanger 17 to connect with generator 2 again, will send out Raw device 2 has concentrated solution pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 to connect with the second generator 3 to be adjusted to Generator 2 has the 3rd solution heat exchangers 17 of concentrated solution pipeline Jing to connect with the 3rd generator 14, and the 3rd generator 14 has dense again Solution line Jing solution heat exchangers 11 and the second solution heat exchanger 12 are connected with the second generator 3, and the 3rd generator 14 is also There is refrigerant steam channel to connect with the second absorber 15, the 3rd generator 14 also has high temperature thermal medium passage and ft connection, the Two absorbers 15 also have heated medium passage and ft connection.
(2), in flow process, 1 weak solution Jing solution pump 9 of absorber and solution heat exchanger 11 enter the second absorber 15, absorb Refrigerant vapour heat release are in heated medium, the 3rd solution pump 16 of weak solution Jing of the second absorber 15 and the 3rd solution heat exchange Device 17 enters generator 2, and the 3rd solution heat exchanger 17 of concentrated solution Jing of generator 2 enters the 3rd generator 14, and high warm is situated between The 3rd generator 14 of mass flow Jing, heating discharge refrigerant vapour into the solution in which and provide to the second absorber 15, the 3rd The concentrated solution Jing solution heat exchanger 11 of raw device 14 and the second solution heat exchanger 12 enter the second generator 3, form the dynamic connection of heat For system.
What the dynamic co-feeding system of heat shown in Fig. 6 was realized in：
(1) in structure, in the dynamic co-feeding system of heat shown in Fig. 3, increase the 3rd generator, the second absorber, the 3rd molten Generator 2 is had refrigerant steam channel to be connected with condenser 4 and is adjusted to generator 2 and has cold by liquid pump and the 3rd solution heat exchanger Agent steam channel is connected with the second absorber 15, and the second absorber 15 also has the 3rd solution pumps 16 and the 3rd of weak solution pipeline Jing molten Liquid heat exchanger 17 is connected with the 3rd generator 14, and the 3rd generator 14 also has the 3rd solution heat exchangers 17 of concentrated solution pipeline Jing Connect with the second absorber 15, the 3rd generator 14 also has refrigerant steam channel to connect with condenser 4, and the 3rd generator 14 also has High temperature thermal medium passage and ft connection, the second absorber 15 also have heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 is produced enters the second absorber 15, the weak solution of the second absorber 15 The 3rd solution pumps 16 of Jing and the 3rd solution heat exchanger 17 enter the 3rd generator 14, and high temperature thermal medium flows through the 3rd generator 14th, heating is provided into the solution release refrigerant vapour in which and to condenser 4, and concentrated solution Jing the 3rd of the 3rd generator 14 is molten Liquid heat exchanger 17 enters the second absorber 15, absorbs refrigerant vapour and heat release is in heated medium, forms the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 7 was realized in：
(1) in structure, in the dynamic co-feeding system of heat shown in Fig. 3, increase the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger, second throttle and heater, absorber 1 set up the 3rd solution pumps 16 of weak solution pipeline Jing and the 3rd solution heat Exchanger 17 is connected with the 3rd generator 14, and the 3rd generator 14 also has the 3rd solution heat exchangers 17 of concentrated solution pipeline Jing and the Two solution heat exchangers 12 are connected with the second generator 3, are had refrigerant steam channel to connect with condenser 4 in generator 2 and are adjusted to After generator 2 has refrigerant steam channel to connect with the 3rd generator 14, the 3rd generator 14 has cryogen liquid pipeline Jing heaters again 19th, the second generator 3 and second throttle 18 are connected with vaporizer 6, and the 3rd generator 14 also has refrigerant steam channel and condensation Device 4 is connected, and heater 19 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 is produced is supplied to the 3rd generator 14 to make driving thermal medium, absorber 1 The 3rd solution pump 16 of part weak solution Jing and the 3rd solution heat exchanger 17 enter the 3rd generator 14, refrigerant vapour flows through the Three generators 14, heating discharge refrigerant vapour into the solution in which and provide to condenser 4, the concentrated solution of the 3rd generator 14 The 3rd solution heat exchangers 17 of Jing and the second solution heat exchanger 12 enter the second generator 3；Flow through the cold of the 3rd generator 14 Into cryogen liquid, cryogen liquid flows through heater 19 and the second generator 3 progressively heat release to the heat release of agent steam, after Jing second throttle 18 reducing pressure by regulating flow enter vaporizer 6, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 8 was realized in：
(1) in structure, in the dynamic co-feeding system of heat shown in Fig. 3, increase the 3rd generator, the 3rd solution heat exchanger, Absorber 1 is had weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 to connect with generator 2 by second throttle and heater The logical absorber 1 that is adjusted to has weak solution pipeline Jing solution pump 9, solution heat exchanger 11 and the 3rd solution heat exchanger 17 and occurs Device 2 is connected, and generator 2 is had concentrated solution pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 and the second generator 3 connections are adjusted to generator 2 has the 3rd solution heat exchangers 17 of concentrated solution pipeline Jing to connect with the 3rd generator 14, and the 3rd occurs Device 14 has concentrated solution pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 to connect with the second generator 3 again, will send out Raw device 2 has refrigerant steam channel to connect with condenser 4 to be adjusted to generator 2 and have refrigerant steam channel to connect with the 3rd generator 14 3rd generator 14 has cryogen liquid pipeline Jing heaters 19, the second generator 3 and second throttle 18 to connect with vaporizer 6 again afterwards Logical, the 3rd generator 14 also has refrigerant steam channel to connect with condenser 4, and heater 19 also has heated medium passage with outside Connection, the 3rd generator 14 also have high temperature thermal medium passage and ft connection.
