CN106595117A - Heat pump system - Google Patents
Heat pump system Download PDFInfo
- Publication number
- CN106595117A CN106595117A CN201611223694.0A CN201611223694A CN106595117A CN 106595117 A CN106595117 A CN 106595117A CN 201611223694 A CN201611223694 A CN 201611223694A CN 106595117 A CN106595117 A CN 106595117A
- Authority
- CN
- China
- Prior art keywords
- heat
- subsystem
- compressor
- working medium
- valve
- 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.)
- Pending
Links
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
- F25B13/00—Compression machines, plants or systems, with reversible cycle
-
- 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
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/02—Compression-sorption machines, plants, or systems
-
- 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
- F25B27/002—Machines, plants or systems, using particular sources of energy using solar energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/003—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
-
- 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
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
-
- 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
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control valves
-
- 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
-
- 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
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/027—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
- F25B2313/02741—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using one four-way valve
-
- 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]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
The invention provides a heat pump system which comprises a solar power hot water subsystem, an air-conditioner heat-exchange working medium circulation subsystem and an absorption type circulation subsystem. The absorption type circulation subsystem comprises a solution generator, a first condenser, a first throttle valve, a first evaporator and an absorber; the solution generator and the absorber are connected through two pipelines and form a refrigeration working medium circulation circuit; and the solution generator, the first condenser, the first throttle valve, the first evaporator and the absorber are sequentially connected. The air-conditioner heat-exchange working medium circulation subsystem comprises a four-way valve, a compressor and a subcooler, an outlet pipeline of the compressor is connected with a first valve port of the four-way valve, a pipeline of the solar power hot water subsystem and the outlet pipeline of the compressor both penetrate through the solution generator, and the subcooler is coupled to the first evaporator. According to the heat pump system, the solar power, wind energy and electric energy are utilized efficiently fully and complementally to drive an air conditioner to conduct refrigerating and heating, and electricity network pressure in the peak time of electricity using is effectively alleviated.
Description
Technical field
The present invention relates to a kind of heat pump, more particularly to a kind of heat pump using regenerative resource.
Background technology
World energy sources structure accounts for the 85% of energy resource consumption total amount based on the fossil energies such as oil, natural gas, coal at present,
Fossil energy eventually can be exhausted, while also bringing serious environmental problem.The building trade power consumption of current China accounts for national total energy
The 30% of consumption, with the quickening and the improvement of people's living standard of urbanization process, architectural energy consumption ratio finally will also rise to
35% or so, architectural energy consumption has become the weakness of China's economic development.Wherein, air-conditioning power consumption accounts for the half of architectural energy consumption again
More than, and the air conditioning electricity time concentrate, directly result in that peak of power consumption period electrical network pressure is big, supply of electric power wretched insufficiency.And
The Renewable resources such as solar energy, wind energy are not effectively used.In addition, either wind energy or solar energy all receive the time
And climate change effect, it is not sufficiently stable, single energy utilization type has which not enough, therefore efficiently, fully, complementally
Using regenerative resources such as solar energy, wind energies, for improving environmental quality and greening building energy saving system development is extremely important.
The content of the invention
To solve above-mentioned technical problem, it is an object of the invention to provide a kind of heat pump, the heat pump can be high
Effect effectively alleviates the electrical network pressure of peak times of power consumption fully and complementally using regenerative resource driving air conditioner refrigerating to heat.
Based on this, the present invention proposes a kind of heat pump, including the circulation of solar heat water subsystem, air-conditioning heat-exchange working medium
Subsystem and Absorption heat-transformer subsystem, the Absorption heat-transformer subsystem include solution generator, the first condenser, first segment
Stream valve, the first vaporizer and absorber, are connected and shape by two pipelines between the solution generator and the absorber
Into refrigeration working medium closed circuit, and the solution generator, first condenser, the first throttle valve, described first steam
Send out device and the absorber is sequentially connected, the pipeline of the solar heat water subsystem passes through the solution generator, the sky
Exchange hot working fluid cycle subsystem and include cross valve, compressor and subcooler, the export pipeline of the compressor and described four
Port valve is connected, and the export pipeline passes through the solution generator, the subcooler and the first vaporizer phase mutual coupling
Close.
Optionally, the Absorption heat-transformer subsystem includes solution heat exchanger, and described two pipelines are through described molten
Liquid heat exchanger.
Further, circulating pump is additionally provided with the refrigeration working medium closed circuit.
Optionally, the air-conditioning heat-exchange working medium cycle subsystem includes the second condenser, the first check valve, second throttle
With the second vaporizer, it is and the compressor, the cross valve, second condenser, first check valve, described supercool
Device, the second throttle and second vaporizer are sequentially connected and form first circulation loop.
