CN106170668B - It is a kind of that steam driven method is provided - Google Patents
It is a kind of that steam driven method is provided Download PDFInfo
- Publication number
- CN106170668B CN106170668B CN201580010306.8A CN201580010306A CN106170668B CN 106170668 B CN106170668 B CN 106170668B CN 201580010306 A CN201580010306 A CN 201580010306A CN 106170668 B CN106170668 B CN 106170668B
- Authority
- CN
- China
- Prior art keywords
- valve
- refrigeration cycle
- heat
- heat pump
- adsorbent bed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- 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
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
- F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
-
- 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
-
- 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
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
It is a kind of that steam driven method is provided, including heat pump refrigeration cycle system and Steam Power Circulation system, heat pump refrigeration cycle system is by recycling steam condensation latent heat as driving heat source, drive heat pump refrigeration cycle system, using the high temperature heat source that heat pump refrigeration cycle system exports as the heat source of Steam Power Circulation system, using the low-temperature heat source that heat pump refrigeration cycle system exports as the condensation heat source of Steam Power Circulation system.In this way, consuming a small amount of mechanical work, heat source and cold source are provided for Steam Power Circulation.Cold source other than it can provide cold source for Steam Power Circulation, flap portion can outside cooling supply, realize the cold alliance of electricity.The economy problems for overcoming the dynamical system of existing heat pump cycle and power cycle composition, realize extensive green power.
Description
Technical field
The present invention relates to a kind of steam driven methods, belong to steam power technical field.
Background technique
General steam class power output device (steam engine, steam turbine) is using energy such as fossil energy, nuclear energy, solar energy
Heat supply, the burning of fossil energy can generate serious environmental pollution, and nuclear-energy plant security control requirements are high, solar collecting device
It invests very big.
CN1940254 discloses a kind of dynamical system bulk cargo for combining and being constituted with absorption system with power circulation system
It sets, this dynamical system, provides the steam exhaust that steam power machinery is discharged in low temperature cold coal using absorption refrigeration and cool down, it should
Technology can provide power using low-grade heat source.CN1940254 also discloses one kind with power circulation system, compression heat pump
The power system device that system, absorption type refrigeration circulating system are constituted, this system is in previous system-based, using heat pump pair
Heat source heats up, and improves the initial temperature of power circulation system, keeps the more previous system of the efficiency of dynamical system higher.
CN1940254 also disclose it is a kind of with power circulation system, absorption type heat pump system, absorption type refrigeration circulating system power
The efficiency of system, this more previous system of system increases again.But these three dynamical systems have a defect that, absorption system
Cooling system at least needs two kinds of heat sources, and a kind of high temperature heat source is as driving heat source, and a kind of middle temperature-heat-source is as coolant and low temperature
Heat source uses.In general, normal temperature environment is a kind of heat source, it is also necessary in addition provide a kind of driving heat source, which could just
Often work.There are many kinds of heat sources, in addition to using fossil energy and waste heat, there is the offer using the different high temperature differences above sea level of high mountain
Different heat sources, also there is that concentrated water does not provide different heat sources deeply using seawater, but these heat sources limited by natural conditions it is larger,
It can be used and manufacture different height above sea level manually to generate the temperature difference, but this method higher cost, economic value be not high.Also it adopts
High temperature heat source is provided with solar energy heating, but solar energy heating needs the space of large area installation solar energy heat collector.This
Limit the commercial applications of system.
Summary of the invention
Technical problem to be solved by the invention is to provide it is to be solved the problem of be: provide that CN1940254 is disclosed to be provided
The driving heat of economy, low pollution, low emission needed for steam driven system in addition to fossil energy, waste heat and solar energy heating
The method in source.
The technical solution adopted by the present invention: a kind of that steam driven method, including heat pump refrigeration cycle system and steaming are provided
Vapour power circulation system, the heat pump refrigeration cycle system is by recycling steam condensation latent heat as driving heat source, driving
The heat pump refrigeration cycle system, using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation
The heat source of system, using the low-temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Condense heat source.
Further, the heat pump refrigeration cycle system is made of refrigerant circulation and solution circulation, and the refrigerant follows
Ring is changed by the refrigerant end of generator, compressor, generator, the second expenditure and pressure valve, evaporator, absorber, solution pump, solution
Hot device, generator refrigerant end circuit is in turn connected by pipeline, the solution circulation by generator, solution heat exchanger,
Absorber, solution pump, solution heat exchanger, generator are in turn connected into circuit by pipeline；The Steam Power Circulation system by
The absorber, expanding machine, evaporator, working medium pump, absorber are in turn connected into another circuit, the heat pump refrigerating by pipeline
The working medium of the circulatory system big material composition of solubility equipped with working medium and in working medium is to solution, the Steam Power Circulation system
It is interior to be equipped with working medium.
Further, the heat pump refrigeration cycle system divides two-way, the refrigerant end of first adsorbent bed of routing, the first valve
Door, compressor, the second valve, the heat source side of the first adsorbent bed, third valve, the second expenditure and pressure valve, evaporator, the 4th valve
Door, the second adsorbent bed refrigerant end are connected in sequence by pipeline；Refrigerant end of the another way by the second adsorbent bed, the 5th valve
Door, compressor, the 6th valve, the heat source side of the second adsorbent bed, the 7th valve, the second expenditure and pressure valve, evaporator, the 8th valve
Door, the first adsorbent bed refrigerant end be connected in sequence by pipeline, the heat pump refrigeration cycle system is using working medium and right
There is working medium the adsorbent of adsorption capacity to form working medium pair, and filling is adsorbed with the absorption of a certain amount of working medium in the first adsorbent bed
Agent, is packed into the few adsorbent of absorption working pair amount in the second adsorbent bed, and the Steam Power Circulation system is also classified into two-way, and one
Route the first adsorbent bed, the 9th valve, expanding machine, evaporator, working medium pump, the 12nd valve, the first adsorbent bed by pipeline according to
It is secondary to connect into primary Ioops；One routing the second adsorbent bed, the tenth valve, expanding machine, evaporator, working medium pump, the 11st valve, second
Adsorbent bed is in turn connected into another circuit by pipeline, is equipped with working medium in the Steam Power Circulation system.
Further, the heat pump refrigeration cycle system is made of driving circulation and heat pump refrigeration cycle.
Further, the driving circulation is in turn connected into circuit by pipeline by evaporator, condenser, evaporator, institute
It states heat pump refrigeration cycle to be made of refrigerant circulation and solution circulation, the refrigerant circulation is mentioned by generator, condenser, working medium
It rises pump, evaporator, absorber, solution pump, solution heat exchanger, generator and circuit is in turn connected by pipeline, the solution follows
Ring is in turn connected into circuit by pipeline by generator, solution heat exchanger, liquid liquid pump, absorber, solution heat exchanger, generator,
Refrigerant and the in the refrigerant solution of the biggish material composition of solubility are equipped in the heat pump refrigeration cycle system；The steaming
Vapour power cycle by be used as the absorber of evaporator, expanding machine, the generator as condenser, working medium pump, as evaporator
Absorber is in turn connected into circuit by pipeline.
Further, the driving circulation is successively connected by the first adsorbent bed, the second adsorbent bed, the first adsorbent bed by pipeline
Be connected into circuit, the heat pump refrigeration cycle divides two-way, first adsorbent bed of routing, the first valve, condenser, working medium elevator pump,
Evaporator, the 4th valve, the second adsorbent bed and pipeline are connected in sequence；One the second adsorbent bed of routing, the 5th valve, condensation
Device, working medium elevator pump, evaporator, the 8th valve, the first adsorbent bed are connected in sequence by pipeline, the heat pump refrigeration cycle
System is equipped with working medium and there is the adsorbent of adsorption capacity to form working medium pair working medium, and absorption is filled in first adsorbent bed
There is the adsorbent of a certain amount of working medium, the few adsorbent of absorption working pair amount is packed into second adsorbent bed, the steam is dynamic
Power circulation by be used as the condenser of evaporator, expanding machine, the evaporator as condenser, working medium pump, as the condensation of evaporator
Device is in turn connected into circuit by pipeline.
Further, the driving circulation is in turn connected into circuit by pipeline by generator, absorber, generator；Institute
It states heat pump refrigeration cycle to be made of refrigerant circulation and solution circulation, the refrigerant circulation is by generator, condenser, the second section
Stream pressure reducing valve, evaporator, absorber, solution pump, solution heat exchanger, generator are in turn connected into circuit by pipeline, described molten
Liquid circulation is in turn connected into back by generator, solution heat exchanger, absorber, solution pump, solution heat exchanger, generator by pipeline
Road, the heat pump refrigeration cycle system is interior to be equipped with refrigerant and the in the refrigerant solution of the biggish material composition of solubility；Institute
Steam Power Circulation is stated by being used as the condenser of evaporator, expanding machine, the evaporator as condenser, working medium pump, being used as evaporation
The condenser of device is in turn connected into circuit by pipeline.
