CN106766316A - A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump - Google Patents

A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump Download PDF

Info

Publication number
CN106766316A
CN106766316A CN201611202686.8A CN201611202686A CN106766316A CN 106766316 A CN106766316 A CN 106766316A CN 201611202686 A CN201611202686 A CN 201611202686A CN 106766316 A CN106766316 A CN 106766316A
Authority
CN
China
Prior art keywords
heat pump
gas
increasing
compressor
heat
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
Application number
CN201611202686.8A
Other languages
Chinese (zh)
Inventor
田幼华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yanyuan Technology (beijing) Co Ltd Depp
Original Assignee
Yanyuan Technology (beijing) Co Ltd Depp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Yanyuan Technology (beijing) Co Ltd Depp filed Critical Yanyuan Technology (beijing) Co Ltd Depp
Priority to CN201611202686.8A priority Critical patent/CN106766316A/en
Publication of CN106766316A publication Critical patent/CN106766316A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/008Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B30/00Heat pumps
    • F25B30/02Heat pumps of the compression type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/40Fluid line arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/02Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for separating lubricants from the refrigerant

Abstract

The present invention provides a kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump, it includes CO2Heat pump and the second heat pump, wherein, CO2Heat pump is low-temperature level, and it includes the CO being sequentially connected2Compressor, gas cooler, evaporative condenser, first throttle device, flash vessel, second throttling device, evaporator and fluid gas separating device;Second heat pump is high-temperature level, and it includes the second compressor, the second condenser, the 3rd throttling arrangement and the evaporative condenser that are sequentially connected;CO2Heat pump is combined with the second heat pump by devaporizer overlapping, CO2Heat pump is absorbed heat by evaporative condenser heat release, the second heat pump by the evaporative condenser;Flash vessel also with CO2Compressor is connected carries out CO with to it2The supplement of gas.Heat pump of the invention can be realized heating and providing hot water in 35 DEG C of cold district, maintain COP and relatively low manufacturing cost higher.

