CN106440468A - Combined heating and power system - Google Patents

Combined heating and power system Download PDF

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Publication number
CN106440468A
CN106440468A CN201610822143.XA CN201610822143A CN106440468A CN 106440468 A CN106440468 A CN 106440468A CN 201610822143 A CN201610822143 A CN 201610822143A CN 106440468 A CN106440468 A CN 106440468A
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China
Prior art keywords
generator
solution
absorber
heat exchanger
connection
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Granted
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CN201610822143.XA
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Chinese (zh)
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CN106440468B (en
Inventor
李华玉
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Individual
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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 combined cooling, heating and power and absorption heat pumps. An absorption heat pump cycling system comprises an absorber, a second absorber, a generator, a second generator, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger, a power machine provides low-temperature heat load for the second generator through an exhaust steam channel and provides low-temperature heat load for an evaporator through a first steam channel, the generator communicates with the outside through a high-temperature heat medium channel, the absorber and a condenser communicate with the outside through heated medium channels, the second absorber 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 absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorb Device has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through solution pump Connect with generator with the second solution heat exchanger, generator also has concentrated solution pipeline through the second solution heat exchanger and second Raw device connection, the second generator is also had concentrated solution pipeline to be connected with absorber with solution heat exchanger through the second solution pump, occurs 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, cold Condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, moves Power machine has live steam passage and ft connection, engine or also exhaust passage and ft connection, engine also have exhaust passage according to After secondary connection vaporizer and the second generator, the second generator has condensed fluid passage and ft connection, absorber and condenser again Also there are heated medium passage and ft connection respectively, the second absorber also has coolant guiding channel and ft connection, generator Also have high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorb Device has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through solution pump Connect with generator with the second solution heat exchanger, generator also has concentrated solution pipeline through the second solution heat exchanger and second Raw device connection, the second generator is also had concentrated solution pipeline to be connected with absorber with solution heat exchanger through the second solution pump, occurs 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, cold Condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, moves Power machine has live steam passage and ft connection respectively and has exhaust passage and ft connection, and engine also has the first steam channel successively After connection vaporizer and the second generator, the second generator has the first condensed fluid passage and ft connection, absorber and condensation again Device also has heated medium passage and ft connection respectively, and the second absorber also has coolant guiding channel and ft connection, occurs Device also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorb Device has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through solution pump Connect with generator with the second solution heat exchanger, generator also has concentrated solution pipeline through the second solution heat exchanger and second Raw device connection, the second generator is also had concentrated solution pipeline to be connected with absorber with solution heat exchanger through the second solution pump, occurs 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, cold Condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, moves Power machine has live steam passage and ft connection, engine or also exhaust passage and ft connection, engine also have exhaust passage with Second generator connection after the second generator have condensed fluid passage and ft connection again, engine also have the first steam channel with It is heated that the finisher of vaporizer connection has the first condensed fluid passage and ft connection, absorber and condenser also to have respectively again Medium channel and ft connection, the second absorber also has coolant guiding channel and ft connection, and generator also has high temperature thermal medium Passage and ft connection, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, evaporation Device, choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorb Device has weak solution pipeline to connect with the second absorber through solution heat exchanger, and the second absorber also has weak solution pipeline through solution pump Connect with generator with the second solution heat exchanger, generator also has concentrated solution pipeline through the second solution heat exchanger and second Raw device connection, the second generator is also had concentrated solution pipeline to be connected with absorber with solution heat exchanger through the second solution pump, occurs 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, cold Condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, moves Power machine has live steam passage and ft connection respectively and has exhaust passage and ft connection, and engine also has the first steam channel and the After two generator connections, the second generator has the first condensed fluid passage and ft connection again, and engine also has the second steam channel The finisher connecting with vaporizer has the second condensed fluid passage and ft connection, absorber and condenser also to have respectively to be added again Hot media channel and ft connection, the second absorber also has coolant guiding channel and ft connection, and generator also has high warm to be situated between 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 absorbers, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber is had weak solution pipeline through solution pump and second Solution heat exchanger is connected with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump and the second solution heat exchange Device is connected with the 3rd absorber, and the 3rd absorber has weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and to send out again Raw device connection, generator is had concentrated solution pipeline to connect with the second generator through the second solution heat exchanger and is adjusted to generator and has Concentrated solution pipeline is connected with the 3rd generator through the 3rd solution heat exchanger, and the 3rd generator has concentrated solution pipeline molten through second again Liquid heat exchanger is connected with the second generator, and the 3rd generator also has refrigerant steam channel to connect with the 3rd 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.