Optionally, the air-conditioning heat-exchange working medium cycle subsystem includes the second check valve and the 3rd choke valve, described first
Check valve is connected in parallel with the 3rd choke valve, and second check valve is connected in parallel with the second throttle, is made described
Compressor, the cross valve, second vaporizer, second check valve, the subcooler, the 3rd choke valve and institute
State the second condenser to be sequentially connected and form second circulation loop.
Further, the heat pump also includes motor, and the motor passes through the first drive mechanism and the compressor
It is connected.
Optionally, the heat pump also includes wind energy conversion system, and the wind energy conversion system is connected with the compressor.
Further, the heat pump also includes the second drive mechanism and transducer, and the wind energy conversion system, described second pass
Motivation structure, the transducer and the compressor are sequentially connected and connect.
Optionally, the solar heat water subsystem includes heat collector, water pump and storage tank, the heat collector, the water
Pump and the storage tank are sequentially connected and form closed circuit.
Optionally, the connecting line between the water pump and the storage tank is through the solution generator.
Implement the embodiment of the present invention, have the advantages that:
The heat pump of the present invention includes solar heat water subsystem, air-conditioning heat-exchange working medium cycle subsystem and absorption follows
Loop subsystems, the Absorption heat-transformer subsystem include solution generator, the first condenser, first throttle valve, the first vaporizer,
Absorber and circulating pump, are connected and form refrigeration working medium by two pipelines between the solution generator and the absorber
Closed circuit, and the solution generator, first condenser, the first throttle valve, first vaporizer, the suction
Receive device to be sequentially connected, wherein, the cooled water-cooled of the first condensers of vapor Jing in solution generator is congealed into water, through first segment
Enter in the first vaporizer, as the first vaporizer and subcooler intercouple after stream valve blood pressure lowering, inhale can low pressure condensed water
Evaporate after the heat for receiving the refrigerant liquid in air-conditioning heat-exchange working medium cycle subsystem;In addition, evaporate in the first vaporizer
Vapor is entered in absorber, is absorbed by refrigeration working medium, and the solution in absorber absorbs the steam from the first vaporizer out
Become weak solution, weak solution enters solution generator, steam is produced by thermal source heating again and forms concentrated solution again, started next
The circulation of wheel;Due to being connected and being formed refrigeration working medium closed circuit between solution generator and absorber by two pipelines,
Concentrated solution in instant liquid generator also can be entered in absorber, absorbed the steam in the first vaporizer by absorber and become
Into weak solution, continue supply work.The pipeline of the solar heat water subsystem passes through the solution generator, can be solution
Solution in generator provides heat, promotes the solution in solution generator to be heated and produces steam formation concentrated solution, is system
Further work provides condition;And solar heat water subsystem effectively make use of solar energy source, circulate with air-conditioning heat-exchange working medium
Subsystem works, and can form the utilization form of various energy resources, very flexibly.The air-conditioning heat-exchange working medium cycle subsystem
Cross valve, compressor and subcooler are included, the export pipeline of the compressor is connected with the cross valve, and the compression
The export pipeline of machine can enter to the high-temperature high-pressure refrigerant discharged in compressor through the solution generator, solution generator
Row pre-cooling, facilitates the work of next step, and the solution generator be respectively cooperating with the air-conditioning heat-exchange working medium cycle subsystem and
Absorption heat-transformer subsystem cooperation, quality when ensure that heat pump refrigeration or heating work, makes whole system
Functional reliability is higher.The subcooler is intercoupled with first vaporizer, and it is supercool with described to state the first vaporizer
Device be coupled after device, can either be for Absorption heat-transformer subsystem work, also can be for air-conditioning heat-exchange working medium cycle subsystem work
Make, it is ensured that in the case of solar energy or other driving source deficiencies, Absorption heat-transformer subsystem and air-conditioning heat-exchange working medium are circulated
Subsystem also can be worked simultaneously, reliably be efficiently completed refrigeration or the work for heating, and two kinds circulate the mode energy being coupled
Enough make hot water temperature lower than the temperature under simple subprogram mode, so as to reduce the requirement to heat collector, increase substantially overall system
The COP of system.