(2), in flow process, the refrigerant vapour that high temperature thermal medium and generator 2 are produced is supplied to the 3rd generator 14 to make to drive heat Medium, the weak solution Jing solution pump 9, solution heat exchanger 11 of absorber 1 and the 3rd solution heat exchanger 17 enter generator 2, The 3rd solution heat exchanger 17 of concentrated solution Jing of generator 2 enters the 3rd generator 14, refrigerant vapour and high temperature thermal medium difference The 3rd generator 14, heating are flowed through into the solution release refrigerant vapour in which and is provided to condenser 4, the 3rd generator 14 Concentrated solution Jing solution heat exchanger 11 and the second solution heat exchanger 12 enter the second generator 3；Flow through the 3rd generator 14 Into cryogen liquid, cryogen liquid flows through heater 19 and the second generator 3 progressively heat release for refrigerant vapour heat release, after Jing second section streams 18 reducing pressure by regulating flow of valve enters vaporizer 6, forms the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Fig. 9 was realized in：
(1) in structure, in the dynamic co-feeding system of heat shown in Fig. 3, increase the 3rd generator, the 3rd solution pump, the 3rd molten Absorber 1 is had weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 by liquid heat exchanger, second throttle and heater Connect with generator 2 and be adjusted to absorber 1 and have weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 and the 3rd generator 14 Connection, the 3rd generator 14 have the 3rd solution pumps 16 of concentrated solution pipeline Jing and the 3rd solution heat exchanger 17 to connect with generator 2 again It is logical, there are concentrated solution pipeline Jing solution heat exchangers 11 and the second solution heat exchanger 12 to connect with the second generator 3 in generator 2 Being adjusted to generator 2 has the 3rd solution heat exchangers 17 of concentrated solution pipeline Jing, solution heat exchanger 11 and the second solution heat exchange Device 12 is connected with the second generator 3, is had refrigerant steam channel to connect with condenser 4 in generator 2 and is adjusted to generator 2 and has cryogen After steam channel is connected with the 3rd generator 14, the 3rd generator 14 has cryogen liquid pipeline Jing heaters 19, the second generator again 3 and second throttle 18 connect with vaporizer 6, the 3rd generator 14 also has refrigerant steam channel to connect with condenser 4, heater 19 also have heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 is produced is supplied to the 3rd generator 14 to make driving thermal medium, absorber 1 Weak solution Jing solution pump 9 and solution heat exchanger 11 enter the 3rd generator 14, refrigerant vapour flow through the 3rd generator 14, plus The solution that heat is entered in which discharges refrigerant vapour and provides to condenser 4, the 3rd solution pump of concentrated solution Jing of the 3rd generator 14 16 and the 3rd solution heat exchanger 17 enter generator 2, the 3rd solution heat exchanger 17, solution of the concentrated solution Jing heat of generator 2 Exchanger 11 and the second solution heat exchanger 12 enter the second generator 3；Flow through the refrigerant vapour heat release of the 3rd generator 14 into Cryogen liquid, cryogen liquid flow through heater 19 and the second generator 3 progressively heat release, after 18 reducing pressure by regulating flow of Jing second throttle enter Enter vaporizer 6, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 10 was realized in：
(1), in structure, in the dynamic co-feeding system of heat shown in Fig. 3, the 3rd generator, the second absorber and the 3rd are increased molten Absorber 1 is had weak solution pipeline Jing solution pump 9 and solution heat exchanger 11 to connect with generator 2 and be adjusted to by liquid heat exchanger Absorber 1 has the 3rd solution heat exchangers 17 of weak solution pipeline Jing to connect with the second absorber 15, and the second absorber 15 has dilute again Solution line Jing solution pump 9 and solution heat exchanger 11 are connected with generator 2, and the second generator 3 is had concentrated solution pipeline Jing Two solution pumps 10 and the second solution heat exchanger 12 are connected with absorber 1 and are adjusted to the second generator 3 and have concentrated solution pipeline Jing Two solution heat exchangers 12 are connected with the 3rd generator 14, and the 3rd generator 14 has 10 He of concentrated solution pipeline the second solution of Jing pump again 3rd solution heat exchanger 17 is connected with absorber 1, after having cryogen liquid pipeline to connect with the second generator 3 condenser 4 Two generators 3 have cryogen liquid