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 absorbers, the 3rd solution pump and the 3rd solution heat exchanger, generator is had refrigerant steam channel to connect adjustment with condenser Have refrigerant steam channel to connect with the 3rd absorber for generator, the 3rd absorber also have weak solution pipeline through the 3rd solution pump and 3rd solution heat exchanger is connected with the 3rd generator, the 3rd generator also have concentrated solution pipeline through the 3rd solution heat exchanger with 3rd absorber connection, the 3rd generator also has refrigerant steam channel to connect with condenser, and the 3rd generator also has high warm to be situated between Matter passage and ft connection, the 3rd absorber also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is 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 second throttle, the second absorber set up weak solution pipeline through the 3rd solution pump and 3rd solution heat exchanger is connected with the 3rd generator, the 3rd generator also have concentrated solution pipeline through the 3rd solution heat exchanger with Second generator connection, by generator have refrigerant steam channel connect with condenser be adjusted to generator have refrigerant steam channel and After 3rd generator connection, the 3rd generator has cryogen liquid pipeline to connect with condenser through second throttle again, the 3rd generator Also have refrigerant steam channel to connect with condenser, 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 heat exchangers and second throttle, the second absorber is had weak solution pipeline through solution pump and the second solution heat exchanger Connect with generator be adjusted to the second absorber have weak solution pipeline through solution pump, the second solution heat exchanger and the 3rd solution heat Exchanger is connected with generator, and generator is had concentrated solution pipeline to connect adjustment through the second solution heat exchanger with the second generator Concentrated solution pipeline is had to connect with the 3rd generator through the 3rd solution heat exchanger for generator, the 3rd generator has concentrated solution pipe again Road second solution heat exchanger is connected with the second generator, generator is had refrigerant steam channel to connect with condenser and is adjusted to After generator has refrigerant steam channel to connect with the 3rd generator, the 3rd generator has cryogen liquid pipeline again through second throttle Connect with condenser, the 3rd generator also has refrigerant steam channel to connect with condenser, 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 pumps, the 3rd solution heat exchanger and second throttle, the second absorber is had weak solution pipeline through solution pump and second Solution heat exchanger is connected with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump and the second solution heat exchange Device is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and to send out again Raw device connection, generator is had concentrated solution pipeline to connect with the second generator through the second solution heat exchanger and is adjusted to generator and has Concentrated solution pipeline is connected with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger, and generator is had cryogen Steam channel is connected with condenser and is adjusted to the 3rd generator after generator has refrigerant steam channel to connect with the 3rd generator Cryogen liquid pipeline is had to connect with condenser through second throttle again, the 3rd generator also has refrigerant steam channel with condenser even Logical, form the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is that any hot described in 7-9 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 system of 11. 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, absorber is had weak solution pipeline through solution heat exchanger and the second absorption Device connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, and the 3rd absorber is again There is weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump, the second generator is had concentrated solution pipe Road the second solution pump connect with absorber with solution heat exchanger be adjusted to the second generator have concentrated solution pipeline through solution heat Exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat exchanger Connect with absorber, after engine is had exhaust passage to be sequentially communicated vaporizer and the second generator the second generator have again cold Lime set passage and ft connection are adjusted to engine has exhaust passage to be sequentially communicated vaporizer, the second generator and the 3rd generator 3rd generator has condensed fluid passage and ft connection more afterwards, and the 3rd generator also has refrigerant steam channel and the 3rd absorber Connection, 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 12. 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, absorber is had weak solution pipeline through solution heat exchanger and the second absorption Device connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, and the 3rd absorber is again There is weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump, the second generator is had concentrated solution pipe Road the second solution pump connect with absorber with solution heat exchanger be adjusted to the second generator have concentrated solution pipeline through solution heat Exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat exchanger Connect with absorber, after engine is had the first steam channel to be sequentially communicated vaporizer and the second generator, the second generator is again Having the first condensed fluid passage and ft connection to be adjusted to engine has the first steam channel to be sequentially communicated vaporizer, the second generator There are the first condensed fluid passage and ft connection with the 3rd generator after the 3rd generator again, the 3rd generator also has refrigerant vapour Passage is connected with the 3rd absorber, and the 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 13. heat, are that any hot described at the 3rd moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and second Absorber connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd absorption Device has weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had dense molten Liquid pipeline is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline through molten Liquid heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline to hand over through the second solution pump and the 3rd solution heat again Parallel operation is connected with absorber, and after engine is had exhaust passage to connect with the second generator, the second generator has condensed fluid to lead to again Road is adjusted to the second generator after engine has exhaust passage to connect with the second generator through the 3rd generator with ft connection There are condensed fluid passage and ft connection again, the 3rd generator also has refrigerant steam channel to connect with the 3rd absorber, the 3rd absorption Device also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or by engine there are exhaust passage and second After generator connection, the second generator has condensed fluid passage and ft connection to be adjusted to engine again and has exhaust passage through second After generator is connected with the 3rd generator, the 3rd generator has condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 14. heat, are that any hot described at the 4th moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and second Absorber connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd absorption Device has weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had dense molten Liquid pipeline is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline through molten Liquid heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline to hand over through the second solution pump and the 3rd solution heat again Parallel operation is connected with absorber, and after engine is had the first steam channel to connect with the second generator, the second generator has first again Condensed fluid passage is adjusted to engine with ft connection has the first steam channel to connect it through the 3rd generator with the second generator Second generator has the first condensed fluid passage and ft connection more afterwards, and the 3rd generator also has refrigerant steam channel and the 3rd absorption Device connects, and the 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or by engine After having the first steam channel to connect with the second generator, the second generator has the first condensed fluid passage to adjust with ft connection again After having the first steam channel to connect with the 3rd generator through the second generator for engine, the 3rd generator has the first condensation again Liquid passage and ft connection.
The dynamic co-feeding systems of 15. heat, are that any hot described at the 4th moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber is had weak solution pipeline through solution heat exchanger and second Absorber connection is adjusted to absorber has weak solution pipeline to connect with the 3rd absorber through the 3rd solution heat exchanger, the 3rd absorption Device has weak solution pipeline to connect with the second absorber with solution heat exchanger through the 3rd solution pump again, the second generator is had dense molten Liquid pipeline is connected with absorber through the second solution pump and solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline through molten Liquid heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline to hand over through the second solution pump and the 3rd solution heat again Parallel operation is connected with absorber, and engine is had exhaust passage and ft connection to be adjusted to engine exhaust passage and the 3rd generation After device connection, the 3rd generator has condensed fluid passage and ft connection again, and the 3rd generator also has refrigerant steam channel and the 3rd Absorber connects, and the 3rd absorber also has coolant guiding channel and ft connection, forms the dynamic co-feeding system of heat；Wherein, or power The 3rd generator after exhaust passage is connected set up with the 3rd generator by machine condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 16. heat, be to move in co-feeding system in the described any hot of 1-15 item, cancels generator and connects High temperature thermal medium passage, generator after high-temperature steam passage is connected set up with generator by engine high temperature condensed fluid passage again With ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 17. heat, is that any hot described in 5-6 item moves in co-feeding system, cancels generator and the 3rd The generator high temperature thermal medium passage with ft connection respectively, engine is set up high-temperature steam passage and is sequentially communicated generator and After three generators, the 3rd generator has high temperature condensed fluid passage and ft connection again, forms the dynamic co-feeding system of heat.
Brief description：
Fig. 1 is according to heat provided by the present invention dynamic co-feeding system the 1st kind of structure and schematic flow sheet.
Fig. 2 is according to heat provided by the present invention dynamic co-feeding system the 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to heat provided by the present invention dynamic co-feeding system the 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to heat provided by the present invention dynamic co-feeding system the 4th kind of structure and schematic flow sheet.