Further, the driving circulation is passed through by compressor, generator, first throttle pressure reducing valve, condenser, compressor
Pipeline connects into circuit, and the heat pump refrigeration cycle is made of refrigerant circulation and solution circulation, and the refrigerant circulation is by sending out
Raw device, condenser, the second expenditure and pressure valve, evaporator, absorber, solution pump, solution heat exchanger, generator pass through pipeline successively
Circuit is connected into, the solution circulation is led to by generator, solution heat exchanger, absorber, solution pump, solution heat exchanger, generator
Piping is in turn connected into circuit, and refrigerant is equipped in the heat pump refrigeration cycle system and solubility is biggish in the refrigerant
The solution of material composition；The Steam Power Circulation system passes through pipe by absorber, evaporator, expanding machine, working medium pump, absorber
Road is in turn connected into circuit.
Further, the driving circulation divides two-way, a compressors, the second valve, the first adsorbent bed, third valve
Door, first throttle pressure reducing valve, condenser, compressor are in turn connected into circuit, another compressors, the 6th valve by pipeline
Door, the second adsorbent bed, the 7th valve, first throttle pressure reducing valve, condenser, compressor are in turn connected into circuit by pipeline；Institute
State heat pump refrigeration cycle and divide two-way, first adsorbent bed of routing, the first valve, condenser, the second expenditure and pressure valve, evaporator,
4th valve, the second adsorbent bed are connected in sequence by pipeline, and another way is by the second adsorbent bed, the 5th valve, condenser,
Two expenditure and pressure valves, evaporator, the 8th valve, the first adsorbent bed are connected in sequence by pipeline, the heat pump refrigeration cycle
System is equipped with working medium and there is the adsorbent of adsorption capacity to form working medium pair working medium, and absorption is filled in first adsorbent bed
There is the adsorbent of a certain amount of working medium, the few adsorbent of absorption working pair amount is packed into second adsorbent bed；The steam is dynamic
The power circulatory system also divides two-way, second adsorbent bed of routing, the tenth valve, expanding machine, evaporator, working medium pump, the 11st valve,
Second adsorbent bed is connected in sequence by pipeline；Another way is by the first adsorbent bed, the 9th valve, expanding machine, evaporator, working medium
Pump, the 12nd valve, the first adsorbent bed are connected in sequence by pipeline.
Further, the driving circulation is passed through by generator, first throttle pressure reducing valve, absorber, compressor, generator
Pipeline is in turn connected into circuit；The heat pump refrigeration cycle is made of refrigerant circulation and solution circulation, the refrigerant circulation
Pipeline is passed through by generator, condenser, the second expenditure and pressure valve, evaporator, absorber, solution pump, solution heat exchanger, generator
It is in turn connected into circuit, the solution circulation is by generator, solution heat exchanger, absorber, solution pump, solution heat exchanger, generation
Device is in turn connected into circuit by pipeline, be equipped in the heat pump refrigeration cycle system refrigerant and in the refrigerant solubility compared with
The solution of big material composition；The Steam Power Circulation system is led to by condenser, expanding machine, evaporator, working medium pump, condenser
Piping is in turn connected into circuit.
Further, the driving circulation divides two-way, routing second adsorbent bed, the tenth valve, compressor, the second valve
Door, the first adsorbent bed, the 12nd valve, first throttle pressure reducing valve, the second adsorbent bed are in turn connected into circuit by pipeline；It is another
Route the first adsorbent bed, the 9th valve, compressor, the 6th valve, the second adsorbent bed, the 7th valve, third expenditure and pressure valve,
One adsorbent bed is in turn connected into circuit by pipeline；The heat pump refrigeration cycle also divides two-way, routing first adsorbent bed, first
Valve, condenser, the second expenditure and pressure valve, evaporator, the 4th valve, the second adsorbent bed are connected in sequence by pipeline；Separately
One the second adsorbent bed of routing, the 5th valve, condenser, the second expenditure and pressure valve, evaporator, the 8th valve, the first adsorbent bed are logical
Piping is connected in sequence, and the heat pump refrigeration cycle system is equipped with working medium and has the adsorbent group of adsorption capacity to working medium
At working medium pair, filling is adsorbed with the adsorbent of a certain amount of working medium in the first adsorbent bed, and absorption is packed into the second adsorbent bed
The few adsorbent of working medium amount；The Steam Power Circulation system by condenser, expanding machine, evaporator and working medium pump by pipeline according to
It is secondary to be formed by connecting.
Effect of the invention: the condensation latent heat of working substance steam is used in effective recycling hot compression formula heat pump refrigeration cycle
Make driving heat source, only consumes a small amount of mechanical compression function.In this way, by consuming a small amount of mechanical work to produce hot environment and low
Warm environment provides heat source and cold source for Steam Power Circulation.Cold source is rich other than it can provide cold source for Steam Power Circulation
Remaining part point can outside cooling supply, realize the cold alliance of electricity.When making low-temperature heat source using air or water, due to the energy essence in air
On be solar energy, air is that nature flows in the environment, is all inexhaustible, nexhaustible in any one place.This
Sample one, it is all in the place for needing power, easily cheap it can obtain on a large scale power.Both it solved
In CN1940254 dynamical system due to a lack of high-efficiency and economic driving heat source and hinder the obstacle of business promotion, also overcome existing
The fossil energies conversion process such as coal, natural gas, petroleum in environmental pollution and carbon emission the problem of, and overcome the existing sun
The problem of renewable energy conversions such as energy, wind energy, biomass energy are at high cost, can not compete with fossil energies such as coals.Thoroughly solve
Problem of environmental pollution and greenhouse gas emission problem caused by the use due to fossil energy that current Earth is faced, trend
Green Development, low carbon development.
Detailed description of the invention
Fig. 1 drives absorption heat pump refrigerant vapor dynamical system schematic diagram certainly.
Fig. 2 drives adsorption type heat pump refrigerant vapor dynamical system schematic diagram certainly.
Fig. 3 composite absorption heat pump refrigerant vapor dynamical system schematic diagram.
Fig. 4 composite adsorption heat pump refrigerating steam power system schematic diagram.
Fig. 5 composite absorption heat pump refrigerant vapor dynamical system schematic diagram.
Fig. 6 composite absorption heat pump refrigerant vapor dynamical system schematic diagram.
Fig. 7 composite adsorption heat pump refrigerating steam power system schematic diagram.
The heat pump refrigerating steam power system schematic diagram of Fig. 8 absorption thermal drivers.
The adsorption type heat pump refrigerant vapor dynamical system schematic diagram of Fig. 9 absorption thermal drivers.
In attached drawing, parts list represented by the reference numerals are as follows:
1, generator, 2, compressor, 3, expenditure and pressure valve, 4, evaporator, 5, absorber, 6, solution heat exchanger, 7, solution
Pump, 8, expanding machine, 9, working medium pump, 10, condenser, 11, adsorbent bed, 12, valve, 13, valve, 14, valve, 15, valve, 16,
Valve, 17, valve, 18, valve, 19, valve, 20, valve, 21, valve, 22, valve, 23, valve, 24, adsorbent bed, 25, section
Flow pressure reducing valve, 26, expenditure and pressure valve, 27, working medium elevator pump.
Specific embodiment
The principle and features of the present invention will be described below with reference to the accompanying drawings, and the given examples are served only to explain the present invention, and
It is non-to be used to limit the scope of the invention.
From driving absorption heat pump refrigerant vapor dynamical system as shown in Figure 1, system is by heat pump refrigeration cycle system and steaming
Vapour power circulation system is constituted.
Heat pump refrigeration cycle system is made of refrigerant circulation and solution circulation.1 refrigerant end of refrigerant circulation generator,
Compressor 2,1 heat source side of generator, expenditure and pressure valve 3, evaporator 4, absorber 5, solution pump 7, solution heat exchanger 6, generator 1
Refrigerant end is connected in sequence with pipeline.The solution circulation is by 1 refrigerant end of generator, solution heat exchanger 6, absorber 5
Refrigerant end, solution pump 7, solution heat exchanger 6,1 refrigerant end of generator are in turn connected into circuit by pipeline.The heat pump system
In SAPMAC method system be equipped with working medium and in working medium the big material composition of solubility working medium to solution.Refrigerant weak solution is being sent out
By high temperature heat source heating evaporation in raw device 1, compression refrigerant steam in generation, concentrated solution enters solution heat exchanger 6 and carrys out self-absorption
Enter absorber 5 after the weak solution heat exchange of device 5, middle compression refrigerant steam compresses pressurization heating through compressor 2, generates high temperature and pressure
Refrigerant vapour, high-temperature high-pressure refrigerant opposing steam flow make driving steam to 1 heat source side of generator, the weak solution into generator 1
Heat release, itself is condensed into refrigerant liquid, and refrigerant liquid, which is throttled, enters evaporator 4 after 3 expenditure and pressure of pressure reducing valve, is first steaming
It sends out to absorb heat in the condensation segment of device 4 from the steam exhaust of Steam Power Circulation and evaporate, moist steam continues in the refrigerating section of evaporator, from cold
It absorbs heat and evaporates in matchmaker, be all vaporizated into low pressure refrigerant vapor, low pressure refrigerant vapor enters absorber 5, is absorbed in device 5
Concentrated solution absorbs, while heat is transmitted to the worker quality liquid of Steam Power Circulation by heat release, and refrigerant weak solution is pumped into through solution pump 7
Solution heat exchanger 6 enters generator 1 with after the heat exchange of the refrigerant concentrated solution of generator 1, starts subsequent cycle.