Further, the Absorption heat-transformer subsystem includes solution heat exchanger, and described two pipelines are through described
Circulating pump is additionally provided with solution heat exchanger, and the refrigeration working medium closed circuit, in refrigeration working medium closed circuit, solution
The concentrated solution that generator flows out is flow automatically in absorber after solution heat exchanger cooling, blood pressure lowering, can cool down in absorber
Solution temperature, during this is conducive to from the first vaporizer the solution that the steam for coming incorporates intermediate concentration, and make intermediate concentration
Solution become weak solution, the weak solution in absorber again Jing circulation be pumped in solution heat exchanger, with solution heat exchange
Enter after concentrated solution switching part heat in device in solution generator, after heat is absorbed in solution generator, evaporation and concentration becomes
Enter in the first condenser into concentrated solution, form closed circuit.The air-conditioning heat-exchange working medium cycle subsystem includes the second condensation
Device, the first check valve, second throttle, the second vaporizer, the second check valve and the 3rd choke valve, and it is the compressor, described
Cross valve, second condenser, first check valve, the subcooler, the second throttle and second evaporation
Device is sequentially connected and is formed first circulation loop, and the cold-producing medium Jing cross valves of the High Temperature High Pressure that compressor is discharged are into the second condensation
Condense in device, this process is radiation processes, and condensed the second check valves of cold-producing medium Jing enter subcooler, with suction in subcooler
Receipts formula cycle subsystem carries out heat exchange, and liquid refrigerant absorbs cold in the second vaporizer again Jing after second throttle reducing pressure by regulating flow
The heat of vaporization of matchmaker's water, plays the effect of refrigeration, and the refrigerant vapour after evaporation is passed through in compressor again, is followed into the next one
Ring.First check valve is connected in parallel with the 3rd choke valve, and second check valve is in parallel with the second throttle
Connection, make the compressor, the cross valve, second vaporizer, second check valve, the subcooler, described the
Three choke valves and second condenser are sequentially connected and are formed second circulation loop, and cross valve can change compressor discharge
The flow direction of cold-producing medium so as to flow direction during refrigeration just conversely, so as to play the effect for heating.The heat pump is also wrapped
Wind energy conversion system and motor are included, the wind energy conversion system and the motor are connected with compressor respectively, can be respectively as the drive of compressor
Dynamic source, efficiently utilizes wind energy resources, enables whole device normal under the complementary control of solar energy, wind energy and electric energy
Work, it is ensured that the quality of work, flexibly with various energy resources, alleviates the electrical network pressure of peak times of power consumption.
Description of the drawings
Fig. 1 is the structural representation of the heat pump described in the present embodiment;
Fig. 2 is the structural representation of the solar heat water subsystem described in the present embodiment;
Fig. 3 is the structural representation of the Absorption heat-transformer subsystem described in the present embodiment;
Fig. 4 is the structural representation of the air-conditioning heat-exchange working medium cycle subsystem described in the present embodiment.
Description of reference numerals:
1st, solar heat water subsystem, 11, heat collector, 12, storage tank, 13, water pump, 2, wind energy conversion system, 3, motor, 4, absorb
Formula cycle subsystem, 41, solution generator, the 42, first vaporizer, the 43, first condenser, 44, first throttle valve, 45, absorb
Device, 46, solution heat exchanger, 47, circulating pump, 5, compression cycle subsystem, 51, compressor, 52, subcooler, 53, four-way
Valve, the 531, first valve port, the 532, second valve port, the 533, the 3rd valve port, the 534, the 4th valve port, the 54, second condenser, 55, first
Check valve, 56, second throttle, the 57, second vaporizer, the 58, second check valve, 59, second throttle, the 6, first driver
Structure, the 7, second drive mechanism, 8, transducer.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than the embodiment of whole.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Referring to Fig. 1 to Fig. 4, the heat pump described in this preferred embodiment includes that solar heat water subsystem 1, air-conditioning exchanges heat
Working medium circulation subsystem 5 and Absorption heat-transformer subsystem 4, Absorption heat-transformer subsystem 4 include that solution generator 41, first is condensed
Device 43, first throttle valve 44, the first vaporizer 42 and absorber 45, are managed by two between solution generator 41 and absorber 45
Road is connected and forms refrigeration working medium closed circuit, and solution generator 41, the first condenser 43, first throttle valve 44, first
Vaporizer 42 and absorber 45 are sequentially connected, and the pipeline of solar heat water subsystem 1 passes through solution generator 41, air-conditioning heat exchange work
Matter cycle subsystem 5 includes cross valve 53, compressor 51 and subcooler 52, and the export pipeline cross valve 53 of compressor 51 is connected
Connect, and export pipeline passes through solution generator 41, subcooler 52 to intercouple with the first vaporizer 42.