Fig. 5 is according to heat provided by the present invention dynamic co-feeding system the 5th kind of structure and schematic flow sheet.
Fig. 6 is according to heat provided by the present invention dynamic co-feeding system the 6th kind of structure and schematic flow sheet.
Fig. 7 is according to heat provided by the present invention dynamic co-feeding system the 7th kind of structure and schematic flow sheet.
Fig. 8 is according to heat provided by the present invention dynamic co-feeding system the 8th kind of structure and schematic flow sheet.
Fig. 9 is according to heat provided by the present invention dynamic co-feeding system the 9th kind of structure and schematic flow sheet.
Figure 10 is according to heat provided by the present invention dynamic co-feeding system the 10th kind of structure and schematic flow sheet.
Figure 11 is according to heat provided by the present invention dynamic co-feeding system the 11st kind of structure and schematic flow sheet.
In figure, 1- absorber, 2- second absorber, 3- generator, 4- second generator, 5- condenser, 6- vaporizer, 7- Choke valve, 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 absorber, 15- the 3rd solution pump, 16- the 3rd solution heat exchanger, 17- second throttle.
Specific embodiment：
First it is noted that in the statement of structure and flow process, inessential in the case of do not repeat；To apparent Flow process do not state.To describe the present invention with example in detail below in conjunction with the accompanying drawings.
Heat shown in Fig. 1 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber 1 Weak solution pipeline is had to connect with the second absorber 2 through solution heat exchanger 10, the second absorber 2 also has weak solution pipeline through solution Pump 8 is connected with generator 3 with the second solution heat exchanger 11, and generator 3 also has concentrated solution pipeline through the second solution heat exchanger 11 are connected with the second generator 4, the second generator 4 also have concentrated solution pipeline through the second solution pump 9 and solution heat exchanger 10 with Absorber 1 connects, and generator 3 also has refrigerant steam channel to connect with condenser 5, and the second generator 4 also has refrigerant steam channel Connect with the second absorber 2, condenser 5 also has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7, and vaporizer 6 also has cryogen Steam channel is connected with absorber 1, and engine 12 has live steam passage and ft connection, and engine 12 also has exhaust passage to connect successively After logical vaporizer 6 and the second generator 4, the second generator 4 has condensed fluid passage and ft connection, absorber 1 and condenser again 5 also have heated medium passage and ft connection respectively, and the second absorber 2 also has coolant guiding channel and ft connection, occurs Device 3 also has high temperature thermal medium passage 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 second The progressively heat release condensing of raw device 4, externally discharges afterwards；The weak solution of absorber 1 enters the second absorption through solution heat exchanger 10 , in cooling medium, the weak solution of the second absorber 2 is through solution pump 8 and the second solution heat exchange for device 2, absorption refrigerant vapour heat release Device 11 enters generator 3, and high temperature thermal medium flows through generator 3, heating enters its interior solution and discharges refrigerant vapour and to condensation Device 5 provides, and the concentrated solution of generator 3 enters the second generator 4, heat absorption release refrigerant vapour simultaneously through the second solution heat exchanger 11 There is provided to the second absorber 2, the concentrated solution of the second generator 4 enters absorber through the second solution pump 9 and solution heat exchanger 10 1st, absorb refrigerant vapour and heat release is in heated medium；The refrigerant vapour heat release of condenser 5 in heated medium and condenses, condensation The cryogen liquid of device 5 enters vaporizer 6, absorbs heat into refrigerant vapour and provide to absorber 1 through choke valve 7 reducing pressure by regulating flow, 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 absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber 1 Weak solution pipeline is had to connect with the second absorber 2 through solution heat exchanger 10, the second absorber 2 also has weak solution pipeline through solution Pump 8 is connected with generator 3 with the second solution heat exchanger 11, and generator 3 also has concentrated solution pipeline through the second solution heat exchanger 11 are connected with the second generator 4, the second generator 4 also have concentrated solution pipeline through the second solution pump 9 and solution heat exchanger 10 with Absorber 1 connects, and generator 3 also has refrigerant steam channel to connect with condenser 5, and the second generator 4 also has refrigerant steam channel Connect with the second absorber 2, condenser 5 also has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7, and vaporizer 6 also has cryogen Steam channel is connected with absorber 1, and engine 12 has live steam passage and ft connection respectively and has exhaust passage and ft connection, Engine 12 also have the first steam channel to be sequentially communicated vaporizer 6 and the second generator 4 after the second generator 4 have again first cold Lime set passage and ft connection, absorber 1 and condenser 5 also have heated medium passage and ft connection, the second absorption respectively Device 2 also has coolant guiding channel and ft connection, and generator 3 also has high temperature thermal medium passage and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing Live steam is divided into two-way after entering engine 12 blood pressure lowering work done, and the first via is supplied to vaporizer 6 and the by the first steam channel Externally discharge after two generator 4 exothermic condensation, the second road is externally discharged after completing blood pressure lowering work done, form the dynamic alliance system of heat System.
Heat shown in Fig. 3 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber 1 Weak solution pipeline is had to connect with the second absorber 2 through solution heat exchanger 10, the second absorber 2 also has weak solution pipeline through solution Pump 8 is connected with generator 3 with the second solution heat exchanger 11, and generator 3 also has concentrated solution pipeline through the second solution heat exchanger 11 are connected with the second generator 4, the second generator 4 also have concentrated solution pipeline through the second solution pump 9 and solution heat exchanger 10 with Absorber 1 connects, and generator 3 also has refrigerant steam channel to connect with condenser 5, and the second generator 4 also has refrigerant steam channel Connect with the second absorber 2, condenser 5 also has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7, and vaporizer 6 also has cryogen Steam channel is connected with absorber 1, and engine 12 has live steam passage and ft connection, and engine 12 also has exhaust passage and outside Connection, after engine 12 also has exhaust passage to connect with the second generator 4, the second generator 4 has condensed fluid passage and outside again Connection, 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 outside again Connection, absorber 1 and condenser 5 also have heated medium passage and ft connection respectively, and the second absorber 2 also has cooling medium Passage and ft connection, generator 3 also has high temperature thermal medium passage and ft connection.