pipeline warp knuckle stream valve 7 to connect with vaporizer 6 to be adjusted to condenser 4 and have cryogen liquid pipeline Jing second again After generator 3 is connected with the 3rd generator 14, the 3rd generator 14 has cryogen liquid pipeline warp knuckle stream valve 7 to connect with vaporizer 6 again Logical, after having exhaust passage to connect with the second generator 3 in engine 13, the second generator 3 has condensed fluid passage to connect with outside again It is logical to be adjusted to the second generator 3 after engine 13 has the 3rd generators 14 of exhaust passage Jing to connect with the second generator 3 and have again Condensed fluid passage and ft connection, the 3rd generator 14 also have refrigerant steam channel to connect with the second absorber 15, and second absorbs Device 15 also has coolant guiding channel and ft connection.
(2), in flow process, live steam is divided into three tunnels into after 13 blood pressure lowering work done of engine, and the steam with elevated pressures passes through First steam channel is externally discharged after being supplied to 6 exothermic condensation of vaporizer, is completed a part of steam discharge after blood pressure lowering work done and is carried Supply the 3rd generator 14 and 3 exothermic condensation of the second generator and externally discharge, complete another part row after blood pressure lowering work done Vapour is externally discharged；The cryogen liquid of condenser 4 flows through the second generator 3 and the 3rd generator 14 progressively heat release, afterwards warp knuckle stream 7 reducing pressure by regulating flow of valve enters vaporizer 6；The 3rd solution heat exchanger 17 of weak solution Jing of absorber 1 enters the second absorber 15, inhales Receive refrigerant vapour and heat release is entered in cooling medium, the weak solution Jing solution pump 9 of the second absorber 15 and solution heat exchanger 11 Generator 2；Second solution heat exchanger of concentrated solution Jing 12 of the second generator 3 enters the 3rd generator 14, heat absorption release cryogen Steam is simultaneously provided to the second absorber 15, the second solution of concentrated solution Jing pump 10 of the 3rd generator 14 and the 3rd solution heat exchanger 17 enter absorber 1, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 11 was realized in：
(1), in structure, in the dynamic co-feeding system of heat shown in Fig. 3, increase preheater, the second condenser 5 is had into cryogen liquid Pipeline Jing cryogens liquid pump 8 is connected with vaporizer 6 and is adjusted to the second condenser 5 and has cryogen liquid pipeline Jing cryogens liquid pump 8 and preheater 20 are connected with vaporizer 6, and having condensed fluid passage to be adjusted to the second generator 3 with ft connection in the second generator 3 has condensed fluid The preheated device 20 of passage and ft connection.
(2), in flow process, the cryogen liquid of the second condenser 5 flows through cryogen liquid pump 8 and boosts, and flows through preheater 15 and absorbs heat, it Vaporizer 6 is entered afterwards；The part steam discharge of engine 13 flows through 3 heat release of the second generator and condenses, and condensed fluid flows through preheater 20 And heat release, externally discharge afterwards, form the dynamic co-feeding system of heat.
What the dynamic co-feeding system of heat shown in Figure 12 was realized in：
In the dynamic co-feeding system of heat shown in Fig. 3, cancel generator 2 and the high temperature thermal medium passage for connecting, engine 13 Setting up generator 2 after high-temperature steam passage is connected with generator 2 has high temperature condensed fluid passage and ft connection again；Engine 13 High temperature driven thermic load is provided by high-temperature steam passage to generator 2 respectively, provided to vaporizer 6 by the first steam channel Low temperature thermic load and low temperature thermic load is provided by exhaust passage to the second generator 3, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of effect that the technology of the present invention can be realized heat proposed by the invention, have the effect that and Advantage：
(1) high-grade steam elder generation work done, low-grade steam are used for heat supply, meet heat energy efficient utilization principle.
(2) by engine steam discharge, the first steam and the second steam channel, individually or respectively to vaporizer and the second generator Low temperature thermic load is provided, and combines the second generator and the second condenser, realize that Steam Power Equipment end steam discharge or low pressure are taken out The effectively utilizes of the temperature difference between vapour and cold environment.
