CN106440470A - Combined heating and power system - Google Patents

Combined heating and power system Download PDF

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Publication number
CN106440470A
CN106440470A CN201610822197.6A CN201610822197A CN106440470A CN 106440470 A CN106440470 A CN 106440470A CN 201610822197 A CN201610822197 A CN 201610822197A CN 106440470 A CN106440470 A CN 106440470A
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China
Prior art keywords
generator
solution
absorber
heat exchanger
connect
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CN201610822197.6A
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Chinese (zh)
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CN106440470B (en
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李华玉
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Classifications

    • 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)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

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

Description

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

Claims (22)

1. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, vaporizer, cold Agent liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) concentrated solution pipeline is had to connect with the second generator (2) with solution heat exchanger (10) through solution pump (8), the second generator (2) Concentrated solution pipeline is also had to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline warp Second solution pump (9) is connected with the second absorber (4) with the second solution heat exchanger (11), and the second absorber (4) also has dilute molten Liquid pipeline is connected with generator (1) through solution heat exchanger (10), and generator (1) also has refrigerant steam channel and condenser (5) Connection, the second generator (2) also has refrigerant steam channel to connect with the second absorber (4), and condenser (5) also has cryogen liquid pipeline Connect with vaporizer (6) through cryogen liquid pump (7), vaporizer (6) also has refrigerant steam channel to connect with absorber (3), engine (12) there are live steam passage and ft connection, engine (12) or also exhaust passage and ft connection, engine (12) also has to be arranged After vapour passage is sequentially communicated vaporizer (6) and generator (1), generator (1) has condensed fluid passage and ft connection again, and second Generator (2) goes back high temperature thermal medium passage and ft connection, and absorber (3) and the second absorber (4) also have heated Jie respectively Matter passage and ft connection, condenser (5) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, vaporizer, cold Agent liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) concentrated solution pipeline is had to connect with the second generator (2) with solution heat exchanger (10) through solution pump (8), the second generator (2) Concentrated solution pipeline is also had to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline warp Second solution pump (9) is connected with the second absorber (4) with the second solution heat exchanger (11), and the second absorber (4) also has dilute molten Liquid pipeline is connected with generator (1) through solution heat exchanger (10), and generator (1) also has refrigerant steam channel and condenser (5) Connection, the second generator (2) also has refrigerant steam channel to connect with the second absorber (4), and condenser (5) also has cryogen liquid pipeline Connect with vaporizer (6) through cryogen liquid pump (7), vaporizer (6) also has refrigerant steam channel to connect with absorber (3), engine (12) there are live steam passage and ft connection respectively and have exhaust passage and ft connection, engine (12) also has the first steam channel After being sequentially communicated vaporizer (6) and generator (1), generator (1) has the first condensed fluid passage and ft connection again, second Raw device (2) goes back high temperature thermal medium passage and ft connection, and absorber (3) and the second absorber (4) also have heated medium respectively Passage and ft connection, condenser (5) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, vaporizer, cold Agent liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) concentrated solution pipeline is had to connect with the second generator (2) with solution heat exchanger (10) through solution pump (8), the second generator (2) Concentrated solution pipeline is also had to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline warp Second solution pump (9) is connected with the second absorber (4) with the second solution heat exchanger (11), and the second absorber (4) also has dilute molten Liquid pipeline is connected with generator (1) through solution heat exchanger (10), and generator (1) also has refrigerant steam channel and condenser (5) Connection, the second generator (2) also has refrigerant steam channel to connect with the second absorber (4), and condenser (5) also has cryogen liquid pipeline Connect with vaporizer (6) through cryogen liquid pump (7), vaporizer (6) also has refrigerant steam channel to connect with absorber (3), engine (12) there are live steam passage and ft connection, engine (12) or also exhaust passage and ft connection, engine (12) also has to be arranged After vapour passage is connected with generator (1), generator (1) has condensed fluid passage and ft connection again, and engine (12) also has first The finisher (6) that steam channel is connected with vaporizer (6) has the first condensed fluid passage