Working medium is equipped in Steam Power Circulation system, by being used as the absorber 5 of heater, expanding machine 8, as condenser
Evaporator 4, working medium pump 9, the absorber 5 as heater are connected in sequence with pipeline.The low boiling working fluid liquid of low-temp low-pressure
Body absorbs heat from the absorber 5 for being used as heat source, becomes high temperature and pressure working substance steam, high temperature and pressure working substance steam enters expansion
Expansion work in machine 8, steam exhaust enter the evaporator 4 as condenser, are subcooled and condense into worker quality liquid, worker quality liquid warp
Force (forcing) pump 9 is pressed into absorber 5, starts next round circulation.Expander acting output outward.
The dynamical system freezed from driving adsorption type heat pump is as shown in Fig. 2, by adsorption type heat pump cooling cycle system and steaming
Vapour power circulation system is constituted.
Heat pump refrigeration cycle system divides two-way, a routing 11 refrigerant end of adsorbent bed, valve 22, compressor 2, valve 20,
11 heat source side of adsorbent bed, valve 14, expenditure and pressure valve 3, evaporator 4, valve 18,24 refrigerant end of adsorbent bed and pipeline successively connect
It connects；One routing 24 refrigerant end of adsorbent bed, valve 17, compressor 2, valve 19,24 heat source side of adsorbent bed, valve 15, section
Stream pressure reducing valve 3, evaporator 4, valve 16,11 refrigerant end of adsorbent bed and pipeline are connected in sequence.Using working medium and to working medium
Adsorbent with adsorption capacity forms working medium pair, and filling is adsorbed with the adsorbent of a certain amount of working medium in the first adsorbent bed,
The few adsorbent of absorption working pair amount is packed into second adsorbent bed.The desorption of adsorbent bed 11,24 absorption phase of adsorbent bed, valve 22,
Valve 20, valve 14 are opened, and valve 19, valve 21, valve 12, valve 15 are closed, and the working medium of adsorbent bed 11 is driven steam and adds
Thermal desorption generates working substance steam, pressurizes and compresses through compressor 2, generates high temperature and pressure working substance steam, and high temperature and pressure working substance steam is returned
It flows to 11 heat source side of adsorbent bed and makees driving heat source, adsorbent bed 11 is heated, itself is condensed into liquid, throttles through throttling pressure reducing valve 3
Decompression is absorbed heat into evaporator 4 and is evaporated, provides low temperature, low pressure working fluid steam enters 24 exotherm of adsorbent bed.Adsorbent bed 24 solves
It inhales, 11 absorption phase of adsorbent bed, valve 17, valve 19, valve 15 are opened, and valve 22, valve 20, valve 14, valve 13 are closed.
From driving steam heat absorption evaporation in adsorbent bed 24, working substance steam is pressurizeed through compressor 2 to be compressed working medium, right into adsorbent bed 24
Adsorbent bed 24 heats, and driving working substance steam condenses into driving worker quality liquid, and driving worker quality liquid is through 3 expenditure and pressure of pressure reducing valve that throttles
Into adsorbent bed 11, the exotherm in adsorbent bed 11.
It is equipped with working medium in Steam Power Circulation system, divides two-way, a routing is used as adsorbent bed 11, the valve of evaporator
21, expanding machine 8, the evaporator 4 as condenser, working medium pump 9, valve 12, the adsorbent bed 11 as evaporator and pipeline be successively
Connection composition；One routing is used as adsorbent bed 24, valve 23, expanding machine 8, evaporator 4, the working medium pump as condenser of evaporator
9, valve 13, the adsorbent bed 24 as evaporator and pipeline are connected in sequence.The desorption of adsorbent bed 11, adsorbent bed 24 adsorb rank
Section, valve 23, valve 13 are opened, and valve 21, valve 19, valve 12, valve 15 are closed, and power worker quality liquid is being used as evaporator
Adsorbent bed 24 in absorb heat evaporation, generate high-pressure working medium steam, high-pressure working medium steam enters 8 expansion work of expanding machine, steam exhaust row
The evaporator 4 for entering to be used as condenser condenses into power worker quality liquid, power worker quality liquid is through work to refrigeration cycle working medium heat release
9 indentation of matter pump is used as the adsorbent bed 24 of evaporator, starts subsequent cycle.The desorption of adsorbent bed 24,11 absorption phase of adsorbent bed, valve
21, valve 14 is opened, and valve 20, valve 23, valve 15, valve 12 are closed, and power worker quality liquid is in the absorption for being used as evaporator
It absorbs heat and evaporates in bed 1, generate high-pressure working medium steam, high-pressure working medium steam enters 8 expansion work of expanding machine, and steam exhaust is discharged into as cold
The evaporator 4 of condenser condenses into power worker quality liquid to refrigeration cycle working medium heat release, and power worker quality liquid is pressed into through working medium pump 9
Adsorbent bed 1 as evaporator starts subsequent cycle.
Composite absorption heat pump refrigerant vapor dynamical system as shown in figure 3, system by absorption heat pump cooling cycle system
It is constituted with Steam Power Circulation system.
Absorption heat pump refrigeration cycle is made of driving circulation and absorption heat pump refrigeration cycle.
Driving circulation is connected in sequence by evaporator 4, condenser 10, evaporator 4 and pipeline.Refrigerating medium is in evaporator 4
In, it is absorbed when heat is by refrigerant liquid evacuator body in evaporator 4, after heat content reduces, into condenser 10, by condenser 10
In refrigerant vapour be cooled to liquid refrigerant, after itself heat absorption increasing enthalpy, into evaporator 4, start subsequent cycle.
Absorption heat pump refrigeration cycle is made of refrigerant circulation and solution circulation, and refrigerant circulation is by generator 1, condensation
Device 10, working medium elevator pump 27, evaporator 4, absorber 5, solution heat exchanger 6, generator 1 and pipeline are connected in sequence.Solution
Circulation is sequentially connected by generator 1, solution heat exchanger 6, liquid liquid pump 7, absorber 5, solution heat exchanger 6, generator 1 by pipeline
At circuit.In the heat pump refrigeration cycle system be equipped with working medium and in working medium the big material composition of solubility working medium to molten
Liquid.Refrigerant weak solution is heated by the steam exhaust of the Steam Power Circulation of the heat source of heat source section and cooling section respectively in generator 1
Evaporation generates refrigerant vapour, and concentrated solution, which enters after solution heat exchanger 6 exchanges heat with the weak solution from absorber 5 to enter, to be absorbed
Device 5, refrigerant vapour, which enters in condenser 10, is condensed into refrigerant liquid, and refrigerant liquid is lifted into steaming through working medium elevator pump
Device 4 is sent out, is evaporated to refrigerant vapour in the heat absorption of evaporator 4, refrigerant vapour enters absorber 5, the concentrated solution being absorbed in device 5
It absorbs, while heat is transmitted to the worker quality liquid of Steam Power Circulation, refrigerant weak solution and the system from generator 1 by heat release
Enter generator 1 after the heat exchange of cryogen concentrated solution, starts subsequent cycle.
Working medium is equipped in Steam Power Circulation system, by being used as the absorber 5 of evaporator, expanding machine 8, as condenser
Absorber 1, working medium pump 9, the absorber 5 as evaporator and pipeline are formed by connecting.Worker quality liquid from be used as heat source absorber 5
Middle absorption heat becomes working substance steam, and working substance steam enters expansion work in expansion machinery 8, and steam exhaust enters as condenser
In the cooling section of generator 1, the weak solution in generator is heated, refrigerant is evaporated, while itself cooling condenses into working medium
Liquid, the pressurized pump 9 of worker quality liquid are pressed into absorber 5, start next round circulation.Expansion machinery expansion work exports outward.
The dynamical system of composite adsorption heat pump refrigerating is as shown in figure 4, by adsorption type heat pump cooling cycle system and steam
Power circulation system is constituted.