Description

A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump
Technical field
Technical field is changed and utilized the invention belongs to heat energy, and in particular to a kind of Gas-supplying enthalpy-increasing suitable for cold district CO2Part overlapping heat pump.
Background technology
In recent years, with the implementation of " coal changes electricity ", air source heat pump progresses into the life of people, but current air-source Heat pump is difficult to meet the ultra-low temperature surroundings operation below -25 DEG C.Air source heat pump of the prior art in use when (such as in the northeast of cold district, the Inner Mongol, Xinjiang etc.) when environment temperature is relatively low, it is impossible to fully draw the heat in environment For heating or hot water preparing, so as to cause the Energy Efficiency Ratio of whole heat pump relatively low, energy consumption is larger, and frosting also easily occurs Etc. unfavorable phenomenon, the service behaviour of whole system is caused to be deteriorated, it is impossible to meet user's heating, the demand of hot water preparing.Existing skill Trans-critical cycle CO in art2Technology in heating field, because return water temperature is generally greater than 31 DEG C, it is impossible to utilize CO2It is higher in critical point The heat that specific heat capacity is produced, therefore Energy Efficiency Ratio is not high;Freon system heating capacity sharp-decay at low ambient temperatures, and singly The working range of one freon refrigerant is smaller, and freon cascade system needs multistage overlapping to meet cold district heating will Ask, relatively costly, COP values are relatively low, therefore urgent need will develop a kind of new heat pump, to improve above-mentioned unfavorable feelings Condition.
Performance degradation is serious at a temperature of there is low temperature environment due to heat pump heating/water system of the prior art, system The hot water temperature of taking-up is not high, the technical problem such as the COP of cold district routine overlapping heat pump is relatively low or relatively costly, therefore this hair Bright research and design goes out a kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump.
The content of the invention
Therefore, the technical problem to be solved in the present invention is to overcome heat pump heating system of the prior art to exist in low temperature Performance degradation is seriously under environment temperature, hot water preparing temperature is not high, conventional overlapping heat pump COP is relatively low and relatively costly lacks Fall into, so as to provide a kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump.
The present invention provides a kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump, it includes CO2Heat pump system System and the second heat pump, wherein,
The CO2Heat pump is low-temperature level, and it includes the CO being sequentially connected2Compressor, gas cooler, evaporative condenser Device, first throttle device, flash vessel, second throttling device, evaporator and fluid gas separating device;
Second heat pump is high-temperature level, the second compressor that it includes being sequentially connected, the second condenser, Section three Stream device and evaporative condenser;
The CO2Heat pump is combined with second heat pump by devaporizer overlapping, the CO2 Heat pump is absorbed heat by the evaporative condenser heat release, second heat pump by the evaporative condenser;And
The flash vessel also with the CO2Compressor is connected to it supplement the CO of medium temperature and medium pressure2。Preferably, it is described Flash vessel is the CO2The CO of compressor supplement2The temperature of gas is 35-50 DEG C, and pressure is 4-6MPa.
Preferably, the CO2Heat pump also include regenerator, its respectively with the CO2Compressor, evaporative condenser, One throttling arrangement and fluid gas separating device are connected.
Preferably, the gas cooler is arranged on the upward refrigerant end of the evaporative condenser.
Preferably, R245fa, R134a are used in second heat pump as refrigerant.
Preferably, first throttle device, second throttling device and the 3rd throttling arrangement are choke valve or injector.
A kind of Gas-supplying enthalpy-increasing CO suitable for cold district that the present invention is provided2Part overlapping heat pump has following beneficial effect Really:
1. CO described in patent of the present invention2System circulation is defined dual-stage servo system, first applies in CO Gas-supplying enthalpy-increasing technology2Across Critical heat pump, under ultralow-temperature operation conditions, increased the mass flow in gas cooler, break through tradition CO2Trans-critical cycle heat The drawback such as pumping system cold operation Energy Efficiency Ratio is low, pressure at expulsion is high, can heat and carry at a temperature of -35 DEG C of ultra-low temperature surroundings Domestic hot-water supply, keeps COP higher, further, since system employs Gas-supplying enthalpy-increasing technology, reduces making for a compressor With, therefore its more conventional CO2Dual-stage servo system greatly reduces cost.
2. the Gas-supplying enthalpy-increasing CO suitable for cold district that the present invention is provided2Part overlapping heat pump is cold using two-part gas But device, the refrigerant circulation of the second heat pump make use of CO2The low-grade energy of critical end, both improves CO2Trans-critical cycle heat pump System (CO2Air cooler outlet temperature is dropped to below critical point) COP again from suitable refrigerant (according to physical properties) Low-grade energy is converted into high-grade energy, high-temperature water outlet, high-temperature tempering under ultralow-temperature operation conditions is realized;