and ft connection, the second generator again (2) high temperature thermal medium passage and ft connection are gone back, absorber (3) and the second absorber (4) also have heated medium passage respectively With ft connection, condenser (5) also coolant guiding channel and ft connection, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by generator, the second generator, absorber, the second absorber, condenser, vaporizer, cold Agent liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Generator (1) concentrated solution pipeline is had to connect with the second generator (2) with solution heat exchanger (10) through solution pump (8), the second generator (2) Concentrated solution pipeline is also had to connect with absorber (3) through the second solution heat exchanger (11), absorber (3) also has weak solution pipeline warp Second solution pump (9) is connected with the second absorber (4) with the second solution heat exchanger (11), and the second absorber (4) also has dilute molten Liquid pipeline is connected with generator (1) through solution heat exchanger (10), and generator (1) also has refrigerant steam channel and condenser (5) Connection, the second generator (2) also has refrigerant steam channel to connect with the second absorber (4), and condenser (5) also has cryogen liquid pipeline Connect with vaporizer (6) through cryogen liquid pump (7), vaporizer (6) also has refrigerant steam channel to connect with absorber (3), engine (12) there are live steam passage and ft connection respectively and have exhaust passage and ft connection, engine (12) also has the first steam channel After connecting with generator (1), generator (1) has the first condensed fluid passage and ft connection again, and engine (12) also has the second steaming The finisher (6) that vapour passage is connected with vaporizer (6) has the second condensed fluid passage and ft connection, the second generator (2) again Also high temperature thermal medium passage and ft connection, absorber (3) and the second absorber (4) also have heated medium passage respectively with outward Portion connects, and condenser (5) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and choke valve, generator (1) sets up concentrated solution pipeline through the 3rd solution pump (14), molten Liquid heat exchanger (10) is connected with the 3rd generator (13) with the 3rd solution heat exchanger (15), and the 3rd generator (13) is also dense Solution line is connected with absorber (3) through the 3rd solution heat exchanger (15), by the second generator (2) have refrigerant steam channel with Second absorber (4) connection is adjusted to after the second generator (2) has refrigerant steam channel to connect with the 3rd generator (13) the Three generators (13) have cryogen liquid pipeline to connect with vaporizer (6) through choke valve (16) again, and the 3rd generator (13) also has cryogen Steam channel is connected with the second absorber (4), forms the dynamic co-feeding system of heat.
6. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers and choke valve, by generator (1) have concentrated solution pipeline through solution pump (8) and solution heat exchanger (10) with Second generator (2) connection is adjusted to generator (1) has concentrated solution pipeline through solution pump (8), solution heat exchanger (10) and the Three solution heat exchangers (15) are connected with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the second solution heat Exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the 3rd solution heat exchanger (15) connect with the 3rd generator (13), the 3rd generator (13) have again concentrated solution pipeline through the second solution heat exchanger (11) with Absorber (3) connects, and the second generator (2) is had refrigerant steam channel to connect with the second absorber (4) and is adjusted to the second generation After device (2) has refrigerant steam channel to connect with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again through throttling Valve (16) is connected with vaporizer (6), and the 3rd generator (13) also has refrigerant steam channel to connect with the second absorber (4), is formed The dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger and choke valve, generator (1) is had concentrated solution pipeline through solution pump (8) and solution heat Exchanger (10) connect with the second generator (2) be adjusted to generator (1) have concentrated solution pipeline through solution pump (8) and solution heat hand over Parallel operation (10) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the 3rd solution pump (14) and Three solution heat exchangers (15) are connected with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the second solution heat Exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the 3rd solution heat exchanger (15) with the second solution heat exchanger (11) is connected with absorber (3), and the second generator (2) is had refrigerant steam channel and second Absorber (4) connection is adjusted to the 3rd after the second generator (2) has refrigerant steam channel to connect with the 3rd generator (13) Raw device (13) has cryogen liquid pipeline to connect with vaporizer (6) through choke valve (16) again, and the 3rd generator (13) also has refrigerant vapour Passage is connected with the second absorber (4), forms the dynamic co-feeding system of heat.
8. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger, choke valve and heater, generator (1) sets up concentrated solution pipeline through the 3rd solution pump (14), solution heat exchanger (10) is connected with the 3rd generator (13) with the 3rd solution heat exchanger (15), the 3rd generator (13) also have concentrated solution pipeline to connect with absorber (3) through the 3rd solution heat exchanger (15), the second generator (2) is had cryogen Steam channel is connected with the second absorber (4) and is adjusted to the second generator (2) and has refrigerant steam channel and the 3rd generator (13) After connection, the 3rd generator (13) has cryogen liquid pipeline again through heater (17), generator (1) and choke valve (16) and evaporation Device (6) connects, and the 3rd generator (13) also has refrigerant steam channel to connect with the second absorber (4), and heater (17) also has quilt Heating medium passage and ft connection, form the dynamic co-feeding system of heat.
9. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution heat exchangers, choke valve and heater, generator (1) is had concentrated solution pipeline through solution pump (8) and solution heat exchange Device (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through solution pump (8), solution heat exchanger (10) connect with the second generator (2) with the 3rd solution heat exchanger (15), the second generator (2) is had concentrated solution pipeline through Two solution heat exchangers (11) connect with absorber (3) be adjusted to the second generator (2) have concentrated solution pipeline through the 3rd solution heat Exchanger (15) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution heat exchanger (11) connect with absorber (3), the second generator (2) is had refrigerant steam channel to connect with the second absorber (4) and is adjusted to After two generators (2) have refrigerant steam channel to connect with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again Connect with vaporizer (6) with choke valve (16) through heater (17), generator (1), the 3rd generator (13) also has refrigerant vapour Passage is connected with the second absorber (4), and heater (17) also has heated medium passage and ft connection, forms the dynamic alliance system of heat System.
10. the dynamic co-feeding system of heat, is that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three solution pumps, the 3rd solution heat exchanger, choke valve and heater, generator (1) is had concentrated solution pipeline through solution pump (8) and Solution heat exchanger (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through solution pump (8) and molten Liquid heat exchanger (10) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the 3rd solution pump (14) connect with the second generator (2) with the 3rd solution heat exchanger (15), the second generator (2) is had concentrated solution pipeline through Two solution heat exchangers (11) connect with absorber (3) be adjusted to the second generator (2) have concentrated solution pipeline through the 3rd solution heat Exchanger (15) is connected with absorber (3) with the second solution heat exchanger (11), and the second generator (2) is had refrigerant steam channel Connect with the second absorber (4) and be adjusted to after the second generator (2) has refrigerant steam channel to connect with the 3rd generator (13) 3rd generator (13) has cryogen liquid pipeline through heater (17), generator (1) and choke valve (16) with vaporizer (6) even again Logical, the 3rd generator (13) also has refrigerant steam channel to connect with the second absorber (4), and heater (17) also has heated medium Passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 11. heat, are that any hot described in claim 8-10 moves in co-feeding system, cancel choke valve, by the Three generators (13) have cryogen liquid pipeline to connect adjustment with choke valve (16) with vaporizer (6) through heater (17), generator (1) There is cryogen liquid pipeline to connect with vaporizer (6) with generator (1) through heater (17) for the 3rd generator (13), form the dynamic connection of heat For system.
The dynamic co-feeding system of 12. heat, is that any hot described in claim 5-11 moves in co-feeding system, the 3rd generator (13) increases If high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 13. heat, are that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, the second generator (2) is had refrigerant steam channel and the second absorption Device (4) connection is adjusted to the second generator (2) has refrigerant steam channel to connect with the 3rd absorber (18), the 3rd absorber (18) Weak solution pipeline is also had to connect with the 3rd generator (13) with the 3rd solution heat exchanger (15) through the 3rd solution pump (14), the 3rd Generator (13) also has concentrated solution pipeline to connect with the 3rd absorber (18) through the 3rd solution heat exchanger (15), the 3rd generator (13) refrigerant steam channel is also had to connect with the second absorber (4), the 3rd generator (13) also has high temperature thermal medium passage with outward Portion connects, and the 3rd absorber (18) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 14. heat, are that any hot described in claim 1-4 moves in co-feeding system, increase the 3rd generator, the Three absorbers, the 3rd solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline through solution pump (8) and molten Liquid heat exchanger (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through solution pump (8) and solution Heat exchanger (10) is connected with the 3rd absorber (18), and the 3rd absorber (18) has weak solution pipeline again through the 3rd solution pump (14) Connect with the second generator (2) with