(2), in flow process, co-feeding system workflow dynamic with heat shown in Fig. 1 compares, and is in place of the flow process changing Live steam is divided into three tunnels after entering engine 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, completes a part of steam discharge after blood pressure lowering work done and is supplied to Two generator 4 exothermic condensation is simultaneously externally discharged, and completes another part steam discharge after blood pressure lowering work done and externally discharges, and forms the dynamic connection of heat For system.
Heat shown in Fig. 4 moves what co-feeding system was realized in：
(1) in structure, it mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, Choke valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber 1 Weak solution pipeline is had to connect with the second absorber 2 through solution heat exchanger 10, the second absorber 2 also has weak solution pipeline through solution Pump 8 is connected with generator 3 with the second solution heat exchanger 11, and generator 3 also has concentrated solution pipeline through the second solution heat exchanger 11 are connected with the second generator 4, the second generator 4 also have concentrated solution pipeline through the second solution pump 9 and solution heat exchanger 10 with Absorber 1 connects, and generator 3 also has refrigerant steam channel to connect with condenser 5, and the second generator 4 also has refrigerant steam channel Connect with the second absorber 2, condenser 5 also has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7, and vaporizer 6 also has cryogen Steam channel is connected with absorber 1, and engine 12 has live steam passage and ft connection respectively and has exhaust passage and ft connection, Engine 12 also have the first steam channel connect with the second generator 4 after the second generator 4 have again the first condensed fluid passage and Ft connection, engine 12 also have the finisher 6 that connects with vaporizer 6 of the second steam channel have again the second condensed fluid passage and Ft connection, absorber 1 and condenser 5 also have heated medium passage and ft connection respectively, and the second absorber 2 also has cooling Medium channel and ft connection, generator 3 also has high temperature thermal medium passage and ft connection.
(2), in flow process, 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 the second generator 4, remaining steam continues to complete work done and externally discharges；First steam flows through the second generator 4 heat release Externally discharge after condensation, 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 absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, the second absorber 2 is had weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 Connect with generator 3 and be adjusted to the second absorber 2 and have weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 and the 3rd Absorber 14 connects, and the 3rd absorber 14 has weak solution pipeline through the 3rd solution pump 15 and the 3rd solution heat exchanger 16 and to send out again Raw device 3 connects, and generator 3 is had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11 and is adjusted to Raw device 3 has concentrated solution pipeline to connect with the 3rd generator 13 through the 3rd solution heat exchanger 16, and the 3rd generator 13 has dense molten again Liquid pipeline is connected with the second generator 4 through the second solution heat exchanger 11, and the 3rd generator 13 also has refrigerant steam channel and the Three absorbers 14 connect, and the 3rd generator 13 also has high temperature thermal medium passage and ft connection, and the 3rd absorber 14 is also added Hot media channel and ft connection.
(2), in flow process, the weak solution of the second absorber 2 enters the 3rd suction through solution pump 8 and the second solution heat exchanger 11 Receive device 14, absorb refrigerant vapour heat release in heated medium, the weak solution of the 3rd absorber 14 is through the 3rd solution pump 15 and the Three solution heat exchanger 16 enters generator 3, and the concentrated solution of generator 3 enters the 3rd generator through the 3rd solution heat exchanger 16 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 14 There is provided, the concentrated solution of the 3rd generator 13 enters the second generator 4 through the second solution heat exchanger 11, form 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, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, by generator 3 have refrigerant steam channel connect with condenser 5 be adjusted to generator 3 have cold Agent steam channel is connected with the 3rd absorber 14, and the 3rd absorber 14 also has weak solution pipeline molten through the 3rd solution pump 15 and the 3rd Liquid heat exchanger 16 is connected with the 3rd generator 13, and the 3rd generator 13 also has concentrated solution pipeline through the 3rd solution heat exchanger 16 Connect with the 3rd absorber 14, the 3rd generator 13 also has refrigerant steam channel to connect with condenser 5, and the 3rd generator 13 also has High temperature thermal medium passage and ft connection, the 3rd absorber 14 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 3 produces enters the 3rd absorber 14, the weak solution of the 3rd absorber 14 Enter the 3rd generator 13 through the 3rd solution pump 15 and the 3rd solution heat exchanger 16, high temperature thermal medium flows through the 3rd generator 13rd, heating enters its interior solution release refrigerant vapour and provides to condenser 5, and the concentrated solution of the 3rd generator 13 is molten through the 3rd Liquid heat exchanger 16 enters the 3rd absorber 14, absorbs refrigerant vapour and heat release is in heated medium, 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 second throttle, the second absorber 2 is set up weak solution pipeline and is handed over through the 3rd solution pump 15 and the 3rd solution heat Parallel operation 16 is connected with the 3rd generator 13, and the 3rd generator 13 also has concentrated solution pipeline through the 3rd solution heat exchanger 16 and second Generator 4 connects, by generator 3 have refrigerant steam channel connect with condenser 5 be adjusted to generator 3 have refrigerant steam channel with After 3rd generator 13 connection, the 3rd generator 13 has cryogen liquid pipeline to connect with condenser 5 through second throttle 17 again, the Three generators 13 also have refrigerant steam channel to connect with condenser 5.