3. the Gas-supplying enthalpy-increasing CO suitable for cold district that the present invention is provided2Part overlapping heat pump is entered using flash vessel pattern Row Gas-supplying enthalpy-increasing so that the amount of parts in high pressure falls below minimum, reduces cost;
4. the Gas-supplying enthalpy-increasing CO suitable for cold district that the present invention is provided2Part overlapping heat pump, can be in -35 DEG C cold Under the conditions of run, realize heating while thermobiosis hot water can also be provided;
5. the Gas-supplying enthalpy-increasing CO suitable for cold district that the present invention is provided2Part overlapping heat pump, by condenser and gas Cooler progressively heat hot water, the cascade utilization energy successively, remain that refrigerant has the less temperature difference with water, reduce (fire is used) Loss.
Brief description of the drawings
Fig. 1 is a kind of Gas-supplying enthalpy-increasing CO suitable for cold district of the invention2The structural representation of part overlapping heat pump.
Reference is expressed as in figure:
1—CO2Compressor, 2- gas coolers, 3- devaporizers, 4- regenerators, 5-first throttle device, 6-dodge Steaming device, 7-second throttling device, 8-evaporator, 9-fluid gas separating device, the compressors of 10- second, the condensers of 11- second, The throttling arrangements of 12- the 3rd, 13- shell-and-tube heat exchangers.
Specific embodiment
The invention provides a kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump, it can be in cold Area operation, realizes heating demands and provides domestic hot-water.
Fig. 1 shows the Gas-supplying enthalpy-increasing CO suitable for cold district of the present invention2The structural representation of part overlapping heat pump Figure.As shown in figure 1, it includes CO2Heat pump and the second heat pump, wherein, the CO2Heat pump is low-temperature level, its bag Include the CO being sequentially connected2Compressor 1, gas cooler 2, evaporative condenser 3, first throttle device 5, flash vessel 6, second throttle Device 7, evaporator 8 and fluid gas separating device 9;Second heat pump is high-temperature level, and it includes the second pressure being sequentially connected Contracting machine 10, the second condenser 11, the 3rd throttling arrangement 12 and evaporative condenser 3;The CO2Heat pump and second heat pump System is combined by the overlapping of devaporizer 3;Wherein described second heat pump is evaporated by the evaporative condenser 3 Heat absorption, the CO2Heat pump cools down heat release (i.e. CO by the evaporative condenser 32Heat pump and the second heat pump cycle system Altogether with the evaporative condenser 3).The import connection heating system import of the second condenser 11, outlet connection CO2Air cooler 2, CO2The outlet connecting pipe shell heat exchanger 13 of air cooler 2, the outlet connection heating system of shell-and-tube heat exchanger 13, provides the user confession Warm demand.There is coil pipe import to connect running water inlet in shell-and-tube heat exchanger 13, outlet connection user provides the user life heat Water.
In the CO2In heat pump, the CO2Compressor 1 is specially with the connection of fluid gas separating device 9:CO2Compression The gas outlet of the import connection fluid gas separating device 9 of machine 1, the bottom oil separating opening of oil return opening connection fluid gas separating device 9.Additionally, The flash vessel 6 also with the CO2Compressor 1 is connected carries out CO with to it2The supplement of gas, realizes the function of Gas-supplying enthalpy-increasing.
Gas-supplying enthalpy-increasing CO suitable for cold district of the invention2Part overlapping heat pump uses the CO of superposition type2Heat pump With the second heat pump, and in CO2Using gas cooler and the connection side of evaporative condenser two-stage type heat release in heat pump Formula, realizes high-temperature water outlet, high-temperature tempering, overcomes existing CO2COP relatively low defect when heat pump return water temperature is high.System System low-temperature end uses CO2Refrigerant, can overcome heat pump of the prior art performance degradation at a temperature of low temperature environment serious Defect so that stable system performance and system energy efficiency maintains level higher, CO all the time2Have in worst cold case superior Thermophysical property:CO2Evaporation latent heat it is larger, refrigerating effect per unit swept volume is high, and (at -40 DEG C, refrigerating effect per unit swept volume is NH3 9.43 times);CO2Kinematic viscosity it is low (kinematic viscosity of saturated liquid only has the 67% of NH3 at -40 DEG C);CO2Thermal conductivity factor The ratio of height, fluid density and vapour density is small, and the distribution of refrigerant is more uniform between each loop after throttling, therefore system can be fitted Answer less than -30 DEG C of ultra-low temperature surroundings temperature.Most critical ground, creatively applies in CO Gas-supplying enthalpy-increasing technology2Trans-critical cycle heat Pumping system, under ultralow-temperature operation conditions, increased the mass flow in gas cooler, break through tradition CO2Trans-critical cycle heat pump Cold operation drawback, greatly improves COP, and the heat pump can solve the problem that the heating problem of extremely cold area and provide high temperature life Hot water living.