Based on above structure, it is connected by two pipelines between solution generator 41 and absorber 45 and forms refrigeration work
Matter closed circuit, solution generator 41, the first condenser 43, first throttle valve 44, the first vaporizer 42, absorber 45 phase successively
Connection, the refrigeration working medium in solution generator 41 are heated to boiling by thermal source, produce refrigerant vapor through the first condenser 43,
It is condensed in the first condenser 43 as refrigerant liquid, liquid coolant is Jing after 44 blood pressure lowering of first throttle valve into the first evaporation
In device 42, absorb in the first vaporizer 42 and steam after the heat of the refrigerant liquid of air-conditioning heat-exchange working medium cycle subsystem 5
Send out and form vapor, produce the effect of refrigeration, evaporate the vapor for being formed and enter absorber 45, by the refrigeration work in absorber 45
Matter is absorbed, and reaches the effect of refrigeration;The vapor absorbed by absorber 45 is transmitted on refrigeration working medium closed circuit, under entering
One cycle period.The compressor 51 of solar heat water subsystem 1 and air-conditioning heat-exchange working medium cycle subsystem 5 is and solution generator
41 are connected, and solar energy source can provide heat for solution generator 41, so that the cold-producing medium evaporation in solution generator 41
Concentration, compressor 51 can exclude the refrigerant vapour of High Temperature High Pressure, flow through after solution generator 41 by weak solution pre-cooling, and press
The heat of the refrigerant vapour that contracting machine 51 is discharged also can be absorbed by solution generator 41, for the solution evaporation for making which internal
Concentration, is that Absorption heat-transformer subsystem 4 provides reliable working foundation.The export pipeline of compressor 51 and the first of cross valve 53
Valve port is connected, and the cross valve 53 can control the flow direction of the cold-producing medium in compressor 51, so as to realize air-conditioning heat-exchange working medium
5 refrigeration work of cycle subsystem and the switching for heating work.Subcooler 52 is intercoupled with the first vaporizer 42, i.e., after the coupling
Device can either can work for compression cycle subsystem again, be further ensured that suction for Absorption heat-transformer subsystem work
Back work of the receipts formula cycle subsystem to compression cycle subsystem, it is ensured that heat pump can be efficiently completed refrigeration or
The work for heating, and the operational mode can make hot water temperature lower than the temperature under simple subprogram mode, so as to reduce to collection
The requirement of hot device, increases substantially the COP of total system.
Referring to Fig. 1 and Fig. 3, Absorption heat-transformer subsystem 4 includes solution heat exchanger 46, and two pipelines are through solution warm
Circulating pump 47 is additionally provided with exchanger 46, and refrigeration working medium closed circuit, the weak solution Jing circulating pump 47 in absorber 45 is carried
Rise in solution heat exchanger 46, with solution generator 41 in concentrated solution switching part heat after enter solution generator 41
In, after absorbing heat in solution generator 41, evaporation and concentration becomes concentrated solution in the first condenser 43, forms cyclic system
System, provides condition for Part I work;In addition, the concentrated solution in solution generator 41, it is also possible to through solution heat exchanger
Flow automatically in absorber 45 after 46 coolings, blood pressure lowering, concentrated solution enters absorber after the cooling effect of solution heat exchanger 46
In 45, the temperature of the solution in absorber 45 can be cooled down, and this is conducive to from the first vaporizer 42 steam for coming to incorporate centre
The solution of intermediate concentration is made to become weak solution into circulation next time in the solution of concentration.Whole Absorption heat-transformer subsystem
Self-loopa is carried out inside 4, and reliably working condition is provided for air-conditioning heat-exchange working medium cycle subsystem 5, and exchange heat with air-conditioning
Working medium circulation subsystem 5 complements each other, and improves the work quality of integral heat pump device.Referring to Fig. 2, the solar water subsystem
System 1 includes heat collector 11, storage tank 12 and water pump 13, and heat collector 11, storage tank 12 and water pump 13 are sequentially connected to connect and formed and follow
Loop back path, water of the connecting line between water pump 13 and storage tank 12 in the solution generator, storage tank 12 is by collection
Hot device 11 is entered in solution generator 41 through water pump 13 after being heated, and realizes the solution Jing solar energys in solution generator 41
The process of heating, directly drives heat pump by solar energy, needs not move through light, the process of electricity conversion, and simple structure, improves energy
The utilization rate in source, and it is cost-effective.It should be noted that in the present embodiment, the refrigeration adopted in Absorption heat-transformer subsystem 4
Working medium is lithium-bromide solution, but in other embodiments, the selection of refrigeration working medium is not limited thereto, when can select as required
Select suitable refrigeration working medium.