(2), in flow process, the refrigerant vapour that generator 3 produces is supplied to the 3rd generator 13 and makees to drive thermal medium, the second suction The part weak solution receiving device 2 enters the 3rd generator 13, refrigerant vapour through the 3rd solution pump 15 and the 3rd solution heat exchanger 16 Flow through the 3rd generator 13, heating enters its interior solution release refrigerant vapour and provides to condenser 5, the 3rd generator 13 Concentrated solution enters the second generator 4 through the 3rd solution heat exchanger 16；Flow through the refrigerant vapour heat release Cheng Leng of the 3rd generator 13 Agent liquid, cryogen liquor stream, through entering condenser 5 after second throttle 17 reducing pressure by regulating flow, 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, increase the 3rd generator, the 3rd solution heat exchanger and Second throttle, the second absorber 2 is had weak solution pipeline to connect with generator 3 through solution pump 8 and the second solution heat exchanger 11 Logical it is adjusted to the second absorber 2 and has weak solution pipeline through solution pump 8, the second solution heat exchanger 11 and the 3rd solution heat exchanger 16 are connected with generator 3, and generator 3 is had concentrated solution pipeline to connect tune through the second solution heat exchanger 11 with the second generator 4 Whole have concentrated solution pipeline to connect with the 3rd generator 13 through the 3rd solution heat exchanger 16 for generator 3, and the 3rd generator 13 is again Have concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11, by generator 3 have refrigerant steam channel with cold Condenser 5 connection be adjusted to the 3rd generator 13 after generator 3 has refrigerant steam channel to connect with the 3rd generator 13 have again cold Agent liquid pipeline is connected with condenser 5 through second throttle 17, and the 3rd generator 13 also has refrigerant steam channel with condenser 5 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 generator 3 generation is supplied to the 3rd generator 13 and makees to drive heat Medium, the weak solution of the second absorber 2 enters through solution pump 8, the second solution heat exchanger 11 and the 3rd solution heat exchanger 16 Generator 3, the concentrated solution of generator 3 enters the 3rd generator 13, refrigerant vapour and high warm through the 3rd solution heat exchanger 16 Medium flows separately through the 3rd generator 13, heating enters its interior solution release refrigerant vapour and provides to condenser 5, the 3rd The concentrated solution of raw device 13 enters the second generator 4 through the second solution heat exchanger 11；Flow through the refrigerant vapour of the 3rd generator 13 Heat release becomes cryogen liquid, and cryogen liquor stream, through entering condenser 5 after second throttle 17 reducing pressure by regulating flow, forms the dynamic co-feeding system of heat.
Heat shown in Fig. 9 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the 3rd solution pump, the 3rd molten Liquid heat exchanger and second throttle, the second absorber 2 is had weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 Connect with generator 3 and be adjusted to the second absorber 2 and have weak solution pipeline through solution pump 8 and the second solution heat exchanger 11 and the 3rd Generator 13 connects, and the 3rd generator 13 has concentrated solution pipeline through the 3rd solution pump 15 and the 3rd solution heat exchanger 16 and to send out again Raw device 3 connects, and generator 3 is had concentrated solution pipeline to connect with the second generator 4 through the second solution heat exchanger 11 and is adjusted to Raw device 3 has concentrated solution pipeline to connect with the second generator 4 with the second solution heat exchanger 11 through the 3rd solution heat exchanger 16, will Generator 3 has refrigerant steam channel to connect with condenser 5 to be adjusted to generator 3 and have refrigerant steam channel and the 3rd generator 13 even After logical, the 3rd generator 13 has cryogen liquid pipeline to connect with condenser 5 through second throttle 17 again, and the 3rd generator 13 also has Refrigerant steam channel is connected with condenser 5.
(2), in flow process, the refrigerant vapour that generator 3 produces is supplied to the 3rd generator 13 and makees to drive thermal medium, the second suction The weak solution receiving device 2 enters the 3rd generator 13 through solution pump 8 and the second solution heat exchanger 11, and refrigerant vapour flows through the 3rd Raw device 13, heating enter its interior solution release refrigerant vapour and simultaneously provide to condenser 5, and the concentrated solution of the 3rd generator 13 is through the Three solution pumps 15 and the 3rd solution heat exchanger 16 enter generator 3, and the concentrated solution of generator 3 is through the 3rd solution heat exchanger 16 Enter the second generator 4 with the second solution heat exchanger 11；The refrigerant vapour heat release flowing through the 3rd generator 13 becomes cryogen liquid, cold Agent liquor stream, through entering condenser 5 after second throttle 17 reducing pressure by regulating flow, forms the dynamic co-feeding system of heat.
Heat shown in Figure 10 moves what co-feeding system was realized in：
(1) in structure, heat shown in Fig. 3 is moved in co-feeding system, increases the 3rd generator, the 3rd absorber, the 3rd molten Liquid pump and the 3rd solution heat exchanger, absorber 1 is had weak solution pipeline to connect with the second absorber 2 through solution heat exchanger 10 Being adjusted to absorber 1 has weak solution pipeline to connect with the 3rd absorber 14 through the 3rd solution heat exchanger 16, the 3rd absorber 14 There is weak solution pipeline to connect with the second absorber 2 with solution heat exchanger 10 through the 3rd solution pump 15 again, the second generator 4 is had Concentrated solution pipeline is connected with absorber 1 through the second solution pump 9 and solution heat exchanger 10 and is adjusted to the second generator 4 and has concentrated solution Pipeline is connected with the 3rd generator 13 through solution heat exchanger 10, and the 3rd generator 13 has concentrated solution pipeline again through the second solution pump 9 are connected with absorber 1 with the 3rd solution heat exchanger 16, after engine 12 is had exhaust passage to connect with the second generator 4 Second generator 4 has condensed fluid passage and ft connection to be adjusted to engine 12 again and has exhaust passage through the 3rd generator 13 and the After two generator 4 connection, the second generator 4 has condensed fluid passage and ft connection again, and the 3rd generator 13 also has refrigerant vapour Passage is connected with the 3rd absorber 14, and the 3rd absorber 14 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 the 3rd generator 13 and the second generator 4 exothermic condensation and externally discharge, complete another part row after blood pressure lowering work done Vapour externally discharges；The weak solution of absorber 1 enters the 3rd absorber 14, absorbs refrigerant vapour simultaneously through the 3rd solution heat exchanger 16 Heat release enters the second absorption in cooling medium, the weak solution of the 3rd absorber 14 through the 3rd solution pump 15 and solution heat exchanger 10 Device 2；The concentrated solution of the second generator 4 through solution heat exchanger 10 enter the 3rd generator 13, heat absorption release refrigerant vapour and to 3rd absorber 14 provides, and the concentrated solution of the 3rd generator 13 enters through the second solution pump 9 and the 3rd solution heat exchanger 16 inhales Receive device 1, form the dynamic co-feeding system of heat.