Additionally, it is CO that flash vessel is used in the present invention2Heat pump Gas-supplying enthalpy-increasing, only with a CO2Compression function meets system System operation demand so that the part in high pressure is dropped at least, reduces cost.Preferably, the flash vessel 6 is the CO2 The CO of the supplement of compressor 12The temperature of gas is 35-50 DEG C, and pressure is 4-6MPa.The CO2Heat pump is trans critical cycle, The intermediate fill gas mouth of the flash vessel 6 connects CO2The gas supplementing opening of compressor 1, is the CO of its above-mentioned intermediate pressure medium temperature of supplement2Gas Body.The gas enters CO2The gas supplementing opening recompression of compressor 1, so as to reduce CO2The power consumption of compressor 1, has reached tonifying Qi increasing The effect of enthalpy, improves system COP.The Gas-supplying enthalpy-increasing opens flash vessel below 0 DEG C and carries out Gas-supplying enthalpy-increasing.
Preferably, the CO2Heat pump also include regenerator 4, its respectively with the CO2Compressor 1, evaporative condenser 3rd, first throttle device 5 and fluid gas separating device 9 are connected.Specifically, as shown in figure 1, the side-entrance connection of the regenerator 4 Devaporizer 3, outlet connection first throttle device 5, another side-entrance connection fluid gas separating device 9, outlet connection CO2Compression The air entry of machine 1.By setting the regenerator, the power consumption of compressor can be reduced, further improve the COP of system.
Preferably, the gas cooler 2 is arranged on the upward refrigerant end of the evaporative condenser 3.So make to bring about the desired sensation Body cooler is configured to first order cooler, and evaporative condenser is configured to second-stage cooler, forms the cooling of two-stage tandem formula Exotherm, can effectively utilize CO2The high exhaust temperature of heat pump is so as to produce high-temperature-hot-water, while it is cold to reduce evaporation The energy consumption of the power of condenser and the second heat pump;Heat of high temperature pair can be discharged by first order cooler (gas cooler) Second condensator outlet hot water is reheated, and realizes progressively heat hot water, less (fire is used) loss, and can be by evaporation Condenser (second-stage cooler) is exchanged heat with the second heat pump circulating system, specifically, due to the evaporation of the second heat pump Temperature is sufficiently low, so as to effectively reduce CO2The temperature of heat pump refrigerant, and then by that can be reached more after throttling expansion Low temperature.
Preferably, R245fa, R134a are used in second heat pump as refrigerant.The CO of patent of the present invention2Heat Pumping system uses CO2As refrigerant, CO can be utilized2The excellent mobile performance under worst cold case of refrigerant and heat exchange property, system Take high-temperature-hot-water.And second heat pump has recycled CO2The low-grade energy of critical end, both improves CO2Trans-critical cycle heat Low-grade energy is converted into high-grade energy by the COP of pumping system from above-mentioned suitable refrigerant (according to physical properties) again (COP is higher for fluorine system circulation), improves heating water return temperature.For example, in -35 DEG C of environment temperature, the steaming of the evaporator 8 - 40 DEG C of temperature of hair;During using R245fa as refrigerant, 65 DEG C of water inlets of the second condenser of overlapping high-temperature level, 70 DEG C of water outlets are (cold Solidifying 75 DEG C of temperature), now, CO2Gas cooler 2 can reach 70 DEG C of water inlets, and 80 DEG C of water outlets can reach heating and require and can reach To domestic water requirement.Certainly, it will be apparent to a skilled person that except above-mentioned refrigerant, other existing middle height Warm refrigerant is also applied for the second heat pump of the invention.
Preferably, first throttle device (5), second throttling device (7) and the 3rd throttling arrangement (12) are choke valve or spray Emitter.Certainly, it will be apparent to a skilled person that other throttling arrangements are also applied for the present invention.
The CO that patent of the present invention is provided2Heat pump can run under the cold conditions of -35 DEG C of environment temperature, the evaporator CO in 82Reachable -40 DEG C of evaporating temperature;When realizing that heating is required, COP is more than 2.5.Patent utilization of the present invention CO2Heat pump across Critical technology, makes CO2The outlet temperature of thermo-compression evaporation cooler 3 is less than 29 DEG C, takes full advantage of CO2The energy of heat pump Trans-critical cycle, and And the middle and high temperature refrigerant of selection such as R245fa, R134a is used as the evaporation working medium of devaporizer 3 so that system COP is higher than general Logical overlapping unit, and the low-grade energy at carbon dioxide low temperature can be promoted to high-grade energy, so as to realize extremely trembling with fear The heating demands in area simultaneously provide domestic hot-water, meet the heating demands and demand of domestic water of cold district user, and will just Investment, operating cost fall below minimum, overcome the shortcomings of that existing heat pump is present.
Those skilled in the art is it is easily understood that on the premise of not conflicting, above-mentioned each advantageous manner can be free Ground combination, superposition.
Presently preferred embodiments of the present invention is the foregoing is only, is not intended to limit the invention, it is all in essence of the invention Any modification, equivalent and improvement made within god and principle etc., should be included within the scope of the present invention.With Only it is the preferred embodiment of the present invention described in upper, it is noted that for those skilled in the art, not On the premise of departing from the technology of the present invention principle, some improvement and modification can also be made, these are improved and modification also should be regarded as this The protection domain of invention.