Referring to Fig. 1 and Fig. 4, air-conditioning heat-exchange working medium cycle subsystem 5 include the second condenser 54, the first check valve 55,
Two choke valves 56 and the second vaporizer 57, and compressor 51, cross valve 53, the second condenser 54, the first check valve 55, subcooler
52nd, second throttle 56 and the second vaporizer 57 are sequentially connected and are formed first circulation loop, and compressor 51 discharges High Temperature High Pressure
Gaseous refrigerant, first pass through solution generator 41 before the first valve port that the gaseous refrigerant connects the cross valve 53,
Gaseous refrigerant in solution generator 41 by pre-cooling after, the second valve port of Jing cross valves 53 is dissipated in being admitted to the second condenser 54
Heat condensation, the liquid refrigerant that cryogenic high pressure is formed after condensation are entered in subcooler 52, because supercool by the first check valve 55
Device 52 is intercoupled with the first vaporizer 42, the liquid refrigerant of cryogenic high pressure in subcooler 52 with Absorption heat-transformer subsystem
4 carry out heat exchange, obtain supercool liquid refrigerant, and the liquid refrigerant enters the after 56 reducing pressure by regulating flow of second throttle
In two vaporizers 57, space increases suddenly, and pressure reduces, and the cold-producing medium of liquid is absorbed by the heat of vaporization vaporization of chilled water,
It is heat absorption from liquid to gaseous process, absorbs substantial amounts of heat in environment, the second vaporizer 57 will turns cold, and make coolant
Water becomes the purpose that low temperature refrigerant water reaches refrigeration, and the second vaporizer 57 connects the 4th valve port of cross valve 53, steams cold-producing medium
Vapour is passed through cross valve 53, and is sucked from the 3rd valve port of cross valve 53 by compressor 51 again, into the circulation in next cycle.Separately
Outward, the low temperature refrigerant water for being formed in process of refrigerastion can be used for air conditioning terminal.
Wherein, air-conditioning heat-exchange working medium cycle subsystem 5 includes the second check valve 58 and the 3rd choke valve 59, the first check valve
55 are connected in parallel with the 3rd choke valve 59, and the second check valve 58 is connected in parallel with second throttle 56, makes compressor 51, cross valve
53rd, the second vaporizer 57, the second check valve 58, subcooler 52, the 3rd choke valve 59 and the second condenser 54 are sequentially connected and shape
Into second circulation loop, compressor 51 discharges the gaseous refrigerant of High Temperature High Pressure, and the of gaseous refrigerant connection cross valve 53
Before one valve port pass through the solution generator 41, by the weak solution pre-cooling in solution generator 41 after, through cross valve 53
4th valve port is entered in the second vaporizer 57, in the second vaporizer 57 is cooled into liquid refrigerant, cold-producing medium by chilled water
It is exothermic process from gaseous state to liquid, sends substantial amounts of heat, makes 57 heating of the second vaporizer, and make chilled water become high temperature refrigerant
Water, indoor air are blown over from the second vaporizer 57, and make indoor fan blowout is steam, so as to realize the process for heating,
Liquid refrigerant in second vaporizer 57 enters subcooler 52 through the second check valve 58, due to subcooler 52 and the first evaporation
Device 42 intercouples, and makes liquid refrigerant carry out heat exchange, supercool liquid with Absorption heat-transformer subsystem 4 in subcooler 52
Cold-producing medium from subcooler 52 Jing after 59 reducing pressure by regulating flow of the 3rd choke valve in the second condenser 54 absorption air heat of vaporization, shape
Into gaseous refrigerant, the second condenser 54 is connected with the second valve port of cross valve 53, and the gaseous refrigerant enters cross valve 53
And reuptaked from the 3rd valve port by compressor 51, into the circulation in next cycle.In addition, above-mentioned high temperature refrigerant water can be for sky
End is adjusted to use.It should be noted that in the present embodiment, the cold-producing medium used in air-conditioning heat-exchange working medium cycle subsystem 5 is
R22 or R410A, but in other embodiments, the species of cold-producing medium is not limited by this embodiment, when can be according to actual need
Will, select suitable refrigerant type.
In addition, the heat pump also includes motor 3, motor 3 is connected with compressor 51 by the first drive mechanism 6,
The purpose that air-conditioning heat-exchange working medium cycle subsystem 5 is driven with electric energy can be reached;The heat pump also include wind energy conversion system 2, the
Two drive mechanisms 7 and transducer 8, wind energy conversion system 2, the second drive mechanism 7, transducer 8 and compressor 51 are sequentially connected and connect, Neng Goushi
Now drive the purpose of air-conditioning heat-exchange working medium cycle subsystem 5, and wind energy be used directly to drive air-conditioning heat exchange with wind energy
Working medium circulation subsystem 5, needs not move through wind-powered electricity generation conversion process, and apparatus structure is simple, can either improve the utilization rate of the energy, and
Production cost can be reduced.
The present invention can automatically select different mode of operations according to the situation of change of outdoor solar energy and wind energy:
(1) when solar energy, wind energy are sufficient, motor 3 can not start, it is also possible to realize Absorption heat-transformer subsystem and
Work while air-conditioning heat-exchange working medium cycle subsystem, saves energy source;
(2) when solar energy is sufficient, wind energy is not enough, wind energy conversion system 2 quits work, and motor 3 starts, and can realize absorption following
Work while loop subsystems and air-conditioning heat-exchange working medium cycle subsystem;
(3) when solar energy is not enough, wind energy is sufficient, wind energy conversion system 2 is started working, in motor 3 and solar heat water subsystem 1
Water pump 13 quit work, while driving Absorption heat-transformer subsystem and air-conditioning heat-exchange working medium cycle subsystem by wind energy conversion system 2
Work;
(4), when solar energy, wind energy are not enough, the water pump 13 in wind energy conversion system 2 and solar heat water subsystem 1 quits work,
Motor 3 is started working, and works while driving Absorption heat-transformer subsystem and air-conditioning heat-exchange working medium cycle subsystem by motor 3.