Heat pump refrigeration cycle system is made of driving circulation, heat pump refrigeration cycle.
Driving circulation is connected in sequence by adsorbent bed 11, adsorbent bed 24, adsorbent bed 11 and pipeline；Adsorbent bed 11 desorbs,
24 absorption phase of adsorbent bed, refrigerant heat adsorbent bed 11, self-radiating in adsorbent bed 11, and heat content reduces；Subsequently into
Adsorbent bed 24 cools down adsorbent bed 24, itself heat absorption, heat content increases；Adsorbent bed 11 is entered back into, is so recycled.
Heat pump refrigeration cycle divides two-way, routing an adsorbent bed 11, valve 22, condenser 10, working medium elevator pump 27, evaporator
4, valve 18, adsorbent bed 24 and pipeline are connected in sequence；One routing adsorbent bed 24, valve 17, condenser 10, working medium elevator pump
27, evaporator 4, valve 16, adsorbent bed 11 and pipeline are connected in sequence.There is the suction of adsorption capacity using working medium and to working medium
Attached dose of composition working medium pair, filling is adsorbed with the adsorbent of a certain amount of working medium in the first adsorbent bed, fills in the second adsorbent bed
Enter the few adsorbent of absorption working pair amount.The desorption of adsorbent bed 11,24 absorption phase of adsorbent bed, valve 22, valve 18 are opened, valve
17, valve 16 is closed, and working medium, by heat source heating desorption, generates working substance steam in adsorbent bed 11, and working substance steam enters condenser
Worker quality liquid is condensed into 10, the boosted pump 27 of worker quality liquid is promoted, and into evaporator 4, the condensation segment in evaporator 4 is driven
The steam exhaust of power circulation, which is absorbed heat, evaporates, and continues to absorb heat in the low-temperature heat source section of evaporator 4 from low-temperature heat source, generates working substance steam, work
Matter steam enters adsorbent bed 24 and is adsorbed by adsorbent, while heat release.The desorption of adsorbent bed 24,11 absorption phase of adsorbent bed, valve 17,
Valve 16 is opened, and valve 22, valve 18 are closed, and working medium, by heat source stream heating desorption, generates working substance steam in adsorbent bed 24,
Working substance steam, which enters in condenser 10, is condensed into worker quality liquid, and the boosted pump 27 of worker quality liquid is promoted, and into evaporator 4, is steaming
It sends out the condensation segment in device 4 and absorbs heat from the steam exhaust of power cycle and evaporate, continue to inhale in the low-temperature heat source section of evaporator 4 from low-temperature heat source
Heat generates working substance steam, is adsorbed by adsorbent into adsorbent bed 11, while heat release.
Working medium is equipped in Steam Power Circulation system, by being used as the condenser 10 of evaporator, expanding machine 8, being used as condenser
Evaporator 4, working medium pump 9, the condenser 10 as evaporator and pipeline be connected in sequence.Power working medium is being used as evaporator
Condenser 10 in absorb heat evaporation, generate working substance steam, working substance steam enters the decompression of 8 expansion work of expanding machine, and steam exhaust is discharged into steaming
Device 4 is sent out, to refrigeration cycle working medium heat release, itself condenses into power worker quality liquid, power worker quality liquid is used as through the indentation of working medium pump 9
The condenser 10 of evaporator, wherein heat absorption evaporation, starts subsequent cycle.
Composite absorption heat pump refrigerant vapor dynamical system as shown in figure 5, device by absorption heat pump cooling cycle system
It is constituted with Steam Power Circulation system.
Absorption heat pump cooling cycle system is made of driving circulation and heat pump refrigeration cycle.
Driving circulation passes sequentially through pipeline by generator 1, absorber 5, generator 1 and connects into circuit.
Heat pump refrigeration cycle by refrigerant circulation and solution circulation constitute, refrigerant circulation by generator 1, condenser 10,
Expenditure and pressure valve 3, evaporator 4, absorber 5, solution pump 7, solution heat exchanger 6, generator 1 and pipeline are in turn connected into circuit,
Solution circulation passes through pipeline successively by generator 1, solution heat exchanger 6, absorber 5, solution pump 7, solution heat exchanger 6, generator 1
Connect into circuit.In the heat pump refrigeration cycle system be equipped with working medium and in working medium the big material composition of solubility working medium pair
Solution.Refrigerant weak solution is added by the steam exhaust of the Steam Power Circulation of the heat source of heat source section and cooling section respectively in generator 1
Thermal evaporation, generates refrigerant vapour, and concentrated solution enters suction after entering solution heat exchanger 6 and the weak solution heat exchange from absorber 5
Device 5 is received, refrigerant vapour, which enters in condenser 10, is condensed into refrigerant liquid, and refrigerant liquid subtracts through the throttling throttling of pressure reducing valve 3
Pressure is evaporated to refrigerant vapour in the heat absorption of evaporator 4, refrigerant vapour enters absorber 5, is absorbed device 5 into evaporator 4
In concentrated solution absorb, while heat is transmitted to the worker quality liquid of Steam Power Circulation by heat release, refrigerant weak solution with from
Enter generator 1 after the refrigerant concentrated solution heat exchange of generator 1, starts subsequent cycle.
Working medium is equipped in Steam Power Circulation system, by being used as the condenser 10 of evaporator, expanding machine 8, being used as condenser
Evaporator 4, working medium pump 9, the condenser 10 as evaporator and pipeline be formed by connecting.Worker quality liquid from be used as evaporator it is cold
Heat is absorbed in condenser 10, becomes working substance steam, working substance steam enters expansion work in expansion machinery 8, and steam exhaust enters as cold
In the cooling section of the evaporator 4 of condenser, conducts heat to the refrigerant liquid of Absorption Cooling System, evaporate refrigerant, while from
Body is cooling to condense into worker quality liquid, and pressurized 9 indentation of pump of worker quality liquid is used as in the condenser 10 of evaporator, starts next repeating query
Ring.8 expansion work of expanding machine exports outward.
Composite absorption heat pump refrigerant vapor dynamical system as shown in fig. 6, system by absorption heat pump cooling cycle system
It is constituted with Steam Power Circulation system.
Absorption heat pump refrigeration cycle is made of driving circulation and absorption heat pump refrigeration cycle.
Driving circulation by vapour compression machine 2, the generator 1 as condenser, expenditure and pressure valve 25, as the cold of evaporator
Condenser 10, compressor 2 and pipeline are formed by connecting.Low-voltage driving working substance steam is pressurizeed through compressor 2 to be compressed, and high drive work is generated
Matter steam makees driving heat source into the generator 1 for being used as condenser, and self-heat generation is condensed into driving worker quality liquid, drives working medium
Liquid is through 25 expenditure and pressure of pressure reducing valve that throttles, into the condenser 10 for being used as evaporator, wherein heat absorption evaporation, low-voltage driving work
Matter steam enters compressor 2, starts subsequent cycle.
Absorption heat pump refrigeration cycle is made of refrigerant circulation and solution circulation, and refrigerant circulation is by generator 1, condensation
Device 10, expenditure and pressure valve 3, evaporator 4, absorber 5, solution pump 7, solution heat exchanger 6, generator 1 and pipeline are in turn connected into
Circuit, solution circulation are successively led to by generator 1, solution heat exchanger 6, absorber 5, solution pump 7, solution heat exchanger 6, generator 1
Piping connects into circuit.Working medium and the big material composition of solubility in working medium are equipped in the heat pump refrigeration cycle system
Working medium is to solution.Refrigerant weak solution by high temperature heat source heating evaporation, generates refrigerant vapour in generator 1, concentrated solution into
Enter absorber 5 after entering solution heat exchanger 6 and the weak solution heat exchange from absorber 5, refrigerant vapour enters in condenser 10
It is condensed into refrigerant liquid, refrigerant liquid, which is throttled, enters evaporator 4 after 3 expenditure and pressure of pressure reducing valve, first in the cold of evaporator 4
The steam exhaust of solidifying Duan Zhongcong Steam Power Circulation, which is absorbed heat, evaporates, and moist steam goes successively to inhale from refrigerant in the refrigerating section of evaporator 4
Thermal evaporation is all vaporizated into low pressure refrigerant vapor, and low pressure refrigerant vapor enters absorber 5, the concentrated solution being absorbed in device 5
It absorbs, while heat is transmitted to the worker quality liquid of Steam Power Circulation, refrigerant weak solution and the system from generator 1 by heat release
Enter generator 1 after the heat exchange of cryogen concentrated solution, starts subsequent cycle.