Claims (6)

1. a kind of Gas-supplying enthalpy-increasing CO2 parts overlapping heat pump suitable for cold district, it is characterised in that:Including CO2Heat pump and Second heat pump, wherein,
The CO2Heat pump is low-temperature level, and it includes the CO being sequentially connected2Compressor (1), gas cooler (2), evaporation are cold Condenser (3), first throttle device (5), flash vessel (6), second throttling device (7), evaporator (8) and fluid gas separating device (9);
Second heat pump is high-temperature level, the second compressor (10) that it includes being sequentially connected, the second condenser (11), the Three throttling arrangements (12) and evaporative condenser (3);
The CO2Heat pump is combined with second heat pump by devaporizer (3) overlapping, the CO2Heat Pumping system is absorbed heat by the evaporative condenser (3) heat release, second heat pump by the evaporative condenser (3);And And
The flash vessel (6) also with the CO2Compressor (1) is connected carries out CO with to it2The supplement of gas.
2. the Gas-supplying enthalpy-increasing CO suitable for cold district according to claim 12Part overlapping heat pump, it is characterised in that:Institute It is the CO to state flash vessel (6)2The CO of compressor (1) supplement2The temperature of gas is 35-50 DEG C, and pressure is 4-6MPa.
3. the Gas-supplying enthalpy-increasing CO suitable for cold district according to claim 1 and 22Part overlapping heat pump, its feature exists In:The CO2Heat pump also include regenerator (4), its respectively with the CO2Compressor (1), evaporative condenser (3), first Throttling arrangement (5) and fluid gas separating device (9).
4. the Gas-supplying enthalpy-increasing CO suitable for cold district according to claim 1 and 22Part overlapping heat pump, its feature exists In:Gas cooler (2) is arranged on the upward refrigerant end of the evaporative condenser (3).
5. the Gas-supplying enthalpy-increasing CO suitable for cold district according to claim 1 and 22Part overlapping heat pump, its feature exists In:Using R245fa, R134a as refrigerant in second heat pump.
6. the Gas-supplying enthalpy-increasing CO suitable for cold district according to claim 1 and 22Part overlapping heat pump, its feature exists In:First throttle device (5), second throttling device (7) and the 3rd throttling arrangement (12) are choke valve or injector.
CN201611202686.8A 2016-12-23 2016-12-23 A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump Pending CN106766316A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611202686.8A CN106766316A (en) 2016-12-23 2016-12-23 A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611202686.8A CN106766316A (en) 2016-12-23 2016-12-23 A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump

Publications (1)

Publication Number Publication Date
CN106766316A true CN106766316A (en) 2017-05-31

Family

ID=58899869

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611202686.8A Pending CN106766316A (en) 2016-12-23 2016-12-23 A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump

Country Status (1)

Country Link
CN (1) CN106766316A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107990580A (en) * 2017-11-07 2018-05-04 西安交通大学 A kind of the self-cascade heat pump system and operational mode of separating for several times injection synergy
CN108007007A (en) * 2017-10-30 2018-05-08 新奥泛能网络科技股份有限公司 Heat pump system
CN108489144A (en) * 2018-01-29 2018-09-04 同济大学 A kind of drying system using overlapping multiple heat pump
CN110186221A (en) * 2019-06-27 2019-08-30 中国科学院理化技术研究所 CO 2 trans-critical heat pump system
CN111550944A (en) * 2020-04-26 2020-08-18 珠海格力电器股份有限公司 Triple throttling enthalpy-increasing double-condensation refrigerating system, air conditioner and control method
CN114507508A (en) * 2022-03-15 2022-05-17 浙江大学 Application of heat pump mixed working medium