The heat pump of the present invention includes solar heat water subsystem, air-conditioning heat-exchange working medium cycle subsystem and absorption follows
Loop subsystems, the Absorption heat-transformer subsystem include solution generator, the first condenser, first throttle valve, the first vaporizer,
Absorber and circulating pump, are connected and form refrigeration working medium by two pipelines between the solution generator and the absorber
Closed circuit, and the solution generator, first condenser, the first throttle valve, first vaporizer, the suction
Receive device to be sequentially connected, wherein, the cooled water-cooled of the first condensers of vapor Jing in solution generator is congealed into water, through first segment
Enter in the first vaporizer, as the first vaporizer and subcooler intercouple after stream valve blood pressure lowering, inhale can low pressure condensed water
Evaporate after the heat for receiving the refrigerant liquid in air-conditioning heat-exchange working medium cycle subsystem, produce the effect of refrigeration;In addition, first steams
The vapor evaporated in sending out device is entered in absorber, is absorbed by refrigeration working medium, and the solution in absorber is absorbed from the first evaporation
Steam in device out becomes weak solution, and weak solution enters solution generator, is produced steam by thermal source heating again and is formed again
Concentrated solution, starts the circulation of next round;Due to being connected by two pipelines between solution generator and absorber and forming system
Cold working medium circulation loop, the concentrated solution in instant liquid generator also can be entered in absorber, are absorbed first by absorber and are evaporated
Steam in device is become weak solution, continues supply work.The pipeline of the solar heat water subsystem passes through the solution
Generator, can provide heat for the solution in solution generator, promote the solution in solution generator to be heated and produce steam shape
Into concentrated solution, the further work for system provides condition;And solar heat water subsystem effectively make use of solar energy source, with
Air-conditioning heat-exchange working medium cycle subsystem cooperating, can form the utilization form of various energy resources, very flexibly.The air-conditioning is changed
Hot working fluid cycle subsystem includes cross valve, compressor and subcooler, the export pipeline of the compressor and the cross valve
It is connected, and the export pipeline of the compressor, through the solution generator, solution generator can be to discharges in compressor
High-temperature high-pressure refrigerant carry out pre-cooling, facilitate the work of next step, and the solution generator to be respectively cooperating with the air-conditioning and change
Hot working fluid cycle subsystem and Absorption heat-transformer subsystem cooperation, when ensure that heat pump refrigeration or heating work
Quality, makes the functional reliability of whole system higher.The subcooler is intercoupled with first vaporizer, and states first
Vaporizer be coupled with the subcooler after device, also can either exchange heat for air-conditioning for Absorption heat-transformer subsystem work
Working medium circulation subsystem work, it is ensured that in the case of solar energy or other driving sources deficiency, Absorption heat-transformer subsystem and
Air-conditioning heat-exchange working medium cycle subsystem also can be worked simultaneously, reliably be efficiently completed refrigeration or the work for heating, and two kinds are followed
The mode that ring is coupled can make hot water temperature lower than the temperature under simple subprogram mode, so as to reduce the requirement to heat collector,
Increase substantially the COP of total system.
It should be appreciated that adopting term " first ", " second " etc. to describe various information, but these information in the present invention
These terms are should not necessarily be limited by, these terms are only for same type of information is distinguished from each other out.For example, without departing from the present invention
In the case of scope, " first " information can also be referred to as " second " information, similar, and " second " information can also be referred to as
" first " information.
The above is the preferred embodiment of the present invention, it is noted that for those skilled in the art
For, under the premise without departing from the principles of the invention, some improvement and deformation can also be made, these improve and deformation is also considered as
Protection scope of the present invention.
Claims (10)
1. a kind of heat pump, it is characterised in that including solar heat water subsystem, air-conditioning heat-exchange working medium cycle subsystem and suction
Receipts formula cycle subsystem, the Absorption heat-transformer subsystem include solution generator, the first condenser, first throttle valve, first
Vaporizer and absorber, are connected and form refrigeration working medium by two pipelines between the solution generator and the absorber
Closed circuit, and the solution generator, first condenser, the first throttle valve, first vaporizer and described
Absorber is sequentially connected, and the pipeline of the solar heat water subsystem passes through the solution generator, the air-conditioning heat-exchange working medium
Cycle subsystem includes cross valve, compressor and subcooler, and the export pipeline of the compressor is connected with the cross valve,
And the export pipeline passes through the solution generator, the subcooler to intercouple with first vaporizer.