Working medium is equipped in Steam Power Circulation system, by be used as the absorber 5 of evaporator, the evaporator 4 as condenser,
Expanding machine 8, working medium pump 9, the absorber 5 as evaporator and pipeline are formed by connecting.The low boiling working fluid liquid of low-temp low-pressure from
Heat is absorbed in absorber 5 as heat source, becomes high temperature and pressure working substance steam, high temperature and pressure working substance steam enters expansion machinery
Expansion work in 8, steam exhaust enter the evaporator 4 as condenser, are subcooled and condense into worker quality liquid, and worker quality liquid is through adding
Press pump 9 is pressed into absorber 5, starts next round circulation.Expansion machinery expansion work exports outward.
The dynamical system of composite adsorption heat pump refrigerating is as shown in fig. 7, by adsorption type heat pump cooling cycle system and steam
Power circulation system is constituted.
Heat pump refrigeration cycle system is made of driving circulation, heat pump refrigeration cycle.
Driving circulation divides two-way, a compressors 2, valve 20, the adsorbent bed 11 as condenser, valve 14, throttling
Pressure reducing valve 25, the condenser 10 as evaporator, compressor 2 and pipeline are connected in sequence.One compressors 2, valve 19,
Adsorbent bed 24, valve 15, expenditure and pressure valve 25 as condenser, the condenser 10 as evaporator, compressor 2 and pipeline according to
It is secondary to be formed by connecting.The desorption of adsorbent bed 11,24 absorption phase of adsorbent bed, valve 20, valve 14 are opened, valve 19, valve 21, valve
12, valve 15 is closed, and driving steam heats adsorbent bed 11, itself is condensed into liquid, driving worker quality liquid is through the pressure reducing valve that throttles
25 expenditure and pressures absorb evaporation in the condenser 10 for being used as evaporator, and working substance steam enters after compressor compresses are pressurizeed inhales
Attached bed 11 is used as driving heat source, so recycles.The desorption of adsorbent bed 24,11 absorption phase of adsorbent bed, valve 19, valve 15 are opened,
Valve 20, valve 13, valve 14, valve 23 are closed, and driving steam heats adsorbent bed 24, itself are condensed into liquid, drive work
Matter liquid absorbs heat into the condenser 10 for being used as evaporator and evaporates, working substance steam enters pressure through 25 expenditure and pressure of pressure reducing valve that throttles
Enter adsorbent bed 24 after the compression pressurization of contracting machine 2 and be used as driving heat source, so recycles.
Heat pump refrigeration cycle divides two-way, routing an adsorbent bed 11, valve 22, condenser 10, expenditure and pressure valve 3, evaporator
4, valve 18, adsorbent bed 24 and pipeline are connected in sequence；One routing adsorbent bed 24, valve 17, condenser 10, expenditure and pressure valve
3, evaporator 4, valve 16, adsorbent bed 11 and pipeline are connected in sequence.There is the suction of adsorption capacity using working medium and to working medium
Attached dose of composition working medium pair, filling is adsorbed with the adsorbent of a certain amount of working medium in the first adsorbent bed, fills in the second adsorbent bed
Enter the few adsorbent of absorption working pair amount.The desorption of adsorbent bed 11,24 absorption phase of adsorbent bed, valve 22, valve 18 are opened, valve
17, valve 16 is closed, and working medium, by heat source stream heating desorption, generates working substance steam in adsorbent bed 11, and working substance steam enters cold
Worker quality liquid is condensed into condenser 10, worker quality liquid is through 3 expenditure and pressure of pressure reducing valve that throttles, into evaporator 4, in evaporator 4
Condensation segment from the steam exhaust of power cycle absorb heat evaporate, continue evaporator 4 low-temperature heat source section from low-temperature heat source absorb heat, generate
Low pressure working fluid steam is adsorbed by adsorbent into adsorbent bed 24, while heat release.The desorption of adsorbent bed 24,11 absorption phase of adsorbent bed,
Valve 17, valve 16 are opened, and valve 22, valve 18 are closed, and working medium, by heat source stream heating desorption, generates work in adsorbent bed 24
Matter steam, working substance steam, which enters in condenser 10, is condensed into worker quality liquid, worker quality liquid through throttle 3 expenditure and pressure of pressure reducing valve, into
Enter evaporator 4, the condensation segment in evaporator 4 absorbs heat from the steam exhaust of power cycle and evaporates, and continues the low-temperature heat source in evaporator 4
Section is absorbed heat from low-temperature heat source, is generated low pressure working fluid steam, is adsorbed by adsorbent into adsorbent bed 11, while heat release.
It is equipped with working medium in Steam Power Circulation system, divides two-way, a routing is used as 24 heat source side of adsorbent bed of evaporator, valve
Door 23, expanding machine 8, the evaporator 4 as condenser, working medium pump 9, valve 13,24 heat source side of adsorbent bed and pipeline are sequentially connected
It forms；One routing is used as 11 heat source side of adsorbent bed of evaporator, valve 21, expanding machine 8, the evaporator 4 as condenser, working medium
Pump 9, valve 12,11 heat source side of adsorbent bed and pipeline are connected in sequence.The desorption of adsorbent bed 11,24 absorption phase of adsorbent bed, valve
Door 23, valve 13 are opened, and valve 19, valve 21, valve 12, valve 15 are closed, and power working medium is in the adsorbent bed for being used as evaporator
Middle heat absorption evaporation in 24, generates high-pressure working medium steam, and high-pressure working medium steam enters the decompression of 8 expansion work of expanding machine, and steam exhaust is discharged into
Evaporator 4 condenses into power worker quality liquid to refrigeration cycle working medium heat release, and power worker quality liquid is used as through the indentation of working medium pump 9 to be steamed
The adsorbent bed 24 of device is sent out, subsequent cycle is started.The desorption of adsorbent bed 24,11 absorption phase of adsorbent bed, valve 21, valve 12 are opened,
Valve 23, valve 13, valve 14, valve 20 are closed, and power working medium is absorbed heat in the adsorbent bed 11 for being used as evaporator and evaporated, and are generated
High-pressure working medium steam, high-pressure working medium steam enter the decompression of 8 expansion work of expanding machine, and steam exhaust is discharged into evaporator 4, to refrigeration cycle work
Matter heat release, condenses into power worker quality liquid, and power worker quality liquid is used as the adsorbent bed 11 of evaporator through the indentation of working medium pump 9, starts
Subsequent cycle.
The heat pump refrigerating dynamical system of thermal drivers is absorbed as shown in figure 8, by absorption formula heat pump refrigeration cycle system and steaming
Vapour power circulation system is constituted.
Heat pump refrigeration cycle system is made of driving circulation and heat pump refrigeration cycle.
Driving circulation is by being used as the generator 1 of condenser, expenditure and pressure valve 25, absorber 5, compressor 2, being used as condenser
Generator 1 and pipeline be connected in sequence.
Heat pump refrigeration cycle is made of refrigerant circulation and solution circulation, and refrigerant circulation is made by generator 1, condenser 10
Cryogen end, expenditure and pressure valve 3, evaporator 4, absorber 5, solution pump 7, solution heat exchanger 6, generator 1 and pipeline are sequentially connected
It forms, solution circulation is successively led to by generator 1, solution heat exchanger 6, absorber 5, solution pump 7, solution heat exchanger 6, generator 1
Piping connects into circuit.Working medium and the big material composition of solubility in working medium are equipped in the heat pump refrigeration cycle system
Working medium is to solution.Refrigerant working medium is heated in generator 1 by heat source stream, generates working substance steam, and working substance steam enters condensation
It is condensed into worker quality liquid in device 10, worker quality liquid is through 3 expenditure and pressure of pressure reducing valve that throttles, and condensation segment in evaporator 4 is from power
The steam exhaust of circulation, which is absorbed heat, evaporates, and continues to absorb heat in the low-temperature heat source section of evaporator 4 from low-temperature heat source, is all vaporizated into low pressure working fluid
Steam, low pressure working fluid steam enter the absorption of absorber 5, while heat release.Weak solution is pumped into solution heat exchanger 6 through solution pump 7 and comes
Enter generator 1 from after the concentrated solution heat exchange of generator 1, starts subsequent cycle.
Working medium is equipped in Steam Power Circulation system, by being used as the condenser 10 of evaporator, expanding machine 8, being used as condenser
Evaporator 4, working medium pump 9, the condenser 10 as evaporator and pipeline be connected in sequence.Power working medium is being used as evaporator
Condenser 10 in absorb heat evaporation, generate high-pressure working medium steam, high-pressure working medium steam enters expanding machine 8, and steam exhaust is discharged into as cold
The evaporator 4 of condenser condenses into power worker quality liquid to refrigeration cycle working medium heat release, and power worker quality liquid is pressed into through working medium pump 9
Condenser 10 as evaporator completes a circulation.
The adsorption type heat pump refrigeration dynamical system of thermal drivers is adsorbed as shown in figure 9, by adsorption type heat pump cooling cycle system
It is constituted with Steam Power Circulation system.
Heat pump refrigeration cycle is made of driving circulation, heat pump refrigeration cycle.