(3) release the application of cleaning or high efficient energy sources in the dynamic co-feeding system of traditional heat to limit.
(4) with engine end steam as the dynamic alliance low-temperature heat source of heat, be conducive to improving the thermal efficiency and equipment of engine The safety of operation.
(5) type of the dynamic co-feeding system of heat is enriched, the range of application of absorption heat pump is extended, is conducive to preferably adopting Heat utilization rate is improved with absorption heat pump technology.

Claims (21)

1. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are constituted； Absorber (1) has weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) to connect with generator (2), and generator (2) is also There are concentrated solution pipeline Jing solution heat exchangers (11) and the second solution heat exchanger (12) to connect with the second generator (3), second Generator (3) also has concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) to connect with absorber (1), Generator (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant steam channel and second Condenser (5) is connected, and after condenser (4) also has cryogen liquid pipeline to connect with the second generator (3), the second generator (3) has again Cryogen liquid pipeline warp knuckle stream valve (7) is connected with vaporizer (6), and the second condenser (5) also has cryogen liquid pipeline Jing cryogen liquid pumps (8) Connect with vaporizer (6), vaporizer (6) also has refrigerant steam channel to connect with absorber (1), and engine (13) has live steam passage With ft connection, engine (13) or also exhaust passage and ft connection, engine (13) also have exhaust passage to be sequentially communicated After vaporizer (6) and the second generator (3), the second generator (3) has condensed fluid passage and ft connection again, absorber (1) and Condenser (4) also has heated medium passage and ft connection respectively, and the second condenser (5) also has coolant guiding channel with outside Connection, generator (2) also have high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
2. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are constituted； Absorber (1) has weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) to connect with generator (2), and generator (2) is also There are concentrated solution pipeline Jing solution heat exchangers (11) and the second solution heat exchanger (12) to connect with the second generator (3), second Generator (3) also has concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) to connect with absorber (1), Generator (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant steam channel and second Condenser (5) is connected, and after condenser (4) also has cryogen liquid pipeline to connect with the second generator (3), the second generator (3) has again Cryogen liquid pipeline warp knuckle stream valve (7) is connected with vaporizer (6), and the second condenser (5) also has cryogen liquid pipeline Jing cryogen liquid pumps (8) Connect with vaporizer (6), vaporizer (6) also has refrigerant steam channel to connect with absorber (1), and engine (13) has live steam respectively Passage and ft connection and there are exhaust passage and ft connection, engine (13) also the first steam channel is sequentially communicated vaporizer (6) the second generator (3) has the first condensed fluid passage and ft connection again after and the second generator (3), absorber (1) and cold Condenser (4) also has heated medium passage and ft connection respectively, and the second condenser (5) also has coolant guiding channel to connect with outside Logical, generator (2) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
3. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are constituted； Absorber (1) has weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) to connect with generator (2), and generator (2) is also There are concentrated solution pipeline Jing solution heat exchangers (11) and the second solution heat exchanger (12) to connect with the second generator (3), second Generator (3) also has concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) to connect with absorber (1), Generator (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant steam channel and second Condenser (5) is connected, and after condenser (4) also has cryogen liquid pipeline to connect with the second generator (3), the second generator (3) has again Cryogen liquid pipeline warp knuckle stream valve (7) is connected with vaporizer (6), and the second condenser (5) also has cryogen liquid pipeline Jing cryogen liquid pumps (8) Connect with vaporizer (6), vaporizer (6) also has refrigerant steam channel to connect with absorber (1), and engine (13) has live steam passage With ft connection, engine (13) or also exhaust passage and ft connection, engine (13) also have exhaust passage and second After raw device (3) connection, the second generator (3) has condensed fluid passage and ft connection again, and engine (13) also has the first steam to lead to The finisher (6) that road is connected with vaporizer (6) has the first condensed fluid passage and ft connection, absorber (1) and condenser again (4) also there are heated medium passage and ft connection respectively, the second condenser (5) also has coolant guiding channel and ft connection, Generator (2) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
