JP2012031239A - Compressor for refrigeration and air-conditioning, and refrigeration and air-conditioning apparatus - Google Patents
Compressor for refrigeration and air-conditioning, and refrigeration and air-conditioning apparatus Download PDFInfo
- Publication number
- JP2012031239A JP2012031239A JP2010169889A JP2010169889A JP2012031239A JP 2012031239 A JP2012031239 A JP 2012031239A JP 2010169889 A JP2010169889 A JP 2010169889A JP 2010169889 A JP2010169889 A JP 2010169889A JP 2012031239 A JP2012031239 A JP 2012031239A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- refrigerating
- compressor
- refrigerant
- air
- 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.)
- Withdrawn
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
-
- 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
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/04—Compression machines, plants or systems with non-reversible cycle with compressor of rotary type
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
- C09K5/041—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
- C09K5/042—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising compounds containing carbon and hydrogen only
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
- C09K5/041—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
- C09K5/044—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
- C09K5/045—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds containing only fluorine as halogen
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M105/00—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
- C10M105/08—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing oxygen
- C10M105/32—Esters
- C10M105/38—Esters of polyhydroxy compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M171/00—Lubricating compositions characterised by purely physical criteria, e.g. containing as base-material, thickener or additive, ingredients which are characterised exclusively by their numerically specified physical properties, i.e. containing ingredients which are physically well-defined but for which the chemical nature is either unspecified or only very vaguely indicated
- C10M171/008—Lubricant compositions compatible with refrigerants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
- F04B39/02—Lubrication
-
- 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
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/10—Components
- C09K2205/12—Hydrocarbons
- C09K2205/126—Unsaturated fluorinated hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/24—Only one single fluoro component present
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
- C10M2203/10—Petroleum or coal fractions, e.g. tars, solvents, bitumen
- C10M2203/106—Naphthenic fractions
- C10M2203/1065—Naphthenic fractions used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/02—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
- C10M2205/028—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms
- C10M2205/0285—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/28—Esters
- C10M2207/283—Esters of polyhydroxy compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/28—Esters
- C10M2207/283—Esters of polyhydroxy compounds
- C10M2207/2835—Esters of polyhydroxy compounds used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/04—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an alcohol or ester thereof; bound to an aldehyde, ketonic, ether, ketal or acetal radical
- C10M2209/043—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an alcohol or ester thereof; bound to an aldehyde, ketonic, ether, ketal or acetal radical used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/10—Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/103—Polyethers, i.e. containing di- or higher polyoxyalkylene groups
- C10M2209/105—Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing three carbon atoms only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/02—Viscosity; Viscosity index
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/09—Characteristics associated with water
- C10N2020/097—Refrigerants
- C10N2020/101—Containing Hydrofluorocarbons
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/09—Characteristics associated with water
- C10N2020/097—Refrigerants
- C10N2020/103—Containing Hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/06—Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/30—Refrigerators lubricants or compressors lubricants
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- Lubricants (AREA)
Abstract
【課題】冷凍空調用圧縮機の耐摩耗性を向上するとともに、この圧縮機を用いた冷凍空調装置の高効率化を実現する。
【解決手段】2、3、3、3−テトラフルオロプロペン、1、3、3、3−テトラフルオロプロペン等を含む冷媒に、ポリオールエステル油等の冷凍機油主剤と、添加ポリオールエステル油とを含む冷凍機油を混合して封入した冷凍空調用圧縮機を用いる。添加ポリオールエステル油の組成は1〜30重量%である。
【選択図】図1An object of the present invention is to improve the wear resistance of a compressor for refrigeration and air conditioning, and to realize high efficiency of a refrigeration air conditioner using the compressor.
A refrigerant containing 2,3,3,3-tetrafluoropropene, 1,3,3,3-tetrafluoropropene, and the like includes a refrigerating machine main agent such as polyol ester oil and an added polyol ester oil. A compressor for refrigerating and air conditioning in which refrigeration oil is mixed and sealed is used. The composition of the added polyol ester oil is 1 to 30% by weight.
[Selection] Figure 1
Description
本発明は、ヒートポンプサイクルを用いた冷凍空調用圧縮機及び冷凍空調装置に関する。 The present invention relates to a refrigeration and air conditioning compressor and a refrigeration air conditioning apparatus using a heat pump cycle.
冷凍空調機器分野における地球環境対策としては、オゾン層破壊物質として冷媒や断熱材に用いられていたCFC(Chlorofluorocarbons)やHCFC(Hydrochlorofluorocarbons)の代替、並びに、地球温暖化対策としての高効率化や冷媒に用いられているHFC(Hydrofluorocarbons)の代替が挙げられ、これらが積極的に進められてきた。 Global environmental measures in the field of refrigerating and air-conditioning equipment include substitution of CFC (Chlorofluorocarbons) and HCFC (Hydrochlorofluorocarbons), which have been used as refrigerants and heat insulating materials as ozone depleting substances, as well as higher efficiency and refrigerants as a countermeasure against global warming Substitutes for HFC (Hydrofluorocarbons) used in Japan, and these have been actively promoted.