2. heat pump according to claim 1, it is characterised in that the Absorption heat-transformer subsystem includes that solution heat is handed over
Parallel operation, described two pipelines are through the solution heat exchanger.
3. heat pump according to claim 1, it is characterised in that be additionally provided with the refrigeration working medium closed circuit and follow
Ring pump.
4. heat pump according to claim 1, it is characterised in that the air-conditioning heat-exchange working medium cycle subsystem includes
Two condensers, the first check valve, second throttle and the second vaporizer, and it is the compressor, the cross valve, described second cold
Condenser, first check valve, the subcooler, the second throttle and second vaporizer are sequentially connected and form
One closed circuit.
5. heat pump according to claim 3, it is characterised in that the air-conditioning heat-exchange working medium cycle subsystem includes
Two check valves and the 3rd choke valve, first check valve are connected in parallel with the 3rd choke valve, second check valve with
The second throttle is connected in parallel, make the compressor, the cross valve, second vaporizer, second check valve,
The subcooler, the 3rd choke valve and second condenser are sequentially connected and form second circulation loop.
6. the heat pump according to any one of claim 1 to 5, it is characterised in that also including motor, the motor passes through
First drive mechanism is connected with the compressor.
7. the heat pump according to any one of claim 1 to 5, it is characterised in that also including wind energy conversion system, the wind energy conversion system
It is connected with the compressor.
8. heat pump according to claim 5, its feature is being, also including the second drive mechanism and transducer, institute
State wind energy conversion system, second drive mechanism, the transducer and the compressor to be sequentially connected and connect.
9. the heat pump according to any one of claim 1 to 5, it is characterised in that the solar heat water subsystem bag
Heat collector, water pump and storage tank are included, the heat collector, the water pump and the storage tank are sequentially connected and form closed circuit.
10. heat pump according to claim 8, it is characterised in that the connection between the water pump and the storage tank
Pipeline passes through the solution generator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611223694.0A CN106595117A (en) | 2016-12-27 | 2016-12-27 | Heat pump system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611223694.0A CN106595117A (en) | 2016-12-27 | 2016-12-27 | Heat pump system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106595117A true CN106595117A (en) | 2017-04-26 |
Family
ID=58603895
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611223694.0A Pending CN106595117A (en) | 2016-12-27 | 2016-12-27 | Heat pump system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106595117A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107702374A (en) * | 2017-09-11 | 2018-02-16 | 新奥泛能网络科技股份有限公司 | Solar energy accumulated heat system and solar refrigeration system |
CN108159837A (en) * | 2017-12-19 | 2018-06-15 | 内蒙古科技大学 | Cold and hot type solid dehumidifying regenerative system in a kind of solar heat pump |
CN108895718A (en) * | 2018-07-18 | 2018-11-27 | 珠海格力电器股份有限公司 | Heat pump system |
WO2019056604A1 (en) * | 2017-09-20 | 2019-03-28 | 河海大学常州校区 | Combined energy-based solar lithium bromide absorption trigeneration system |
CN110057129A (en) * | 2019-05-29 | 2019-07-26 | 华北电力大学 | A kind of coupling heat pump heat exchanger |
CN112815576A (en) * | 2019-11-18 | 2021-05-18 | 海南光谱太阳能技术工程有限公司 | Comprehensive energy-saving system for solar energy utilization |
CN113108503A (en) * | 2021-03-24 | 2021-07-13 | 中国科学院工程热物理研究所 | Heat pump set based on self-cascade circulation |
WO2024060634A1 (en) * | 2022-09-21 | 2024-03-28 | 青岛海尔空调器有限总公司 | Solar absorption refrigeration system, control method, and electronic device |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101055136A (en) * | 2007-06-01 | 2007-10-17 | 浙江大学 | Low grade energy driven and mechanical power driven composite heat pump, refrigeration system |
CN200979313Y (en) * | 2006-11-30 | 2007-11-21 | 华南理工大学 | Wind power drive refrigeration and heat pump installation |
CN101290176A (en) * | 2008-05-07 | 2008-10-22 | 中原工学院 | Heat reclamation -type solar energy jetting electric compression heat pump air-conditioning unit |
KR20160034129A (en) * | 2014-09-19 | 2016-03-29 | (주)대성마리프 | Union system for fusing new-renewable electric energy and gas engine heat pump |
CN105627473A (en) * | 2016-02-23 | 2016-06-01 | 上海交通大学 | Solar thermally-driven independent temperature and humidity control air conditioning system |