4. heat moves co-feeding system, mainly by absorber, generator, the second generator, condenser, the second condenser, vaporizer, section Stream valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are constituted； Absorber (1) has weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) to connect with generator (2), and generator (2) is also There are concentrated solution pipeline Jing solution heat exchangers (11) and the second solution heat exchanger (12) to connect with the second generator (3), second Generator (3) also has concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) to connect with absorber (1), Generator (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant steam channel and second Condenser (5) is connected, and after condenser (4) also has cryogen liquid pipeline to connect with the second generator (3), the second generator (3) has again Cryogen liquid pipeline warp knuckle stream valve (7) is connected with vaporizer (6), and the second condenser (5) also has cryogen liquid pipeline Jing cryogen liquid pumps (8) Connect with vaporizer (6), vaporizer (6) also has refrigerant steam channel to connect with absorber (1), and engine (13) has live steam respectively Passage and ft connection and there are exhaust passage and ft connection, engine (13) also the first steam channel and the second generator (3) after connecting, the second generator (3) has the first condensed fluid passage and ft connection again, and engine (13) also has the second steam to lead to The finisher (6) that road is connected with vaporizer (6) has the second condensed fluid passage and ft connection, absorber (1) and condenser again (4) also there are heated medium passage and ft connection respectively, the second condenser (5) also has coolant guiding channel and ft connection, Generator (2) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in claim 1-4, increase the 3rd generator, the Absorber (1) is had weak solution pipeline Jing solution pumps (9) and molten by two absorbers, the 3rd solution pump and the 3rd solution heat exchanger Liquid heat exchanger (11) connect with generator (2) be adjusted to absorber (1) have weak solution pipeline Jing solution pumps (9) and solution heat hand over Parallel operation (11) is connected with the second absorber (15), and the second absorber (15) has the 3rd solution pumps (16) of weak solution pipeline Jing and again Three solution heat exchangers (17) are connected with generator (2), by generator (2) have concentrated solution pipeline Jing solution heat exchangers (11) and Second solution heat exchanger (12) is connected with the second generator (3) and is adjusted to generator (2) and has the 3rd solution of concentrated solution pipeline Jing Heat exchanger (17) is connected with the 3rd generator (14), and the 3rd generator (14) has concentrated solution pipeline Jing solution heat exchangers again (11) and the second solution heat exchanger (12) is connected with the second generator (3), and the 3rd generator (14) also has refrigerant steam channel Connect with the second absorber (15), the 3rd generator (14) also has high temperature thermal medium passage and ft connection, the second absorber (15) there are heated medium passage and ft connection, form the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in claim 1-4, increase the 3rd generator, the Generator (2) is had refrigerant steam channel with condenser (4) even by two absorbers, the 3rd solution pump and the 3rd solution heat exchanger It is logical to be adjusted to generator (2) and have refrigerant steam channel to connect with the second absorber (15), the second absorber (15) also weak solution The 3rd solution pumps (16) of pipeline Jing and the 3rd solution heat exchanger (17) are connected with the 3rd generator (14), the 3rd generator (14) Also the 3rd solution heat exchangers (17) of concentrated solution pipeline Jing are connected with the second absorber (15), and the 3rd generator (14) is also cold Agent steam channel is connected with condenser (4), and the 3rd generator (14) also has high temperature thermal medium passage and ft connection, and second absorbs Device (15) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is, in the dynamic co-feeding system of any hot described in claim 1-6, to cancel choke valve, by second Generator (3) has cryogen liquid pipeline warp knuckle stream valve (7) to connect with vaporizer (6) to be adjusted to the second generator (3) and have cryogen liquid pipe Road is connected with vaporizer (6), forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in claim 1-4, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger, second throttle and heater, it is molten that absorber (1) sets up weak solution pipeline Jing the 3rd Liquid pump (16) and the 3rd solution heat exchanger (17) are connected with the 3rd generator (14), and the 3rd generator (14) also has concentrated solution pipe Tri- solution heat exchangers of Lu Jing (17) and the second solution heat exchanger (12) are connected with the second generator (3), by generator (2) There is refrigerant steam channel to connect with condenser (4) to be adjusted to generator (2) and have refrigerant steam channel and the 3rd generator (14) even After logical, the 3rd generator (14) has cryogen liquid pipeline Jing heaters (19), the second generator (3) and second throttle (18) again Connect with vaporizer (6), the 3rd generator (14) also has refrigerant steam channel to connect with condenser (4), and heater (19) also has Heated medium passage and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in claim 1-4, increase the 3rd generator, the Absorber (1) is had weak solution pipeline Jing solution pumps (9) and solution heat by three solution heat exchangers, second throttle and heater Exchanger (11) is connected with generator (2) and is adjusted to absorber (1) and has weak solution pipeline Jing solution pumps (9), solution heat exchanger (11) connect with generator (2) with the 3rd solution heat exchanger (17), generator (2) there are are into concentrated solution pipeline Jing solution heat exchanges Device (11) and the second solution heat exchanger (12) are connected with the second generator (3) and are adjusted to generator (2) and have concentrated solution pipeline Jing 3rd solution heat exchanger (17) is connected with the 3rd generator (14), and the 3rd generator (14) has concentrated solution pipeline Jing solution heat again Exchanger (11) and the second solution heat exchanger (12) are connected with the second generator (3), and generator (2) is had refrigerant steam channel Connect with condenser (4) and be adjusted to the 3rd generation after generator (2) has refrigerant steam channel to connect with the 3rd generator (14) Device (14) has cryogen liquid pipeline Jing heaters (19), the second generator (3) and second throttle (18) with vaporizer (6) even again Logical, the 3rd generator (14) also has refrigerant steam channel to connect with condenser (4), and heater (19) also has heated medium passage With ft connection, the dynamic co-feeding system of heat is formed.