the 3rd solution heat exchanger (15), the second generator (2) is had concentrated solution pipeline molten through second Liquid heat exchanger (11) is connected with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the 3rd solution heat exchange Device (15) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution heat exchanger (11) Connect with absorber (3), the 3rd generator (13) also has refrigerant steam channel to connect with the 3rd absorber (18), the 3rd generator (13) also have high temperature thermal medium passage and ft connection, the 3rd absorber (18) also has heated medium passage and ft connection, Form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 15. heat, is that the heat described in claim 1 is moved in co-feeding system, increases the 3rd generator, the 3rd absorption Device, the 3rd solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline to hand over through solution pump (8) and solution heat Parallel operation (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through the 3rd solution heat exchanger (15) Connect with the 3rd generator (13), the 3rd generator (13) has concentrated solution pipeline again through solution pump (8) and solution heat exchanger (10) connect with the second generator (2), the second absorber (4) is had weak solution pipeline through solution heat exchanger (10) and generator (1) connection is adjusted to the second absorber (4) has weak solution pipeline to connect with the 3rd absorber (18) through solution heat exchanger (10), 3rd absorber (18) has weak solution pipeline again through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) and generator (1) Connection, after engine (12) is had exhaust passage to be sequentially communicated vaporizer (6) and generator (1), generator (1) has condensation again Liquid passage and ft connection are adjusted to engine (12) has exhaust passage to be sequentially communicated vaporizer (6), generator (1) and the 3rd After raw device (13), the 3rd generator (13) has condensed fluid passage and ft connection again, and the 3rd generator (13) also has refrigerant vapour Passage is connected with the 3rd absorber (18), and the 3rd absorber (18) also has coolant guiding channel and ft connection, forms the dynamic connection of heat For system.
The dynamic co-feeding system of 16. heat, is that the heat described in claim 2 is moved in co-feeding system, increases the 3rd generator, the 3rd absorption Device, the 3rd solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline to hand over through solution pump (8) and solution heat Parallel operation (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through the 3rd solution heat exchanger (15) Connect with the 3rd generator (13), the 3rd generator (13) has concentrated solution pipeline again through solution pump (8) and solution heat exchanger (10) connect with the second generator (2), the second absorber (4) is had weak solution pipeline through solution heat exchanger (10) and generator (1) connection is adjusted to the second absorber (4) has weak solution pipeline to connect with the 3rd absorber (18) through solution heat exchanger (10), 3rd absorber (18) has weak solution pipeline again through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) and generator (1) Connection, after engine (12) is had the first steam channel to be sequentially communicated vaporizer (6) and generator (1), generator (1) has again First condensed fluid passage and ft connection are adjusted to engine (12) has the first steam channel to be sequentially communicated vaporizer (6), occur After device (1) and the 3rd generator (13), the 3rd generator (13) has the first condensed fluid passage and ft connection again, the 3rd generation Device (13) also has refrigerant steam channel to connect with the 3rd absorber (18), and the 3rd absorber (18) also has coolant guiding channel with outward Portion connects, and forms the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is that the heat described in claim 3 is moved in co-feeding system, increases the 3rd generator, the 3rd absorption Device, the 3rd solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline to hand over through solution pump (8) and solution heat Parallel operation (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through the 3rd solution heat exchanger (15) Connect with the 3rd generator (13), the 3rd generator (13) has concentrated solution pipeline again through solution pump (8) and solution heat exchanger (10) connect with the second generator (2), the second absorber (4) is had weak solution pipeline through solution heat exchanger (10) and generator (1) connection is adjusted to the second absorber (4) has weak solution pipeline to connect with the 3rd absorber (18) through solution heat exchanger (10), 3rd absorber (18) has weak solution pipeline again through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) and generator (1) Connection, after engine (12) is had exhaust passage to connect with generator (1), generator (1) has condensed fluid passage and outside to connect again Lead to and be adjusted to the 3rd generator (13) after engine (12) has exhaust passage to connect with the 3rd generator (13) through generator (1) There are condensed fluid passage and ft connection again, the 3rd generator (13) also has refrigerant steam channel to connect with the 3rd absorber (18), 3rd absorber (18) also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or by engine (12) After having exhaust passage to connect with generator (1), generator (1) has condensed fluid passage and ft connection to be adjusted to engine again (12) after having exhaust passage to connect with generator (1) through the 3rd generator (13), generator (1) has condensed fluid passage again with outward Portion connects.
