WO2008074990A1 - Air-source heat pump - Google Patents

Air-source heat pump Download PDF

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Publication number
WO2008074990A1
WO2008074990A1 PCT/GB2007/004722 GB2007004722W WO2008074990A1 WO 2008074990 A1 WO2008074990 A1 WO 2008074990A1 GB 2007004722 W GB2007004722 W GB 2007004722W WO 2008074990 A1 WO2008074990 A1 WO 2008074990A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat
heat pump
evaporator
temperature
air
Prior art date
Application number
PCT/GB2007/004722
Other languages
English (en)
French (fr)
Inventor
Stephen Forbes Pearson
Original Assignee
Star Refrigeration Limited
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
Priority claimed from GB0625122A external-priority patent/GB0625122D0/en
Priority claimed from GB0719403A external-priority patent/GB0719403D0/en
Application filed by Star Refrigeration Limited filed Critical Star Refrigeration Limited
Priority to CA002672831A priority Critical patent/CA2672831A1/en
Priority to AU2007336039A priority patent/AU2007336039A1/en
Priority to JP2009540844A priority patent/JP2010513830A/ja
Priority to US12/516,974 priority patent/US20100077779A1/en
Priority to NZ577589A priority patent/NZ577589A/en
Priority to EP07848469A priority patent/EP2092248A1/en
Publication of WO2008074990A1 publication Critical patent/WO2008074990A1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D3/00Hot-water central heating systems
    • F24D3/18Hot-water central heating systems using heat pumps
    • 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
    • F25B30/06Heat pumps characterised by the source of low potential heat
    • 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
    • F25B47/00Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
    • F25B47/006Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass for preventing frost
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00Heat sources or energy sources
    • F24D2200/04Gas or oil fired boiler
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00Heat sources or energy sources
    • F24D2200/08Electric heater
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00Heat sources or energy sources
    • F24D2200/12Heat pump
    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/01Heaters
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/12Hot water central heating systems using heat pumps
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/52Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency

Definitions

  • the present invention relates to air-source heat pumps, which extract heat from air at ambient temperature. Heat rejected at a higher temperature is used as a heat source for heating buildings etc.
  • the concept of the heat pump has been known for many years. It operates by extracting heat that is available from a source at a particular (lower) temperature and rejecting the heat together with the energy required to drive the heat pump at a higher temperature.
  • the rejected heat is typically used to heat a living space, such as a building, and may heat the air in the living space directly or via the use of a recirculating heat transfer fluid, such as water.
  • a refrigerator is a type of heat pump in which the main objective is to remove heat from the object being cooled. In some circumstances, it is possible to make use of the heat rejected as well as benefiting from the refrigeration effect.
  • Such heat pumps are particularly economic. However, in most circumstances it is difficult to match heating and cooling requirements; and in practice most systems are used either for heating or cooling.
  • Heat pumps operating in a vapour compression cycle require a source of energy to undertake the compression stage.
  • an absorption type heat pump dissolved refrigerant and solvent is pumped to high pressure as liquid and heat is used to boil refrigerant out of the solvent at a pressure under which the pure refrigerant can be condensed. The pure refrigerant is then reduced in pressure and transferred to an evaporator where it is capable of extracting heat.
  • an electrically or mechanically driven compressor is used, thereby avoiding the burning of fossil fuel in the building.
  • vapour compression heat pumps the amount of heat energy rejected into the building is normally several times greater than the amount of energy used to drive the heat pump.
  • the use of heat pumps for the heating of buildings is now becoming economic and may, in some circumstances, become mandatory. A large proportion of the heat output from a heat pump is provided by the environment and is therefore renewable.
  • Heat pumps are known which extract heat from the ground, or from ground water.
  • the present invention is concerned with heat pumps which use ambient air as the heat source.
  • heat is extracted from ambient air, which heats evaporating refrigerant in the evaporator. Work is then done on the refrigerant to compress it and heat it to a higher temperature. Heat is output from the compressed refrigerant at a higher temperature and is used as a heat source for heating the building etc.
  • heat pumps are at their most efficient when the difference between the temperature at which heat is absorbed and the temperature at which heat is rejected is small. However, this is the situation in which there is least requirement for heating of the building. The greatest quantity of heat is normally required when the ambient air is at its coldest and the heat pump is therefore at its least efficient.
  • Another disadvantage is that if the temperature of the evaporator is allowed to become too low due to the use of particularly cold ambient air, there is a danger that the evaporator will become choked with condensed water vapour in the form of frost.
  • some source of supplementary heating is normally required in cold weather.
  • auxiliary heating it is known to provide a source of auxiliary heating, but this is usually done electrically.
  • an auxiliary heater can be activated to provide additional heating, usually directly into the building to augment the heat from the heat pump. As the ambient temperature becomes colder, the efficiency of the heat pump is reduced and the need for additional auxiliary heating increases.
  • the present invention seeks to mitigate these disadvantages.
  • the present invention relates to the use of a heater which directly heats the incoming air to an air-source heat pump and thereby prevents frosting when the ambient air temperature is low. This effectively increases the temperature of the ambient air and thereby increases the efficiency of the heat pump, as well as reducing frosting.
  • the present invention provides an air-source heat pump wherein heat is extracted from air at ambient temperature by an evaporator and heat is rejected at a higher temperature in a condenser; the heat pump further comprising an auxiliary heater arranged to preheat the ambient air when required to prevent deposition of frost on the evaporator.
  • the auxiliary heater will only be operated when there is a risk of frost forming on the evaporator surfaces, for example under conditions of low temperature.
  • the auxiliary heater will be arranged to provide auxiliary heat to the ambient air when the ambient temperature falls below 10°C, particularly below 5°C, especially below 2°C and most especially below 1°C. When the relative humidity of the ambient air is high, the heating effect of the ambient air is greater and there is therefore less need for auxiliary heating.
  • the auxiliary heater will usually be arranged to operate by monitoring the evaporating pressure (or temperature) of refrigerant and then applying sufficient heat by means of the auxiliary heater to prevent the refrigerant evaporating at a pressure that would allow frost to form.
  • the auxiliary heater could be controlled dependent on the temperature and humidity of the ambient air; but this is more difficult to do in practice.
  • the auxiliary heater may be an electrical heater or may use waste heat from other sources. However, it is particularly preferred to employ a combustion heater, wherein flue gas from the combustion heater mixes with the ambient air.
  • the ambient air itself may be used as the air source for the combustion heater or the air may come from elsewhere.
  • the combustion heater itself contributes to the carbon dioxide emission of the system, it is nevertheless a relatively cheap and efficient form of auxiliary heating and one that will not be required during most of the heating season in a temperate climate.
  • the conditions will generally be arranged such that water as a product of combustion within the flue gases condenses as liquid on the surfaces of the evaporator and will thereby allow the latent heat of evaporation to be recovered.
  • the auxiliary combustion heater generally uses fossil fuels, such as hydrocarbons as the fuel source. It has been found that gas (such as North Sea gas), which has a low sulphur content does not cause corrosion of the evaporator surfaces.
  • the hydrocarbons are generally liquid or gaseous hydrocarbons, more particularly with less than 10 carbon atoms. C 1 -C 6 hydrocarbons are preferred, especially natural gas (which is largely methane), propane or butane.
  • the auxiliary heater is a combustion heater (e.g. a gas-fired boiler) which heats a fluid used to provide heat directly to the building (or anything else to be heated). Typically, the fluid is air or recirculating water. The heater is operated when additional heating is required, and provides heat directly to the building via the heated fluid. Also, flue gases from the boiler are mixed with ambient air before the air is passed over the evaporator, and thus provide additional heat input to the heat pump.