10. the dynamic co-feeding system of heat, be in the dynamic co-feeding system of any hot described in claim 1-4, increase the 3rd generator, the Absorber (1) is had weak solution pipeline Jing solution pumps by three solution pumps, the 3rd solution heat exchanger, second throttle and heater (9) and solution heat exchanger (11) connect with generator (2) be adjusted to absorber (1) have weak solution pipeline Jing solution pumps (9) and Solution heat exchanger (11) is connected with the 3rd generator (14), and the 3rd generator (14) has the 3rd solution pumps of concentrated solution pipeline Jing again (16) connect with generator (2) with the 3rd solution heat exchanger (17), generator (2) there are are into concentrated solution pipeline Jing solution heat exchanges Device (11) and the second solution heat exchanger (12) are connected with the second generator (3) and are adjusted to generator (2) and have concentrated solution pipeline Jing 3rd solution heat exchanger (17), solution heat exchanger (11) and the second solution heat exchanger (12) are with the second generator (3) even It is logical, there is refrigerant steam channel to connect with condenser (4) in generator (2) and be adjusted to generator (2) and have refrigerant steam channel and the Three generators (14) connection after the 3rd generator (14) have again cryogen liquid pipeline Jing heaters (19), the second generator (3) and Second throttle (18) is connected with vaporizer (6), and the 3rd generator (14) also has refrigerant steam channel to connect with condenser (4), Heater (19) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 11. heat, is that the 3rd generator (14) increases in the dynamic co-feeding system of any hot described in claim 8-10 If high temperature thermal medium passage and ft connection, the dynamic co-feeding system of heat is formed.
The dynamic co-feeding system of 12. heat, is, in the dynamic co-feeding system of any hot described in claim 8-11, to cancel choke valve and second Second generator (3) is had cryogen liquid pipeline warp knuckle stream valve (7) to be connected with vaporizer (6) and is adjusted to the second generator by choke valve (3) have cryogen liquid pipeline to connect with vaporizer (6), by the second generator (3) have cryogen liquid pipeline Jing second throttle (18) with Vaporizer (6) connection is adjusted to the second generator (3) has cryogen liquid pipeline to connect with vaporizer (6), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 13. heat, is, in the dynamic co-feeding system of heat described in claim 1, to increase the 3rd generator, the second absorption Absorber (1) is had weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) and is sent out by device and the 3rd solution heat exchanger Raw device (2) connection is adjusted to absorber (1) the 3rd solution heat exchangers (17) of weak solution pipeline Jing and the second absorber (15) Connection, the second absorber (15) have weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) with generator (2) even again It is logical, the second generator (3) there are into concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) and absorber (1) connection is adjusted to the second generator (3) concentrated solution pipeline the second solution heat exchangers of Jing (12) and the 3rd generator (14) Connection, the 3rd generator (14) have concentrated solution pipeline Jing the second solution pump (10) and the 3rd solution heat exchanger (17) again and absorb Device (1) is connected, and after having cryogen liquid pipeline to connect with the second generator (3) condenser (4), the second generator (3) has cryogen again Liquid pipeline warp knuckle stream valve (7) connect with vaporizer (6) be adjusted to condenser (4) have cryogen liquid pipeline the second generators of Jing (3) with After the connection of 3rd generator (14), the 3rd generator (14) has cryogen liquid pipeline warp knuckle stream valve (7) to connect with vaporizer (6) again, After having exhaust passage to be sequentially communicated vaporizer (6) and the second generator (3) in engine (13), the second generator (3) has cold again Lime set passage and ft connection be adjusted to engine (13) have exhaust passage be sequentially communicated vaporizer (6), the second generator (3) and After 3rd generator (14), the 3rd generator (14) has condensed fluid passage and ft connection again, and the 3rd generator (14) is also cold Agent steam channel is connected with the second absorber (15), and the second absorber (15) also has coolant guiding channel and ft connection, is formed The dynamic co-feeding system of heat.