The dynamic co-feeding system of 18. heat, is that the heat described in claim 4 is moved in co-feeding system, increases the 3rd generator, the 3rd absorption Device, the 3rd solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline to hand over through solution pump (8) and solution heat Parallel operation (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through the 3rd solution heat exchanger (15) Connect with the 3rd generator (13), the 3rd generator (13) has concentrated solution pipeline again through solution pump (8) and solution heat exchanger (10) connect with the second generator (2), the second absorber (4) is had weak solution pipeline through solution heat exchanger (10) and generator (1) connection is adjusted to the second absorber (4) has weak solution pipeline to connect with the 3rd absorber (18) through solution heat exchanger (10), 3rd absorber (18) has weak solution pipeline again through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) and generator (1) Connection, after just engine (12) has the first steam channel to connect with generator (1), generator (1) has the first condensed fluid to lead to again Road and ft connection are adjusted to after engine (12) has the first steam channel to connect with the 3rd generator (13) through generator (1) 3rd generator (13) has the first condensed fluid passage and ft connection again, and the 3rd generator (13) also has refrigerant steam channel and the Three absorbers (18) connect, and the 3rd absorber (18) also has coolant guiding channel and ft connection, form the dynamic co-feeding system of heat；Its In, or engine (12) have the first steam channel to connect with generator (1) after generator (1) have again the first condensed fluid passage with Ft connection is adjusted to and occurs after engine (12) has the first steam channel to connect with generator (1) through the 3rd generator (13) Device (1) has the first condensed fluid passage and ft connection again.
The dynamic co-feeding system of 19. heat, is that the heat described in claim 4 is moved in co-feeding system, increases the 3rd generator, the 3rd absorption Device, the 3rd solution pump and the 3rd solution heat exchanger, generator (1) is had concentrated solution pipeline to hand over through solution pump (8) and solution heat Parallel operation (10) is connected with the second generator (2) and is adjusted to generator (1) and has concentrated solution pipeline through the 3rd solution heat exchanger (15) Connect with the 3rd generator (13), the 3rd generator (13) has concentrated solution pipeline again through solution pump (8) and solution heat exchanger (10) connect with the second generator (2), the second absorber (4) is had weak solution pipeline through solution heat exchanger (10) and generator (1) connection is adjusted to the second absorber (4) has weak solution pipeline to connect with the 3rd absorber (18) through solution heat exchanger (10), 3rd absorber (18) has weak solution pipeline again through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) and generator (1) Connection, engine (12) is had exhaust passage and ft connection to be adjusted to engine (12) exhaust passage and the 3rd generator (13) after connecting, the 3rd generator (13) has condensed fluid passage and ft connection again, and the 3rd generator (13) also has refrigerant vapour Passage is connected with the 3rd absorber (18), and the 3rd absorber (18) also has coolant guiding channel and ft connection, forms the dynamic connection of heat For system；Wherein, or engine (12) sets up after exhaust passage is connected the 3rd generator (13) with the 3rd generator (13) again There are condensed fluid passage and ft connection.
The dynamic co-feeding system of 20. heat, is that the heat described in claim 3 is moved in co-feeding system, increases preheater, by condenser (5) There is cryogen liquid pipeline to connect with vaporizer (6) through cryogen liquid pump (7) to be adjusted to condenser (5) and have cryogen liquid pipeline through cryogen liquid pump (7) connect with vaporizer (6) with preheater (19), generator (1) is had condensed fluid passage and ft connection to be adjusted to generator (1) there are the preheated device of condensed fluid passage (19) and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 21. heat, is that any hot described in claim 1-20 moves in co-feeding system, cancels the second generator (2) with the high temperature thermal medium passage connecting, engine (12) is set up after high-temperature steam passage is connected with the second generator (2) Two generators (2) have high temperature condensed fluid passage and ft connection again, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 22. heat, is that any hot described in claim 13-14 moves in co-feeding system, cancels the second generator (2) and the 3rd generator (13) the high temperature thermal medium passage with ft connection respectively, high-temperature steam passage set up by engine (12) After being sequentially communicated the second generator (2) and the 3rd generator (13), the 3rd generator (13) has high temperature condensed fluid passage again with outward Portion connects, and forms 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
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
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

Patent Citations (5)

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