Heat shown in Figure 11 moves what co-feeding system was realized in：
Heat shown in Fig. 4 is moved in co-feeding system, cancels generator 3 and the high temperature thermal medium passage connecting, engine 12 Setting up generator 3 after high-temperature steam passage is connected with generator 3 has high temperature condensed fluid passage and ft connection again；Engine 12 Passing through high-temperature steam passage respectively provides driving thermic load, passes through the second steam channel to vaporizer 6 offer low temperature to generator 3 Thermic load and provide low temperature thermic load to the second generator 4 by the first steam channel, forms the dynamic co-feeding system of heat.
Effect that the technology of the present invention can be realized heat proposed by the invention moves co-feeding system, have the effect that and Advantage：
(1) high-grade steam elder generation work done, low-grade steam is used for heat supply, meets heat energy efficient utilization principle.
(2) by engine steam discharge, the first steam and the second steam channel, individually or respectively to vaporizer and the second generator Low temperature thermic load is provided, and combines the second generator and the second absorber, realize Steam Power Equipment end steam discharge or low pressure is taken out The effectively utilizes of the temperature difference between vapour and cold environment.
(3) release cleaning or high efficient energy sources and move the application restriction in co-feeding system in conventional thermal.
(4) with engine end steam for the dynamic alliance low-temperature heat source of heat, be conducive to improving the thermal efficiency and the equipment of engine The safety running.
(5) enrich the type of the dynamic co-feeding system of heat, extend the range of application of absorption heat pump, be conducive to preferably adopting Improve heat utilization rate with absorption heat pump technology.

Claims (17)

1. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, section Stream valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber (1) Weak solution pipeline is had to connect with the second absorber (2) through solution heat exchanger (10), the second absorber (2) also has weak solution pipeline Connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), generator (3) also has concentrated solution pipeline through the Two solution heat exchangers (11) are connected with the second generator (4), and the second generator (4) also has concentrated solution pipeline through the second solution pump (9) connect with absorber (1) with solution heat exchanger (10), generator (3) also has refrigerant steam channel with condenser (5) even Logical, the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), and condenser (5) also has cryogen liquid pipeline warp Choke valve (7) is connected with vaporizer (6), and vaporizer (6) also has refrigerant steam channel to connect with absorber (1), engine (12) There are live steam passage and ft connection, engine (12) or also exhaust passage and ft connection, engine (12) also has steam discharge to lead to After road is sequentially communicated vaporizer (6) and the second generator (4), the second generator (4) has condensed fluid passage and ft connection again, Absorber (1) and condenser (5) also have heated medium passage and ft connection respectively, and the second absorber (2) also has cooling to be situated between Matter passage and ft connection, generator (3) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
2. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, section Stream valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber (1) Weak solution pipeline is had to connect with the second absorber (2) through solution heat exchanger (10), the second absorber (2) also has weak solution pipeline Connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), generator (3) also has concentrated solution pipeline through the Two solution heat exchangers (11) are connected with the second generator (4), and the second generator (4) also has concentrated solution pipeline through the second solution pump (9) connect with absorber (1) with solution heat exchanger (10), generator (3) also has refrigerant steam channel with condenser (5) even Logical, the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), and condenser (5) also has cryogen liquid pipeline warp Choke valve (7) is connected with vaporizer (6), and vaporizer (6) also has refrigerant steam channel to connect with absorber (1), 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 successively After connection vaporizer (6) and the second generator (4), the second generator (4) has the first condensed fluid passage and ft connection again, inhales Receive device (1) and condenser (5) also has heated medium passage and ft connection respectively, the second absorber (2) also has cooling medium Passage and ft connection, generator (3) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
3. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, section Stream valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber (1) Weak solution pipeline is had to connect with the second absorber (2) through solution heat exchanger (10), the second absorber (2) also has weak solution pipeline Connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), generator (3) also has concentrated solution pipeline through the Two solution heat exchangers (11) are connected with the second generator (4), and the second generator (4) also has concentrated solution pipeline through the second solution pump (9) connect with absorber (1) with solution heat exchanger (10), generator (3) also has refrigerant steam channel with condenser (5) even Logical, the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), and condenser (5) also has cryogen liquid pipeline warp Choke valve (7) is connected with vaporizer (6), and vaporizer (6) also has refrigerant steam channel to connect with absorber (1), engine (12) There are live steam passage and ft connection, engine (12) or also exhaust passage and ft connection, engine (12) also has steam discharge to lead to After road is connected with the second generator (4), the second generator (4) has condensed fluid passage and ft connection again, and engine (12) also has The finisher (6) that first steam channel is connected with vaporizer (6) has the first condensed fluid passage and ft connection, absorber again (1) and condenser (5) also has heated medium passage and ft connection respectively, the second absorber (2) also has coolant guiding channel With ft connection, generator (3) also high temperature thermal medium passage and ft connection, form the dynamic co-feeding system of heat.
4. the dynamic co-feeding system of heat, mainly by absorber, the second absorber, generator, the second generator, condenser, vaporizer, section Stream valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and engine are formed；Absorber (1) Weak solution pipeline is had to connect with the second absorber (2) through solution heat exchanger (10), the second absorber (2) also has weak solution pipeline Connect with generator (3) with the second solution heat exchanger (11) through solution pump (8), generator (3) also has concentrated solution pipeline through the Two solution heat exchangers (11) are connected with the second generator (4), and the second generator (4) also has concentrated solution pipeline through the second solution pump (9) connect with absorber (1) with solution heat exchanger (10), generator (3) also has refrigerant steam channel with condenser (5) even Logical, the second generator (4) also has refrigerant steam channel to connect with the second absorber (2), and condenser (5) also has cryogen liquid pipeline warp Choke valve (7) is connected with vaporizer (6), and vaporizer (6) also has refrigerant steam channel to connect with absorber (1), engine (12) There are live steam passage and ft connection respectively and have exhaust passage and ft connection, engine (12) also the first steam channel and the After two generators (4) connection, the second generator (4) has the first condensed fluid passage and ft connection again, and engine (12) also has the The finisher (6) that two steam channels are connected with vaporizer (6) has the second condensed fluid passage and ft connection, absorber (1) again Also there are heated medium passage and ft connection with condenser (5) respectively, the second absorber (2) also has coolant guiding channel with outward Portion connects, and generator (3) also has high temperature thermal medium passage and ft connection, forms the dynamic co-feeding system of heat.