The dynamic co-feeding system of 14. heat, is, in the dynamic co-feeding system of heat described in claim 2, to increase the 3rd generator, the second absorption Absorber (1) is had weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) and is sent out by device and the 3rd solution heat exchanger Raw device (2) connection is adjusted to absorber (1) the 3rd solution heat exchangers (17) of weak solution pipeline Jing and the second absorber (15) Connection, the second absorber (15) have weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) with generator (2) even again It is logical, the second generator (3) there are into concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) and absorber (1) connection is adjusted to the second generator (3) concentrated solution pipeline the second solution heat exchangers of Jing (12) and the 3rd generator (14) Connection, the 3rd generator (14) have concentrated solution pipeline Jing the second solution pump (10) and the 3rd solution heat exchanger (17) again and absorb Device (1) is connected, and after having cryogen liquid pipeline to connect with the second generator (3) condenser (4), the second generator (3) has cryogen again Liquid pipeline warp knuckle stream valve (7) connect with vaporizer (6) be adjusted to condenser (4) have cryogen liquid pipeline the second generators of Jing (3) with After the connection of 3rd generator (14), the 3rd generator (14) has cryogen liquid pipeline warp knuckle stream valve (7) to connect with vaporizer (6) again, After having the first steam channel to be sequentially communicated vaporizer (6) and the second generator (3) in engine (13), the second generator (3) is again Have the first condensed fluid passage and ft connection be adjusted to engine (13) have the first steam channel be sequentially communicated vaporizer (6), the After two generators (3) and the 3rd generator (14), the 3rd generator (14) has the first condensed fluid passage and ft connection again, the Three generators (14) also have refrigerant steam channel to connect with the second absorber (15), and the second absorber (15) also has cooling medium to lead to Road and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, is, in the dynamic co-feeding system of heat described in claim 3, to increase the 3rd generator, the second absorption Absorber (1) is had weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) and is sent out by device and the 3rd solution heat exchanger Raw device (2) connection is adjusted to absorber (1) the 3rd solution heat exchangers (17) of weak solution pipeline Jing and the second absorber (15) Connection, the second absorber (15) have weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) with generator (2) even again It is logical, the second generator (3) there are into concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) and absorber (1) connection is adjusted to the second generator (3) concentrated solution pipeline the second solution heat exchangers of Jing (12) and the 3rd generator (14) Connection, the 3rd generator (14) have concentrated solution pipeline Jing the second solution pump (10) and the 3rd solution heat exchanger (17) again and absorb Device (1) is connected, and after having cryogen liquid pipeline to connect with the second generator (3) condenser (4), the second generator (3) has cryogen again Liquid pipeline warp knuckle stream valve (7) connect with vaporizer (6) be adjusted to condenser (4) have cryogen liquid pipeline the second generators of Jing (3) with After the connection of 3rd generator (14), the 3rd generator (14) has cryogen liquid pipeline warp knuckle stream valve (7) to connect with vaporizer (6) again, After having exhaust passage to connect with the second generator (3) in engine (13) the second generator (3) have again condensed fluid passage with it is outer Portion's connection is adjusted to second after engine (13) has the 3rd generators (14) of exhaust passage Jing to connect with the second generator (3) Raw device (3) has condensed fluid passage and ft connection again, and the 3rd generator (14) also has refrigerant steam channel and the second absorber (15) connect, the second absorber (15) also has coolant guiding channel and ft connection, form the dynamic co-feeding system of heat；Wherein, or will After engine (13) has exhaust passage to connect with the second generator (3), the second generator (3) has condensed fluid passage again with outside Connection is adjusted to the 3rd generation after engine (13) has the second generators of exhaust passage Jing (3) to connect with the 3rd generator (14) Device (14) has condensed fluid passage and ft connection again.
The dynamic co-feeding system of 16. heat, is, in the dynamic co-feeding system of heat described in claim 4, to increase the 3rd generator, the second absorption Absorber (1) is had weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) and is sent out by device and the 3rd solution heat exchanger Raw device (2) connection is adjusted to absorber (1) the 3rd solution heat exchangers (17) of weak solution pipeline Jing and the second absorber (15) Connection, the second absorber (15) have weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) with generator (2) even again It is logical, the second generator (3) there are into concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) and absorber (1) connection is adjusted to the second generator (3) concentrated solution pipeline the second solution heat exchangers of Jing (12) and the 3rd generator (14) Connection, the 3rd generator (14) have concentrated solution pipeline Jing the second solution pump (10) and the 3rd solution heat exchanger (17) again and absorb Device (1) is connected, and after having cryogen liquid pipeline to connect with the second generator (3) condenser (4), the second generator (3) has cryogen again Liquid pipeline warp knuckle stream valve (7) connect with vaporizer (6) be adjusted to condenser (4) have cryogen liquid pipeline the second generators of Jing (3) with After the connection of 3rd generator (14), the 3rd generator (14) has cryogen liquid pipeline warp knuckle stream valve (7) to connect with vaporizer (6) again, After having the first steam channel to connect with the second generator (3) in engine (13), the second generator (3) has the first condensed fluid again Passage is adjusted to engine (13) with ft connection has the 3rd generators (14) of the first steam channel Jing with the second generator (3) even After logical, the second generator (3) has the first condensed fluid passage and ft connection again, and the 3rd generator (14) also has refrigerant vapour to lead to Road is connected with the second absorber (15), and the second absorber (15) also has coolant guiding channel and ft connection, forms the dynamic alliance of heat System；Wherein, after or having the first steam channel to connect with the second generator (3) in engine (13), the second generator (3) is again Having the first condensed fluid passage to be adjusted to engine (13) with ft connection has the first the second generators of steam channel Jing (3) and the 3rd After generator (14) connection, the 3rd generator (14) has the first condensed fluid passage and ft connection again.