Driving circulation divides two-way, routing 24 heat source side of adsorbent bed, valve 23, compressor 2, valve 20,11 heat of adsorbent bed
Source, valve 12, expenditure and pressure valve 25,24 heat source side of adsorbent bed and pipeline are connected in sequence.One routing 11 heat source of adsorbent bed
End, valve 21, compressor 2, valve 19,24 heat source side of adsorbent bed, valve 15, expenditure and pressure valve 26,11 heat source side of adsorbent bed and
Pipeline is connected in sequence.Using working medium and to working medium there is the adsorbent of adsorption capacity to form working medium pair, in the first adsorbent bed
It is middle to fill the adsorbent for being adsorbed with a certain amount of working medium, the few adsorbent of absorption working pair amount is packed into the second adsorbent bed.Absorption
11 desorption of bed, 24 absorption phase of adsorbent bed, valve 23, valve 20, valve 12 are opened, and valve 19, valve 21, valve 15 are closed,
It drives steam to heat adsorbent bed 11, itself is condensed into liquid, driving worker quality liquid enters absorption through the throttling decompression of pressure reducing valve 25
Bed 24 absorbs absorption thermal evaporation in adsorbent bed 24, generates steam, and steam enters adsorbent bed 11 after the compression pressurization of compressor 2
As driving heat source, so recycle.The desorption of adsorbent bed 24,11 absorption phase of adsorbent bed, valve 21, valve 19, valve 15 are opened,
Valve 20, valve 12, valve 23 are closed, and driving steam heats adsorbent bed 24, itself are condensed into liquid, drive worker quality liquid section
26 expenditure and pressure of pressure reducing valve is flowed, evaporation of absorbing heat in adsorbent bed 11 generates steam, enters adsorbent bed through the pressurization compression of compressor 2
24 are used as driving heat source, so recycle.
Heat pump refrigeration cycle divides two-way, routing a 11 refrigerant end of adsorbent bed, valve 22, condenser 10, expenditure and pressure valve
3, evaporator 4, valve 18,24 refrigerant end of adsorbent bed are connected in sequence through pipeline；One routing 24 refrigerant end of adsorbent bed, valve
Door 17, condenser 10, expenditure and pressure valve 3, evaporator 4, valve 16,11 refrigerant end of adsorbent bed are connected in sequence through pipeline.
The desorption of adsorbent bed 11,24 absorption phase of adsorbent bed, valve 22, valve 18 are opened, and valve 17, valve 16 are closed, and working medium is being adsorbed
By heat source stream heating desorption in bed 11, working substance steam is generated, working substance steam, which enters in condenser 10, is condensed into worker quality liquid, work
Matter liquid is through 3 expenditure and pressure of pressure reducing valve that throttles, and into evaporator 4, the condensation segment in evaporator 4 is inhaled from the steam exhaust of power cycle
Thermal evaporation continues to absorb heat in the low-temperature heat source section of evaporator 4 from low-temperature heat source, low pressure working fluid steam is all vaporizated into, into suction
Attached bed 24 is adsorbed by adsorbent, while heat release.The desorption of adsorbent bed 24,11 absorption phase of adsorbent bed, valve 17, valve 16 are opened,
Valve 22, valve 18 are closed, and working medium by heat source stream heating desorption, generates working substance steam in adsorbent bed 24, working substance steam into
Enter and be condensed into worker quality liquid in condenser 10, worker quality liquid is through 3 expenditure and pressure of pressure reducing valve that throttles, into evaporator 4, in evaporator
Condensation segment in 4 absorbs heat from the steam exhaust of power cycle to be evaporated, and continues to absorb heat in the low-temperature heat source section of evaporator 4 from low-temperature heat source,
Low pressure working fluid steam is generated, is adsorbed by adsorbent into adsorbent bed 11, while heat release.
Working medium is equipped in Steam Power Circulation system, by being used as the condenser 10 of evaporator, expanding machine 8, being used as condenser
Evaporator 4, working medium pump 9 form.Power working medium is absorbed heat in the condenser 10 for being used as evaporator and is evaporated, and generates high-pressure working medium and steams
Vapour, high-pressure working medium steam enter the decompression of 8 expansion work of expanding machine, and steam exhaust is discharged into evaporator 4, to refrigeration cycle working medium heat release, coagulate
Form power worker quality liquid, power worker quality liquid is used as the condenser 10 of evaporator through the indentation of working medium pump 9, starts subsequent cycle.
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the invention, it is all in spirit of the invention and
Within principle, any modification, equivalent replacement, improvement and so on be should all be included in the protection scope of the present invention.
Claims (9)
1. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
State heat pump refrigeration cycle system by refrigerant circulation and solution circulation form, the refrigerant circulation by generator (1) refrigeration
Agent end, compressor (2), generator (1), the second expenditure and pressure valve (3), evaporator (4), absorber (5), solution pump (7), solution
Heat exchanger (6), generator (1) refrigerant end circuit is in turn connected by pipeline, the solution circulation by generator (1),
Solution heat exchanger (6), absorber (5), solution pump (7), solution heat exchanger (6), generator (1) are in turn connected into back by pipeline
Road；The Steam Power Circulation system is by the absorber (5), expanding machine (8), evaporator (4), working medium pump (9), absorber
(5) another circuit is in turn connected by pipeline, the heat pump refrigeration cycle system is equipped with working medium and solubility is big in working medium
Material composition working medium to solution, working medium is equipped in the Steam Power Circulation system.
2. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
It states heat pump refrigeration cycle system and divides two-way, the refrigerant end of a routing the first adsorbent bed (11), the first valve (22), compressor
(2), the second valve (20), the heat source side of the first adsorbent bed (11), third valve (14), the second expenditure and pressure valve (3), evaporator
(4), the 4th valve (18), the second adsorbent bed (24) refrigerant end are connected in sequence by pipeline；Another way is by the second absorption
The bed refrigerant end of (24), the 5th valve (17), compressor (2), the 6th valve (19), the second adsorbent bed (24) heat source side,
7th valve (15), the second expenditure and pressure valve (3), evaporator (4), the 8th valve (16), the first adsorbent bed (11) refrigerant
End is connected in sequence by pipeline, and the heat pump refrigeration cycle system has the absorption of adsorption capacity using working medium and to working medium
Agent forms working medium pair, and filling is adsorbed with the adsorbent of a certain amount of working medium in the first adsorbent bed (11), in the second adsorbent bed (24)
In be packed into the few adsorbent of absorption working pair amount, the Steam Power Circulation system is also classified into two-way, first adsorbent bed of routing
(11), the 9th valve (21), expanding machine (8), evaporator (4), working medium pump (9), the 12nd valve (12), the first adsorbent bed (11)
Primary Ioops are in turn connected by pipeline；One routing the second adsorbent bed (24), the tenth valve (23), expanding machine (8), evaporator
(4), working medium pump (9), the 11st valve (13), the second adsorbent bed (24) are in turn connected into another circuit, the steaming by pipeline
Working medium is equipped in vapour power circulation system.
3. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
It states heat pump refrigeration cycle system to be made of driving circulation and heat pump refrigeration cycle, the driving circulation is by evaporator (4), condenser
(10), evaporator (4) is in turn connected into circuit by pipeline, and the heat pump refrigeration cycle recycles structure by refrigerant circulation and solution
At, the refrigerant circulation by generator (1), condenser (10), working medium elevator pump (27), evaporator (4), absorber (5), molten
Liquid pump (7), solution heat exchanger (6), generator (1) are in turn connected into circuit by pipeline, and the solution circulation is by generator
(1), solution heat exchanger (6), liquid liquid pump (7), absorber (5), solution heat exchanger (6), generator (1) are sequentially connected by pipeline
At circuit, in the heat pump refrigeration cycle system equipped with refrigerant and in the refrigerant the biggish material composition of solubility it is molten
Liquid；Working medium is equipped in the Steam Power Circulation system, by being used as the absorber (5) of evaporator, expanding machine (8), being used as condensation
Generator (1), working medium pump (9), the absorber (5) as evaporator of device are in turn connected into circuit by pipeline.
4. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
Heat pump refrigeration cycle system is stated to be made of driving circulation and heat pump refrigeration cycle, the driving recycle by the first adsorbent bed (11),
Second adsorbent bed (24), the first adsorbent bed (11) are in turn connected into circuit by pipeline, and the heat pump refrigeration cycle divides two-way, and one
Route the first adsorbent bed (11), the first valve (22), condenser (10), working medium elevator pump (27), evaporator (4), the 4th valve
(18), the second adsorbent bed (24) and pipeline are connected in sequence；One routing the second adsorbent bed (24), the 5th valve (17), condensation
Device (10), working medium elevator pump (27), evaporator (4), the 8th valve (16), the first adsorbent bed (11) are sequentially connected by pipeline
At the heat pump refrigeration cycle system is equipped with working medium and there is the adsorbent of adsorption capacity to form working medium pair working medium, described
Filling is adsorbed with the adsorbent of a certain amount of working medium in first adsorbent bed (11), is packed into absorption in second adsorbent bed (24)
The few adsorbent of working medium amount, the Steam Power Circulation system is interior to be equipped with working medium, by the condenser (10), the expansion that are used as evaporator
Machine (8), the evaporator (4) as condenser, working medium pump (9), the condenser (10) as evaporator are sequentially connected by pipeline
At circuit.
5. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
It states heat pump refrigeration cycle system to be made of driving circulation and heat pump refrigeration cycle, the driving circulation is by generator (1), absorber
(5), generator (1) is in turn connected into circuit by pipeline；The heat pump refrigeration cycle recycles structure by refrigerant circulation and solution
At the refrigerant circulation is by generator (1), condenser (10), the second expenditure and pressure valve (3), evaporator (4), absorber
(5), solution pump (7), solution heat exchanger (6), generator (1) are in turn connected into circuit by pipeline, and the solution circulation is by sending out
Raw device (1), solution heat exchanger (6), absorber (5), solution pump (7), solution heat exchanger (6), generator (1) pass through pipeline successively
Connect into circuit, in the heat pump refrigeration cycle system equipped with refrigerant and in the refrigerant the biggish material composition of solubility
Solution；Working medium is equipped in the Steam Power Circulation system, by be used as the condenser (10) of evaporator, expanding machine (8), be used as it is cold
Evaporator (4), working medium pump (9), the condenser (1) 0 as evaporator of condenser are in turn connected into circuit by pipeline.
6. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
It states heat pump refrigeration cycle system to be made of driving circulation and heat pump refrigeration cycle, the driving circulation is by compressor (2), generator
(1), first throttle pressure reducing valve (25), condenser (10), compressor (2) connect into circuit by pipeline, and the heat pump refrigerating follows
Ring is made of refrigerant circulation and solution circulation, and the refrigerant circulation is subtracted by generator (1), condenser (10), the second throttling
Pressure valve (3), evaporator (4), absorber (5), solution pump (7), solution heat exchanger (6), generator (1) are sequentially connected by pipeline
At circuit, the solution circulation is by generator (1), solution heat exchanger (6), absorber (5), solution pump (7), solution heat exchanger
(6), generator (1) is in turn connected into circuit by pipeline, and refrigerant is equipped in the heat pump refrigeration cycle system and is being freezed
The solution of the biggish material composition of solubility in agent；It is equipped with working medium in the Steam Power Circulation system, by absorber (5), steams
Hair device (4), expanding machine (8), working medium pump (9), absorber (5) are in turn connected into circuit by pipeline.
7. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
It states heat pump refrigeration cycle system to be made of driving circulation and heat pump refrigeration cycle, the driving circulation divides two-way, a routing compaction
Machine (2), the second valve (20), the first adsorbent bed (11), third valve (14), first throttle pressure reducing valve (25), condenser (10),
Compressor (2) is in turn connected into circuit, another compressors (2), the 6th valve (19), the second adsorbent bed by pipeline
(24), the 7th valve (15), first throttle pressure reducing valve (25), condenser (10), compressor (2) are in turn connected into back by pipeline
Road；The heat pump refrigeration cycle divides two-way, routing the first adsorbent bed (11), the first valve (22), condenser (10), the second section
Stream pressure reducing valve (3), evaporator (4), the 4th valve (18), the second adsorbent bed (24) are connected in sequence by pipeline, another way
By the second adsorbent bed (24), the 5th valve (17), condenser (10), the second expenditure and pressure valve (3), evaporator (4), the 8th valve
(16), the first adsorbent bed (11) is connected in sequence by pipeline, and the heat pump refrigeration cycle system is equipped with working medium and to working medium
Adsorbent with adsorption capacity forms working medium pair, and filling is adsorbed with the suction of a certain amount of working medium in first adsorbent bed (11)
Attached dose, the few adsorbent of absorption working pair amount is packed into second adsorbent bed (24)；In the Steam Power Circulation system
Equipped with working medium, also divide two-way, routing the second adsorbent bed (24), the tenth valve (23), expanding machine (8), evaporator (4), working medium
Pump (9), the 11st valve (13), the second adsorbent bed (24) are connected in sequence by pipeline；Another way is by the first adsorbent bed
(11), the 9th valve (21), expanding machine (8), evaporator (4), working medium pump (9), the 12nd valve (12), the first adsorbent bed (11)
It is connected in sequence by pipeline.
8. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
It states heat pump refrigeration cycle system to be made of driving circulation and heat pump refrigeration cycle, the driving circulation is by generator (1), first segment
Stream pressure reducing valve (25), absorber (5), compressor (2), generator (1) are in turn connected into circuit by pipeline；The heat pump refrigerating
Circulation is made of refrigerant circulation and solution circulation, and the refrigerant circulation is by generator (1), condenser (10), the second throttling
Pressure reducing valve (3), evaporator (4), absorber (5), solution pump (7), solution heat exchanger (6), generator (1) are successively connected by pipeline
It is connected into circuit, the solution circulation is by generator (1), solution heat exchanger (6), absorber (5), solution pump (7), solution heat exchanger
(6), generator (1) is in turn connected into circuit by pipeline, and refrigerant is equipped in the heat pump refrigeration cycle system and is being freezed
The solution of the biggish material composition of solubility in agent；Working medium is equipped in the Steam Power Circulation system, by condenser (10), swollen
Swollen machine (8), evaporator (4), working medium pump (9), condenser (10) are in turn connected into circuit by pipeline.
9. a kind of provide steam driven method, including heat pump refrigeration cycle system and Steam Power Circulation system, feature exist
In: the heat pump refrigeration cycle system drives the heat pump refrigerating by recycling steam condensation latent heat as driving heat source
The circulatory system, the heating heat using the high temperature heat source that the heat pump refrigeration cycle system exports as the Steam Power Circulation system
Source, condensation heat source of the low-temperature heat source exported using the heat pump refrigeration cycle system as the Steam Power Circulation system, institute
It states heat pump refrigeration cycle system to be made of driving circulation and heat pump refrigeration cycle, the driving circulation divides two-way, a routing second
Adsorbent bed (24), the tenth valve (23), compressor (2), the second valve (20), the first adsorbent bed (11), the 12nd valve (12),
First throttle pressure reducing valve (25), the second adsorbent bed (24) are in turn connected into circuit by pipeline；Another way is by the first adsorbent bed
(11), the 9th valve (21), compressor (2), the 6th valve (19), the second adsorbent bed (24), the 7th valve (15), third throttling
Pressure reducing valve (26), the first adsorbent bed (11) are in turn connected into circuit by pipeline；The heat pump refrigeration cycle also divides two-way, all the way
By the first adsorbent bed (11), the first valve (22), condenser (10), the second expenditure and pressure valve (3), evaporator (4), the 4th valve
(18), the second adsorbent bed (24) is connected in sequence by pipeline；Another way by the second adsorbent bed (24), the 5th valve (17),
Condenser (10), the second expenditure and pressure valve (3), evaporator (4), the 8th valve (16), the first adsorbent bed (11) by pipeline according to
Secondary to be formed by connecting, the heat pump refrigeration cycle system is equipped with working medium and there is the adsorbent of adsorption capacity to form working medium working medium
Right, filling is adsorbed with the adsorbent of a certain amount of working medium in the first adsorbent bed, and absorption working pair amount is packed into the second adsorbent bed
Few adsorbent；Working medium is equipped in the Steam Power Circulation system, by condenser (10), expanding machine (8), evaporator (4) and
Working medium pump (9) is connected in sequence by pipeline.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410280243.5A CN104061710A (en) | 2014-06-23 | 2014-06-23 | Method for providing steam power and device thereof |
| CN2014102802435 | 2014-06-23 | ||
| PCT/CN2015/079571 WO2015196881A1 (en) | 2014-06-23 | 2015-05-22 | Method for providing steam power |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106170668A CN106170668A (en) | 2016-11-30 |
| CN106170668B true CN106170668B (en) | 2019-04-09 |