5. the dynamic co-feeding system of heat, is 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 absorber (2) is had weak solution pipeline through solution pump (8) Connect with generator (3) with the second solution heat exchanger (11) and be adjusted to the second absorber (2) and have weak solution pipeline through solution pump (8) with the second solution heat exchanger (11) is connected with the 3rd absorber (14), and the 3rd absorber (14) has weak solution pipeline warp again 3rd solution pump (15) is connected with generator (3) with the 3rd solution heat exchanger (16), and generator (3) is had concentrated solution pipeline warp Second solution heat exchanger (11) is connected with the second generator (4) and is adjusted to generator (3) and has concentrated solution pipeline through the 3rd solution Heat exchanger (16) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline again through the second solution heat exchange Device (11) is connected with the second generator (4), and the 3rd generator (13) also has refrigerant steam channel to connect with the 3rd absorber (14), 3rd generator (13) also have high temperature thermal medium passage and ft connection, the 3rd absorber (14) also have heated medium passage with Ft connection, 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 absorbers, the 3rd solution pump and the 3rd solution heat exchanger, generator (3) is had refrigerant steam channel with condenser (5) even Logical be adjusted to generator (3) and have refrigerant steam channel to connect with the 3rd absorber (14), the 3rd absorber (14) also weak solution Pipeline is connected with the 3rd generator (13) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15), the 3rd generator (13) Concentrated solution pipeline is also had to connect with the 3rd absorber (14) through the 3rd solution heat exchanger (16), the 3rd generator (13) is also cold Agent steam channel is connected with condenser (5), and the 3rd generator (13) also has high temperature thermal medium passage and ft connection, the 3rd absorption Device (14) also has heated medium passage and ft connection, forms the dynamic co-feeding system of heat.
7. the dynamic co-feeding system of heat, is 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 second throttle, the second absorber (2) sets up weak solution pipeline through the 3rd solution pump (15) connect with the 3rd generator (13) with the 3rd solution heat exchanger (16), the 3rd generator (13) also has concentrated solution pipeline warp 3rd solution heat exchanger (16) is connected with the second generator (4), and generator (3) is had refrigerant steam channel and condenser (5) Connection be adjusted to the 3rd generator (13) after generator (3) has refrigerant steam channel to connect with the 3rd generator (13) have again cold Agent liquid pipeline is connected with condenser (5) through second throttle (17), and the 3rd generator (13) also has refrigerant steam channel and condensation Device (5) connects, and 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 heat exchangers and second throttle, the second absorber (2) is had weak solution pipeline through solution pump (8) and the second solution heat Exchanger (11) is connected with generator (3) and is adjusted to the second absorber (2) and has weak solution pipeline through solution pump (8), the second solution Heat exchanger (11) is connected with generator (3) with the 3rd solution heat exchanger (16), and generator (3) is had concentrated solution pipeline through Two solution heat exchangers (11) connect with the second generator (4) be adjusted to generator (3) have concentrated solution pipeline through the 3rd solution heat Exchanger (16) 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 the second generator (4), generator (3) is had refrigerant steam channel to connect with condenser (5) and is adjusted to generator (3) after having refrigerant steam channel to connect with the 3rd generator (13), the 3rd generator (13) has cryogen liquid pipeline again through second section Stream valve (17) is connected with condenser (5), and the 3rd generator (13) also has refrigerant steam channel to connect with condenser (5), forms heat Dynamic co-feeding system.
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 pumps, the 3rd solution heat exchanger and second throttle, the second absorber (2) is had weak solution pipeline through solution pump (8) Connect with generator (3) with the second solution heat exchanger (11) and be adjusted to the second absorber (2) and have weak solution pipeline through solution pump (8) with the second solution heat exchanger (11) is connected with the 3rd generator (13), and the 3rd generator (13) has concentrated solution pipeline warp again 3rd solution pump (15) is connected with generator (3) with the 3rd solution heat exchanger (16), and generator (3) is had concentrated solution pipeline warp Second solution heat exchanger (11) is connected with the second generator (4) and is adjusted to generator (3) and has concentrated solution pipeline through the 3rd solution Heat exchanger (16) is connected with the second generator (4) with the second solution heat exchanger (11), and generator (3) is had refrigerant vapour to lead to Road is connected with condenser (5) and is adjusted to the 3rd after generator (3) has refrigerant steam channel to connect with the 3rd generator (13) Raw device (13) has cryogen liquid pipeline to connect with condenser (5) through second throttle (17) again, and the 3rd generator (13) also has cryogen Steam channel is connected with condenser (5), forms the dynamic co-feeding system of heat.