The dynamic co-feeding system of 17. heat, is, in the dynamic co-feeding system of heat described in claim 4, to increase the 3rd generator, the second absorption Absorber (1) is had weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) and is sent out by device and the 3rd solution heat exchanger Raw device (2) connection is adjusted to absorber (1) the 3rd solution heat exchangers (17) of weak solution pipeline Jing and the second absorber (15) Connection, the second absorber (15) have weak solution pipeline Jing solution pumps (9) and solution heat exchanger (11) with generator (2) even again It is logical, the second generator (3) there are into concentrated solution pipeline Jing the second solution pump (10) and the second solution heat exchanger (12) and absorber (1) connection is adjusted to the second generator (3) concentrated solution pipeline the second solution heat exchangers of Jing (12) and the 3rd generator (14) Connection, the 3rd generator (14) have concentrated solution pipeline Jing the second solution pump (10) and the 3rd solution heat exchanger (17) again and absorb Device (1) is connected, and after having cryogen liquid pipeline to connect with the second generator (3) condenser (4), the second generator (3) has cryogen again Liquid pipeline warp knuckle stream valve (7) connect with vaporizer (6) be adjusted to condenser (4) have cryogen liquid pipeline the second generators of Jing (3) with After the connection of 3rd generator (14), the 3rd generator (14) has cryogen liquid pipeline warp knuckle stream valve (7) to connect with vaporizer (6) again, Having exhaust passage to be adjusted to engine (13) with ft connection in engine (13) has exhaust passage and the 3rd generator (14) even After logical, the 3rd generator (14) has condensed fluid passage and ft connection again, the 3rd generator (14) also have refrigerant steam channel with Second absorber (15) is connected, and the second absorber (15) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat； Wherein, or engine (13) is set up the 3rd generator (14) after exhaust passage is connected with the 3rd generator (14) and has condensed fluid again Passage and ft connection.
The dynamic co-feeding systems of 18. heat, are, in the dynamic co-feeding system of any hot described in claim 13-17, to cancel choke valve, by the Three generators (14) have cryogen liquid pipeline warp knuckle stream valve (7) to connect with vaporizer (6) to be adjusted to the 3rd generator (14) and have cryogen Liquid pipeline is connected with vaporizer (6), forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 19. heat, is, in the dynamic co-feeding system of heat described in claim 3, to increase preheater, by the second condenser (5) there is cryogen liquid pipeline Jing cryogen liquid pumps (8) to connect with vaporizer (6) to be adjusted to the second condenser (5) and have cryogen liquid pipeline Jing Cryogen liquid pump (8) and preheater (20) are connected with vaporizer (6), and the second generator (3) is had condensed fluid passage and ft connection Being adjusted to the second generator (3) has the preheated device of condensed fluid passage (20) and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 20. heat, be in the dynamic co-feeding system of any hot described in claim 1-19, cancel generator (2) with The high temperature thermal medium passage of connection, engine (13) set up after high-temperature steam passage is connected with generator (2) generator (2) again There are high temperature condensed fluid passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 21. heat, are, in the dynamic co-feeding system of any hot described in claim 5-6, to cancel generator (2) and the Three generators (14) high temperature thermal medium passage respectively with ft connection, engine (13) are set up high-temperature steam passage and are sequentially communicated After generator (2) and the 3rd generator (14), the 3rd generator (14) has high temperature condensed fluid passage and ft connection again, is formed The dynamic co-feeding system of heat.
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CN104654658A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104748439A (en) * 2014-01-27 2015-07-01 李华玉 Heat and power combined supplying system
CN104864623A (en) * 2014-01-27 2015-08-26 李华玉 Thermodynamic combined supply system

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104654652A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104654653A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104654658A (en) * 2014-01-27 2015-05-27 李华玉 Combined thermal dynamic system
CN104748439A (en) * 2014-01-27 2015-07-01 李华玉 Heat and power combined supplying system
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