  • the gas fired boiler may be of the condensing type, to improve efficiency and reduce the heat content of the flue gases relative to the heat content of the heated fluid. It may alternatively be of the non-condensing type.
  • the heated fluid is usually air or recirculating water. Other gases or liquids could be used for other applications. Recirculating water is generally used to heat radiators. The heated air or water may provide under-floor heating in a building.
  • the heat pump may employ any suitable refrigerant.
  • a particular benefit of the present invention is that it allows the temperature at which heat is extracted (i.e. the evaporating temperature ) to be controlled so as to improve the performance of the heat pump.
  • the heat pump typically operates in an evaporation-condensation cycle using a source of energy to compress the volatile refrigerant.
  • the source of energy may be a compressor (such as an electrically driven compressor) or may be a liquid pump plus a source of heat in an absorption type system.
  • the heat pump will be arranged to extract heat from ambient air (preheated if necessary) in the range 5 - 15 0 C, particularly 7 - 12°C. Heat is typically rejected at a temperature in the range 30 - 35°C for direct air heating or for under- floor heating and, typically 50 - 55°C for the heating of circulating water.
  • Figure 1 is a schematic drawing of an air-source heat pump according to a first embodiment of the present invention, which utilises a combustion heater as the auxiliary heater;
  • Figures 2a and 2b are schematic drawings of a second embodiment, where the auxiliary heater is a gas-boiler which also heats a flow of recirculating heating water.
  • Figure 1 shows the circuit of an air-source heat pump having a compressor 1, a condenser 2, an expansion device 3, an evaporator 4, a casing 5, a fan 6, a gas burner 7, and interconnecting piping 14.
  • the heat pump contains a volatile refrigerant which is re-circulated.
  • liquified refrigerant from the condenser 2 at a temperature 55 0 C is expanded through an expansion device 3 into an evaporator 4 wherein the refrigerant evaporates within the pipes of the evaporator and extracts heat from ambient air.
  • the refrigerant at a temperature of 5 0 C is drawn from the evaporator by the compressor 1 , is compressed again to condensing pressure and is condensed in the condenser 2.
  • Condensing refrigerant at a temperature of 55°C rejects heat to the building to be heated and is thereby liquefied at a temperature of 55°C.
  • the heat extracted from the air stream plus the equivalent of the work put into the compressor is rejected from the condenser.
  • the refrigerant then flows through the interconnecting piping 14 back to the expansion device 3. At the expansion device the refrigerant is reduced to evaporating pressure and returned to the evaporator, where the cycle recommences.
  • Ambient air 10 is the source of heat for the heat pump. Ambient air is drawn into the casing 5 by means of a fan 6 and exits in the direction of the arrow. Under normal circumstances where the temperature of the ambient air is not too low, heat is extracted from the ambient air by heat exchange with the surfaces of the evaporator 4. However, when the temperature of the ambient air reduces there is the danger of frost collecting on the evaporator surfaces.
  • the temperature and/or pressure of the evaporator may be monitored by a sensor means (not shown) and when a predetermined value is reached, the combustion heater 7 is operated.
  • the combustion heater uses natural gas (which generally speaking does not produce corrosive flue gases which might damage the evaporator surfaces).
  • the auxiliary combustion heater 7 is operated to bring the temperature of the ambient air back to a preset temperature, whereby the danger of frosting is avoided and the efficiency of the heat pump is improved.
  • Water that condenses on the evaporator surfaces may be arranged to drain away via a drain (not shown).
  • the auxiliary gas burner 7 is ignited, thus providing an additional source of heat and preventing the formation of frost.
  • the burner may be controlled to provide a preset temperature in the ambient air flowing over the evaporator surfaces, or may be controlled to prevent the refrigerant evaporating at a temperature below the freezing point of water.
  • the ambient temperature is about 3 0 C at the limiting condition when the refrigerant evaporates at O 0 C. If ambient temperature falls below 3 0 C, the auxiliary heater will be engaged progressively till all the heat is being provided by the auxiliary heater.
  • the invention described therefore provides an effective method of providing heat without having to use fossil fuel except in exceptional circumstances.
  • fossil fuel does have to be used, it is used at maximum efficiency because the products of combustion are cooled down to about 3 0 C.
  • Figures 2a and 2b show a second embodiment (analogous parts are marked with the same reference numerals as in Figure 1) where the gas burner 7 not only provides flue gas into the evaporator 4 but also heats a recirculating flow 15 of heated water, which is used for heating the building (together with heat from the condenser 2).
  • Figure 2a shows a gas-fired boiler 7 housed in a separate chamber defined by a partition 8. Air flow 9 supplies the boiler with combustion air and flue gases 12 exit via boiler flue 13. Ambient air 10 enters the heat pump unit through louvres 16 in the wall of the casing 5, and mixes with flue gases 12 from the gas boiler. The mixed gas stream then passes over evaporator 4, as described above, and exits as stream 11.
  • a heated water circuit 15 is provided to heat radiators etc., within the building. It picks up heat rejected in condensor 2 during normal operation of the heat pump. However, when additional heating is required the gas-fired boiler 7 is operated. This provides additional heat to the recirculating water 15 and also provides flue gases, which provide additional heat to the ambient air 10 flowing over the evaporator 4. This provides a balance of direct heating via water stream 15 and indirect heating via the heat pump, which can be optimised to suit different conditions.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)
  • Central Heating Systems (AREA)
PCT/GB2007/004722 2006-12-16 2007-12-10 Air-source heat pump WO2008074990A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
CA002672831A CA2672831A1 (en) 2006-12-16 2007-12-10 Air-source heat pump
AU2007336039A AU2007336039A1 (en) 2006-12-16 2007-12-10 Air-source heat pump
JP2009540844A JP2010513830A (ja) 2006-12-16 2007-12-10 空気熱源ヒートポンプ
US12/516,974 US20100077779A1 (en) 2006-12-16 2007-12-10 Air-source heat pump
NZ577589A NZ577589A (en) 2006-12-16 2007-12-10 Heat pump with exhaust gas from combustion heater used to warm inlet air and fluid heated by combustion heater
EP07848469A EP2092248A1 (en) 2006-12-16 2007-12-10 Air-source heat pump