10. the dynamic co-feeding system of heat, is that any hot described in claim 7-9 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 system of 11. 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, absorber (1) is had weak solution pipeline through solution heat exchanger (10) and the Two absorbers (2) connection is adjusted to absorber (1) has weak solution pipeline through the 3rd solution heat exchanger (16) and the 3rd absorber (14) connect, the 3rd absorber (14) has weak solution pipeline again through the 3rd solution pump (15) and solution heat exchanger (10) and second Absorber (2) connects, the second generator (4) is had concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) and Absorber (1) connection is adjusted to the second generator (4) has concentrated solution pipeline through solution heat exchanger (10) and the 3rd generator (13) connect, the 3rd generator (13) have concentrated solution pipeline through the second solution pump (9) and the 3rd solution heat exchanger (16) again and Absorber (1) connects, and engine (12) is had exhaust passage to be sequentially communicated vaporizer (6) and the second generator (4) afterwards second Generator (4) have again condensed fluid passage and ft connection be adjusted to engine (12) have exhaust passage be sequentially communicated vaporizer (6), After second generator (4) and the 3rd generator (13), the 3rd generator (13) has condensed fluid passage and ft connection again, and the 3rd Generator (13) also has refrigerant steam channel to connect with the 3rd absorber (14), and the 3rd absorber (14) also has coolant guiding channel With ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding system of 12. 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, absorber (1) is had weak solution pipeline through solution heat exchanger (10) and the Two absorbers (2) connection is adjusted to absorber (1) has weak solution pipeline through the 3rd solution heat exchanger (16) and the 3rd absorber (14) connect, the 3rd absorber (14) has weak solution pipeline again through the 3rd solution pump (15) and solution heat exchanger (10) and second Absorber (2) connects, the second generator (4) is had concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) and Absorber (1) connection is adjusted to the second generator (4) has concentrated solution pipeline through solution heat exchanger (10) and the 3rd generator (13) connect, the 3rd generator (13) have concentrated solution pipeline through the second solution pump (9) and the 3rd solution heat exchanger (16) again and Absorber (1) connects, after engine (12) is had the first steam channel to be sequentially communicated vaporizer (6) and the second generator (4) Second generator (4) has the first condensed fluid passage and ft connection to be adjusted to engine (12) again has the first steam channel to connect successively After logical vaporizer (6), the second generator (4) and the 3rd generator (13), the 3rd generator (13) has the first condensed fluid passage again With ft connection, also refrigerant steam channel is connected the 3rd generator (13) with the 3rd absorber (14), the 3rd absorber (14) Also have coolant guiding channel 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 3 moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (10) Connect with the second absorber (2) be adjusted to absorber (1) have weak solution pipeline through the 3rd solution heat exchanger (16) with the 3rd suction Receive device (14) connection, the 3rd absorber (14) have weak solution pipeline through the 3rd solution pump (15) and solution heat exchanger (10) again and Second absorber (2) connects, and the second generator (4) is had concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) connect with absorber (1) be adjusted to the second generator (4) have concentrated solution pipeline through solution heat exchanger (10) with the 3rd Raw device (13) connection, the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (9) and the 3rd solution heat exchanger (16) connect with absorber (1), the second generator after engine (12) is had exhaust passage to connect with the second generator (4) (4) having condensed fluid passage and ft connection to be adjusted to engine (12) again has exhaust passage through the 3rd generator (13) and second After raw device (4) connection, the second generator (4) has condensed fluid passage and ft connection again, and the 3rd generator (13) also has cryogen to steam Vapour passage is connected with the 3rd absorber (14), and the 3rd absorber (14) also has coolant guiding channel and ft connection, forms heat dynamic Co-feeding system；Wherein, after or engine (12) being had exhaust passage to connect with the second generator (4), the second generator (4) is again Having condensed fluid passage and ft connection to be adjusted to engine (12) has exhaust passage through the second generator (4) and the 3rd generator (13) after connecting, the 3rd generator (13) has condensed fluid passage and ft connection again.
The dynamic co-feeding systems of 14. heat, are that any hot described in claim 4 moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (10) Connect with the second absorber (2) be adjusted to absorber (1) have weak solution pipeline through the 3rd solution heat exchanger (16) with the 3rd suction Receive device (14) connection, the 3rd absorber (14) have weak solution pipeline through the 3rd solution pump (15) and solution heat exchanger (10) again and Second absorber (2) connects, and the second generator (4) is had concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) connect with absorber (1) be adjusted to the second generator (4) have concentrated solution pipeline through solution heat exchanger (10) with the 3rd Raw device (13) connection, the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (9) and the 3rd solution heat exchanger (16) connect with absorber (1), the second generation after engine (12) is had the first steam channel to connect with the second generator (4) Device (4) has the first condensed fluid passage and ft connection to be adjusted to engine (12) again and has the first steam channel through the 3rd generator (13) after connecting with the second generator (4), the second generator (4) has the first condensed fluid passage and ft connection, the 3rd generation again Device (13) also has refrigerant steam channel to connect with the 3rd absorber (14), and the 3rd absorber (14) also has coolant guiding channel with outward Portion connects, and forms the dynamic co-feeding system of heat；Wherein, or by engine (12) the first steam channel is had to connect with the second generator (4) Second generator (4) has the first condensed fluid passage and ft connection to be adjusted to engine (12) again and has the first steam channel warp afterwards After second generator (4) is connected with the 3rd generator (13), the 3rd generator (13) has the first condensed fluid passage to connect with outside again Logical.
The dynamic co-feeding systems of 15. heat, are that any hot described in claim 4 moves in co-feeding system, increase the 3rd generator, the 3rd Absorber, the 3rd solution pump and the 3rd solution heat exchanger, absorber (1) is had weak solution pipeline through solution heat exchanger (10) Connect with the second absorber (2) be adjusted to absorber (1) have weak solution pipeline through the 3rd solution heat exchanger (16) with the 3rd suction Receive device (14) connection, the 3rd absorber (14) have weak solution pipeline through the 3rd solution pump (15) and solution heat exchanger (10) again and Second absorber (2) connects, and the second generator (4) is had concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) connect with absorber (1) be adjusted to the second generator (4) have concentrated solution pipeline through solution heat exchanger (10) with the 3rd Raw device (13) connection, the 3rd generator (13) has concentrated solution pipeline again through the second solution pump (9) and the 3rd solution heat exchanger (16) connect with absorber (1), engine (12) is had exhaust passage and ft connection to be adjusted to engine (12) has steam discharge to lead to After road is connected with the 3rd generator (13), the 3rd generator (13) has condensed fluid passage and ft connection again, the 3rd generator (13) refrigerant steam channel is also had to connect with the 3rd absorber (14), the 3rd absorber (14) also has coolant guiding channel and outside Connection, forms the dynamic co-feeding system of heat；Wherein, or engine (12) is set up after exhaust passage is connected with the 3rd generator (13) Three generators (13) have condensed fluid passage and ft connection again.
16. hot dynamic co-feeding systems, are to move in co-feeding system in any hot described in claim 1-15, cancel generator (3) and connect Logical high temperature thermal medium passage, generator (3) after high-temperature steam passage is connected set up with generator (3) by engine (12) has again High temperature condensed fluid passage and ft connection, form the dynamic co-feeding system of heat.
The dynamic co-feeding systems of 17. heat, are that any hot described in claim 5-6 moves in co-feeding system, cancel generator (3) and the Three generators (13) the high temperature thermal medium passage with ft connection respectively, engine (12) is set up high-temperature steam passage and is sequentially communicated After generator (3) and the 3rd generator (13), the 3rd generator (13) has high temperature condensed fluid passage and ft connection again, is formed The dynamic co-feeding system of heat.
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