CN206488503U (en) * | 2016-12-27 | 2017-09-12 | 广东技术师范学院 | A kind of heat pump |
-
2016
- 2016-12-27 CN CN201611223694.0A patent/CN106595117A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN200979313Y (en) * | 2006-11-30 | 2007-11-21 | 华南理工大学 | Wind power drive refrigeration and heat pump installation |
CN101055136A (en) * | 2007-06-01 | 2007-10-17 | 浙江大学 | Low grade energy driven and mechanical power driven composite heat pump, refrigeration system |
CN101290176A (en) * | 2008-05-07 | 2008-10-22 | 中原工学院 | Heat reclamation -type solar energy jetting electric compression heat pump air-conditioning unit |
KR20160034129A (en) * | 2014-09-19 | 2016-03-29 | (주)대성마리프 | Union system for fusing new-renewable electric energy and gas engine heat pump |
CN105627473A (en) * | 2016-02-23 | 2016-06-01 | 上海交通大学 | Solar thermally-driven independent temperature and humidity control air conditioning system |
CN206488503U (en) * | 2016-12-27 | 2017-09-12 | 广东技术师范学院 | A kind of heat pump |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107702374A (en) * | 2017-09-11 | 2018-02-16 | 新奥泛能网络科技股份有限公司 | Solar energy accumulated heat system and solar refrigeration system |
WO2019056604A1 (en) * | 2017-09-20 | 2019-03-28 | 河海大学常州校区 | Combined energy-based solar lithium bromide absorption trigeneration system |
CN108159837A (en) * | 2017-12-19 | 2018-06-15 | 内蒙古科技大学 | Cold and hot type solid dehumidifying regenerative system in a kind of solar heat pump |
CN108895718A (en) * | 2018-07-18 | 2018-11-27 | 珠海格力电器股份有限公司 | Heat pump system |
CN110057129A (en) * | 2019-05-29 | 2019-07-26 | 华北电力大学 | A kind of coupling heat pump heat exchanger |
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 |
CN112815576A (en) * | 2019-11-18 | 2021-05-18 | 海南光谱太阳能技术工程有限公司 | Comprehensive energy-saving system for solar energy utilization |
CN113108503A (en) * | 2021-03-24 | 2021-07-13 | 中国科学院工程热物理研究所 | Heat pump set based on self-cascade circulation |
WO2024060634A1 (en) * | 2022-09-21 | 2024-03-28 | 青岛海尔空调器有限总公司 | Solar absorption refrigeration system, control method, and electronic device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106595117A (en) | Heat pump system | |
CN206488503U (en) | A kind of heat pump | |
CN101571330B (en) | Multifunctional frost-free solar-assisted heat pump system | |
CN105042931A (en) | Combined heat pump system adopting trans-critical circulation and absorption heat pump co-production | |
CN103983042A (en) | Solar indoor cold and hot integrated system | |
CN101556095A (en) | Low-grade energy driving and mechanical work driving combined heat pump or refrigerating system | |
CN201844606U (en) | Novel high-efficiency and direct-fired lithium bromide absorption-type water heater/chiller | |
CN105004095B (en) | A kind of trans critical cycle and the combined heat-pump system of two-stage absorption heat pump coproduction | |
CN102759159B (en) | A kind of heat pipe hot pump composite system | |
CN203687251U (en) | Dry air energy and solar energy compounded air conditioning system | |
CN109269143B (en) | Novel absorption heat pump and application method thereof | |
CN201203297Y (en) | Solar auxiliary direct combustion type cold and hot water machine unit | |
CN106440475A (en) | Two-section cascade-type single-effect lithium bromide absorption refrigeration heat pump unit | |
CN105716324A (en) | Double-heat-source efficient air conditioner system based on compression-injection combination and application | |
CN107843026A (en) | A kind of refrigeration system using solar energy | |
CN205783497U (en) | A kind of water energy storage system | |
CN201218627Y (en) | Dual-effect absorption type ground source heat pump and floor air conditioner integration system | |
CN106839217A (en) | De- electrically independent operation combined type heat pump air conditioner system and its control method | |
CN202254468U (en) | Hot-start electric drive effective environment friendly water chiller unit | |
CN111609578B (en) | Small-sized multi-mode solar-assisted household air conditioning system | |
CN201497255U (en) | Solar backheating type sodium thiocyanate-ammonia absorption refrigerator air conditioner and heat pump device | |
CN201218628Y (en) | Cold-hot bidirectional and simultaneous utilizing dual- effect type third-kind absorption heat pump | |
CN102297542B (en) | Water chilling unit capable of first being thermally started and then electrically driven | |
CN209341622U (en) | Multi-energy source dual-efficiency type lithium bromide absorption type refrigerator | |
CN202008255U (en) | Total cold recovery water source screw high temperature heat pump hot water unit |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170426 |
|
RJ01 | Rejection of invention patent application after publication |