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
GB0625122A GB0625122D0 (en) 2006-12-16 2006-12-16 Heat pump
GB0625122.7 2006-12-16
GB0719403A GB0719403D0 (en) 2007-10-04 2007-10-04 Air-source heat pump
GB0719403.8 2007-10-04

Publications (1)

Publication Number Publication Date
WO2008074990A1 true WO2008074990A1 (en) 2008-06-26

Family

ID=39263063

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB2007/004722 WO2008074990A1 (en) 2006-12-16 2007-12-10 Air-source heat pump

Country Status (7)

Country Link
US (1) US20100077779A1 (zh)
EP (1) EP2092248A1 (zh)
JP (1) JP2010513830A (zh)
AU (1) AU2007336039A1 (zh)
CA (1) CA2672831A1 (zh)
NZ (1) NZ577589A (zh)
WO (1) WO2008074990A1 (zh)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102128493A (zh) * 2010-01-14 2011-07-20 良品机械股份有限公司 具有开放回路的大气取热式热泵热水器
CN101672563B (zh) * 2009-10-15 2011-11-09 康景安 互吸节能冰箱热水器
US20120000221A1 (en) * 2010-07-02 2012-01-05 Abdelaziz Omar Absorption heat pump system and method of using the same
CN103115433A (zh) * 2013-03-20 2013-05-22 广西玉林宏江能源科技有限公司 一种利用燃气燃烧补偿热源的节能热泵热水器
CN103216883A (zh) * 2013-03-20 2013-07-24 广西玉林宏江能源科技股份有限公司 一种利用燃气燃烧补偿空气热源热量不足的节能暖空调
CN103673396A (zh) * 2013-12-20 2014-03-26 湖南创化低碳环保科技有限公司 热交换系统
CN109442530A (zh) * 2018-10-16 2019-03-08 中国大唐集团科学技术研究院有限公司火力发电技术研究院 一种基于跨临界二氧化碳热泵的汽轮机余热利用系统
CN111207408A (zh) * 2020-01-17 2020-05-29 贵州中能投科技有限公司 余热智能回收系统
IE20230494A1 (en) * 2022-11-25 2024-06-05 Actionzero Escopod Ltd A heat pump apparatus with improved efficiency