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201488273U (en) * 2009-07-27 2010-05-26 广东长菱空调冷气机制造有限公司 Air source heat pump water heater
CN204063660U (en) * 2014-07-03 2014-12-31 珠海格力电器股份有限公司 Three stage compression autocascade cycle heat pump
CN105135738A (en) * 2015-09-13 2015-12-09 华南理工大学 Air-supplying enthalpy-adding heat pump air conditioning system capable of promoting heat exchange performance of heat exchangers
CN105241105A (en) * 2015-10-22 2016-01-13 湖南大学 Refrigerating system based on oil cooling compression circulation
CN205037565U (en) * 2015-10-21 2016-02-17 浙江佳力科技股份有限公司 Realize high return water temperature and different critical CO2 heat pump system that strides who heats operating mode requirement
CN206488501U (en) * 2016-12-23 2017-09-12 燕园德普科技(北京)有限公司 A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201488273U (en) * 2009-07-27 2010-05-26 广东长菱空调冷气机制造有限公司 Air source heat pump water heater
CN204063660U (en) * 2014-07-03 2014-12-31 珠海格力电器股份有限公司 Three stage compression autocascade cycle heat pump
CN105135738A (en) * 2015-09-13 2015-12-09 华南理工大学 Air-supplying enthalpy-adding heat pump air conditioning system capable of promoting heat exchange performance of heat exchangers
CN205037565U (en) * 2015-10-21 2016-02-17 浙江佳力科技股份有限公司 Realize high return water temperature and different critical CO2 heat pump system that strides who heats operating mode requirement
CN105241105A (en) * 2015-10-22 2016-01-13 湖南大学 Refrigerating system based on oil cooling compression circulation
CN206488501U (en) * 2016-12-23 2017-09-12 燕园德普科技(北京)有限公司 A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108007007A (en) * 2017-10-30 2018-05-08 新奥泛能网络科技股份有限公司 Heat pump system
CN108007007B (en) * 2017-10-30 2020-03-10 新奥泛能网络科技股份有限公司 Heat pump system
CN107990580A (en) * 2017-11-07 2018-05-04 西安交通大学 A kind of the self-cascade heat pump system and operational mode of separating for several times injection synergy
CN108489144A (en) * 2018-01-29 2018-09-04 同济大学 A kind of drying system using overlapping multiple heat pump
CN110186221A (en) * 2019-06-27 2019-08-30 中国科学院理化技术研究所 CO 2 trans-critical heat pump system
CN111550944A (en) * 2020-04-26 2020-08-18 珠海格力电器股份有限公司 Triple throttling enthalpy-increasing double-condensation refrigerating system, air conditioner and control method
CN111550944B (en) * 2020-04-26 2024-03-29 珠海格力电器股份有限公司 Triple throttling enthalpy-increasing double-condensation refrigerating system, air conditioner and control method
CN114507508A (en) * 2022-03-15 2022-05-17 浙江大学 Application of heat pump mixed working medium

Similar Documents

Publication Publication Date Title
CN106766316A (en) A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump
CN204373252U (en) Change type CO2 trans critical cycle refrigeration system
CN202254464U (en) Trans-critical carbon dioxide (CO2) circulating refrigeration system
CN110044093A (en) Two-stage Compression second vapor injection CO2Three-level backheat chiller-heat pump/refrigeration system
CN107014015A (en) Recovery type heat evaporating condensation type handpiece Water Chilling Units
CN108253650B (en) A kind of control method of critical-cross carbon dioxide combined heat-pump system
CN105042931A (en) Combined heat pump system adopting trans-critical circulation and absorption heat pump co-production
CN104913541B (en) Stirling cycle and the direct-coupled refrigeration machine of Vapor Compression Refrigeration Cycle and method
CN105004095B (en) A kind of trans critical cycle and the combined heat-pump system of two-stage absorption heat pump coproduction
CN110030756A (en) A kind of Trans-critical cycle CO with injector2Multi-temperature zone supermarket cold-hot combined supply system
CN105953464A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN101413739A (en) Double-effect heat pump circulation three-effect heat exchanger
CN209944799U (en) Enhanced vapor injection system and air source heat pump
CN206488501U (en) A kind of Gas-supplying enthalpy-increasing CO suitable for cold district2Part overlapping heat pump
CN206669949U (en) Recovery type heat evaporating condensation type handpiece Water Chilling Units
CN212299530U (en) Refrigerating system with pressure control device
CN205783983U (en) The heat high efficiente callback device of air source handpiece Water Chilling Units
CN104296286B (en) Heat source tower refrigerating and heating energy-saving equipment with ice storage and heat storage functions
CN209524655U (en) Coolant circulating system
CN202613753U (en) Carbon dioxide trans-critical two-stage steam compression type regenerative cycle heat pump
CN206131508U (en) Critical CO2 combined heat pump strides
CN109724284A (en) A kind of supercritical carbon dioxide refrigeration system of two-stage throttling
CN109612145A (en) A kind of CO that multi-injector group is strengthened2Dual temperature refrigeration system
CN209672629U (en) A kind of supercritical carbon dioxide refrigeration system of two-stage throttling
CN211060438U (en) Parallel compression machinery supercooling double-condenser combined supply system

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
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20170531

WD01 Invention patent application deemed withdrawn after publication