Family
ID=51549549
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410280243.5A Pending CN104061710A (en) | 2014-06-23 | 2014-06-23 | Method for providing steam power and device thereof |
| CN201580010306.8A Active CN106170668B (en) | 2014-06-23 | 2015-05-22 | It is a kind of that steam driven method is provided |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410280243.5A Pending CN104061710A (en) | 2014-06-23 | 2014-06-23 | Method for providing steam power and device thereof |
Country Status (2)
| Country | Link |
|---|---|
| CN (2) | CN104061710A (en) |
| WO (1) | WO2015196881A1 (en) |
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104061710A (en) * | 2014-06-23 | 2014-09-24 | 周永奎 | Method for providing steam power and device thereof |
| CN104034083A (en) * | 2014-06-23 | 2014-09-10 | 周永奎 | Self-driven thermocompression heat pump cooling method and device |
| CN104048450A (en) * | 2014-06-23 | 2014-09-17 | 周永奎 | Absorption type heat pump refrigeration and power combined supply method and device thereof |
| CN107420171B (en) * | 2017-05-16 | 2023-07-18 | 新奥能源动力科技（上海）有限公司 | A waste heat utilization system of an internal combustion engine |
| CN107525307A (en) * | 2017-09-22 | 2017-12-29 | 北京华清微拓节能技术股份公司 | System and method for recovered material waste heat |
| CN108036506A (en) * | 2017-12-27 | 2018-05-15 | 清华大学 | A kind of direct combustion type heat-pump hot-water preparation facilities |
| CN108825320A (en) * | 2018-09-11 | 2018-11-16 | 翁志远 | A kind of cryogenic fluid electricity generation system and dynamical system |
| CN110700903A (en) * | 2018-10-08 | 2020-01-17 | 李华玉 | Single working medium combined cycle steam power device |
| CN109707472B (en) * | 2019-02-28 | 2021-10-22 | 东北大学 | A distributed energy system utilizing CDQ waste heat |
| CN110206602B (en) * | 2019-05-23 | 2022-01-11 | 中国能源建设集团广东省电力设计研究院有限公司 | Thermoelectric system based on nuclear power station and control method thereof |
| CN110057129B (en) * | 2019-05-29 | 2024-03-08 | 北京华电东晟科技有限公司 | Coupling heat pump heat exchanger |
| CN110344898B (en) * | 2019-08-05 | 2024-04-23 | 上海发电设备成套设计研究院有限责任公司 | Absorption type sea water desalination and closed cycle power generation system |
| CN111141047A (en) * | 2020-01-22 | 2020-05-12 | 天津商业大学 | A solar energy absorption cascade carbon dioxide two-stage compression refrigeration system |
| CN111594280B (en) * | 2020-06-23 | 2023-09-19 | 南京天加能源科技有限公司 | Dual-turbine gas suspension ORC power generation system and control method |
| CN112717448A (en) * | 2020-11-20 | 2021-04-30 | 郑喜勋 | Low boiling point working medium compression secondary steam device |
| CN113818941A (en) * | 2021-09-18 | 2021-12-21 | 广东省现代农业装备研究所 | High-efficiency refrigeration method and device |
| CN113931710A (en) * | 2021-10-20 | 2022-01-14 | 郑小涛 | Combined cooling and power generation system |
| CN113883909B (en) * | 2021-11-11 | 2024-11-12 | 西安热工研究院有限公司 | A composite cycle device and method for utilizing flue gas waste heat |
| CN114034138B (en) * | 2021-11-11 | 2025-03-11 | 西安热工研究院有限公司 | A system and method for improving the back pressure of an indirect air-cooling unit during summer operation |
| CN114000998B (en) * | 2021-11-30 | 2025-01-28 | 中国华能集团清洁能源技术研究院有限公司 | A carbon dioxide power generation device and a working method thereof |
| CN113982715B (en) * | 2021-12-09 | 2025-01-24 | 中国华能集团清洁能源技术研究院有限公司 | A combined heat and power generation device and method for coupling carbon dioxide power generation and geothermal energy |
| CN114251860A (en) * | 2021-12-29 | 2022-03-29 | 常州金坛金能电力有限公司 | High-pressure heat pump to produce steam and simultaneously refrigerate |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2949213A1 (en) * | 1979-12-04 | 1981-06-11 | Günther 1000 Berlin Bernburg | Heat pump with atmosphere as source - has output raising steam to drive turbine with low overall energy losses |
| JPS61123703A (en) * | 1984-11-21 | 1986-06-11 | Toshiba Corp | Steam power plant |
| CN1891980A (en) * | 2005-07-04 | 2007-01-10 | 陈培豪 | Steam Power Cycles and Plants |
| CN1940254A (en) * | 2005-09-29 | 2007-04-04 | 罗桂荣 | Composite thermodynamic engine of power circulation system and refrigerating circulation system |
| CN1954134A (en) * | 2004-06-01 | 2007-04-25 | 正田登 | Highly efficient heat cycle device |
| DE102011108260A1 (en) * | 2011-07-24 | 2013-01-24 | Paul-Gerhard Kanis | Steam power plant has external heat pump to receive heat from ambient air and set heat to higher temperature level, so as to preheat feed water |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5272878A (en) * | 1992-12-10 | 1993-12-28 | Schlichtig Ralph C | Azeotrope assisted power system |
| WO2012116174A1 (en) * | 2011-02-23 | 2012-08-30 | Jianguo Xu | Thermally activated pressure booster for heat pumping and power generation |
| CN104061710A (en) * | 2014-06-23 | 2014-09-24 | 周永奎 | Method for providing steam power and device thereof |
-
2014
- 2014-06-23 CN CN201410280243.5A patent/CN104061710A/en active Pending
-
2015
- 2015-05-22 WO PCT/CN2015/079571 patent/WO2015196881A1/en active Application Filing
- 2015-05-22 CN CN201580010306.8A patent/CN106170668B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2949213A1 (en) * | 1979-12-04 | 1981-06-11 | Günther 1000 Berlin Bernburg | Heat pump with atmosphere as source - has output raising steam to drive turbine with low overall energy losses |
| JPS61123703A (en) * | 1984-11-21 | 1986-06-11 | Toshiba Corp | Steam power plant |
| CN1954134A (en) * | 2004-06-01 | 2007-04-25 | 正田登 | Highly efficient heat cycle device |
| CN1891980A (en) * | 2005-07-04 | 2007-01-10 | 陈培豪 | Steam Power Cycles and Plants |
| CN1940254A (en) * | 2005-09-29 | 2007-04-04 | 罗桂荣 | Composite thermodynamic engine of power circulation system and refrigerating circulation system |
| DE102011108260A1 (en) * | 2011-07-24 | 2013-01-24 | Paul-Gerhard Kanis | Steam power plant has external heat pump to receive heat from ambient air and set heat to higher temperature level, so as to preheat feed water |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2015196881A1 (en) | 2015-12-30 |
| CN106170668A (en) | 2016-11-30 |
| CN104061710A (en) | 2014-09-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106170668B (en) | It is a kind of that steam driven method is provided | |
| CN106170669B (en) | A kind of absorption heat pump refrigeration power method of combined supply | |
| CN105180515B (en) | A kind of multipurpose pumping system | |
| CN104929706B (en) | Combined cycle energy supplying system | |
| CN103983036B (en) | A kind of CO2 reclaimed for afterheat of IC engine circulates polygenerations systeme | |
| CN108119194A (en) | Triple combined circulation power apparatus | |
| CN104963732B (en) | Combined cycle energy supplying system | |
| CN104929704B (en) | Combined cycle energy supplying system | |
| CN103233821B (en) | An air temperature regulation system | |
| CN202133176U (en) | A Two-Stage Jet Refrigeration Cycle System with Economizer | |
| CN102230702B (en) | Two-stage ejection refrigeration cycle system with economizer | |
| CN101586482B (en) | Low-temperature engine and engine heat regeneration method | |
| CN111735237A (en) | A medium and low temperature heat energy utilization power-cooling combined supply system | |
| CN105019954B (en) | Combined cycle energy supplying system | |
| CN107288695A (en) | A kind of environmentally friendly temp difference engine | |
| CN204141888U (en) | Organic Rankine-air injection enthalpy-increasing the vapour compression refrigeration system of Driven by Solar Energy | |
| CN202501677U (en) | Vapor Compression Refrigeration Device Driven by Organic Rankine Cycle | |
| CN205536641U (en) | Realize heat endless thermodynamic cycle system through environment working medium | |
| CN105783300B (en) | The thermodynamic cycle system and application of recycle heat are realized by environment working medium | |
| RU2643878C1 (en) | Method of operation of the compressed-air power station with an absorption lithium bromide refrigerating system (lbrs) | |
| CN116006283A (en) | Low-grade heat energy comprehensive utilization system | |
| CN106152599B (en) | 4th class thermal drivers compressing-absorbing type heat pump | |
| CN101430145A (en) | Air pressure-thermal power expansion type circulating method and apparatus | |
| CN110206699A (en) | It is a kind of using low-grade composite heat power supply as the thermal cycle electricity generation system of energy | |
| CN105351111B (en) | Air energy engine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201104 Address after: 244000 No.118, block B, high tech entrepreneurship service center, Tongling Economic Development Zone, Anhui Province Patentee after: Tongwei Technology Co.,Ltd. Tongling City Address before: 644007 Yibin province Sichuan City Cuiping District Jiuzhou Road No. 23 Patentee before: Zhou Yongkui |