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EP2460926A1 (en) * 2010-12-02 2012-06-06 Electrolux Home Products Corporation N.V. Heat pump dryer
CN102889683A (zh) * 2011-07-20 2013-01-23 珠海格力电器股份有限公司 一种控制方法、控制器及空气能热水器
CN105318453B (zh) * 2014-06-13 2018-03-30 美的集团股份有限公司 室外机化霜装置及空调器
KR101583603B1 (ko) * 2015-07-17 2016-01-12 세연기업 주식회사 하이브리드 히트 펌프 시스템
CN109708132A (zh) * 2019-03-04 2019-05-03 上海虹铂环保科技有限公司 一种废热烟气回收及均衡混流分配装置
CN112015207B (zh) * 2019-12-06 2021-08-24 安徽省农业科学院水稻研究所 一种野外人工气候室温度控制系统及温度控制方法
CN111678278B (zh) * 2020-06-24 2021-11-09 西安建筑科技大学 一种预热型空气源热泵抑霜系统及抑霜方法
CN111735101A (zh) * 2020-06-28 2020-10-02 武汉施尔诺新能源科技有限公司 一种二联供壁挂炉联动补偿系统

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DE3022571A1 (de) * 1980-06-16 1982-01-21 KKW Kulmbacher Klimageräte-Werk GmbH, 8650 Kulmbach Verfahren zum betreiben einer waermepumpe
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101672563B (zh) * 2009-10-15 2011-11-09 康景安 互吸节能冰箱热水器
CN102128493A (zh) * 2010-01-14 2011-07-20 良品机械股份有限公司 具有开放回路的大气取热式热泵热水器
US20120000221A1 (en) * 2010-07-02 2012-01-05 Abdelaziz Omar Absorption heat pump system and method of using the same
CN103115433A (zh) * 2013-03-20 2013-05-22 广西玉林宏江能源科技有限公司 一种利用燃气燃烧补偿热源的节能热泵热水器
CN103216883A (zh) * 2013-03-20 2013-07-24 广西玉林宏江能源科技股份有限公司 一种利用燃气燃烧补偿空气热源热量不足的节能暖空调
CN103115433B (zh) * 2013-03-20 2015-12-23 广西玉林宏江能源科技有限公司 一种利用燃气燃烧补偿热源的节能热泵热水器
CN103673396A (zh) * 2013-12-20 2014-03-26 湖南创化低碳环保科技有限公司 热交换系统
CN103673396B (zh) * 2013-12-20 2015-11-18 湖南创化低碳环保科技有限公司 热交换系统
CN109442530A (zh) * 2018-10-16 2019-03-08 中国大唐集团科学技术研究院有限公司火力发电技术研究院 一种基于跨临界二氧化碳热泵的汽轮机余热利用系统
CN111207408A (zh) * 2020-01-17 2020-05-29 贵州中能投科技有限公司 余热智能回收系统
CN111207408B (zh) * 2020-01-17 2022-04-19 贵州中能投科技有限公司 余热智能回收系统
IE20230494A1 (en) * 2022-11-25 2024-06-05 Actionzero Escopod Ltd A heat pump apparatus with improved efficiency

Also Published As

Publication number Publication date
US20100077779A1 (en) 2010-04-01
AU2007336039A1 (en) 2008-06-26
AU2007336039A2 (en) 2009-09-03
CA2672831A1 (en) 2008-06-26
EP2092248A1 (en) 2009-08-26
NZ577589A (en) 2011-05-27
JP2010513830A (ja) 2010-04-30

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