オゾン層破壊物質であるCFCやHCFCの代替としては、オゾン層を破壊しないこと、毒性や燃焼性が低いこと、効率を確保できることを主眼として冷媒や断熱材の選定、並びに機器開発が進められた。その結果、冷蔵庫の断熱材においては、CFC11をHCFC141b、シクロペンタンの順に発泡剤を代替していき、現在は、真空断熱材との併用に移行している。 As alternatives to CFCs and HCFCs, which are ozone-depleting substances, the selection of refrigerants and heat insulating materials and equipment development were promoted with the main objective of not destroying the ozone layer, low toxicity and low flammability, and ensuring efficiency. . As a result, in the heat insulating material of the refrigerator, the foaming agent is replaced in the order of HCFC141b and cyclopentane in CFC11, and now it is shifted to the combined use with the vacuum heat insulating material.
冷媒としては、冷蔵庫やカーエアコンにおいてCFC12CをHFC134a(地球温暖化係数GWP(Global Warming Potential)=1430)の順に代替し、ルームエアコンやパッケージエアコンにおいてHCFC22をR410A(HFC32/HFC125(50/50重量%)混合物:GWP=2088)に代替した。 As a refrigerant, CFC12C is replaced with HFC134a (Global Warming Potential GWP = 1430) in the order of refrigerators and car air conditioners, and HCFC22 is replaced with R410A (HFC32 / HFC125 (50/50% by weight) in room air conditioners and packaged air conditioners. ) Mixture: replaced with GWP = 2088).
しかし、1997年に京都で開催された気候変動枠組条約第3回締約国会議(COP3)で、HFC排出量が温室効果ガスとしてCO2換算されて規制対象となったため、HFCの削減が進められることとなった。 However, at the Conference of the Parties to the 3rd Framework Convention on Climate Change, which was held in Kyoto in 1997 (COP3), for HFC emissions has become subject to regulation are terms of CO 2 as a greenhouse gas, reduction of HFC is advanced It became a thing.
そこで、家庭用冷蔵庫においては、冷媒封入量が少なく、可燃性冷媒も製造上使用可能と判断され、HFC134aを可燃性のR600a(イソブタン:GWP=3)へと代替した。さらに、世論の高まりにより、現在は、カーエアコン用のHFC134aやルームエアコン並びにパッケージエアコン用のR410Aにも目が向けられている。また、業務用冷蔵庫においては、R600aの封入量が多く、可燃性の危惧から、現在でもHFC134aが使用されている。 In view of this, in the refrigerator for home use, it was judged that the amount of refrigerant enclosed was small and a flammable refrigerant could be used for manufacturing, and HFC134a was replaced with flammable R600a (isobutane: GWP = 3). Furthermore, due to the growing public opinion, attention is now focused on the HFC134a for car air conditioners, the room air conditioner and the R410A for packaged air conditioners. Moreover, in commercial refrigerators, the amount of R600a enclosed is large, and HFC134a is still used because of the fear of flammability.
現実には、2001年に施行された家電リサイクル法(特定家庭用機器再商品化法)や2003年施行の自動車リサイクル法(使用済自動車の再資源化等に関する法律)により機器のリサイクルが義務化され、冷媒として用いられているHFC等が回収され処理されている。しかし、EU(欧州連合)では、2006年指令(Directive 2006/40/EC)において、カーエアコンに用いる冷媒としてGWP>150の冷媒の使用が2011年1月出荷分から禁じられた。これを受けて、カーエアコン業界では様々な動きをみせており、ルームエアコンもR410Aがいずれは規制されるのではないかと言う懸念が生じている。前記EU指令に基づき、2011年に定置型エアコンを含めた規制見直しの可能性もあり、代替冷媒の検討が加速している。 In reality, recycling of equipment is obligated by the Home Appliance Recycling Law (Specific Home Appliance Recycling Law) enacted in 2001 and the Automobile Recycling Law (Law Concerning Recycling of Used Cars) Enforced in 2003 HFC and the like used as a refrigerant are collected and processed. However, in the EU (European Union), in the 2006 Directive (Directive 2006/40 / EC), the use of a refrigerant with GWP> 150 as a refrigerant used in a car air conditioner was prohibited from the shipment in January 2011. In response, the car air conditioner industry has made various moves, and there is a concern that room air conditioners will eventually be restricted by R410A. Based on the EU directive, there is a possibility of reviewing regulations including stationary air conditioners in 2011, and studies on alternative refrigerants are accelerating.
これらの代替冷媒としては、HFC134aと同等の熱物性を有し、低GWP、低毒性、低可燃性などの理由から、2、3、3、3−テトラフルオロプロペン(HFO1234yf(Hydrofluoroolefine)(GWP=4)や1、3、3、3−テトラフルオロプロペン(HFO1234ze)(GWP=10)の単独もしくはこれらの混合冷媒が候補とされている。2、3、3、3−テトラフルオロプロペンと混合する冷媒としては、ジフルオロメタン(HFC32)が主である。 These alternative refrigerants have the same thermophysical properties as HFC134a, and because of low GWP, low toxicity, low flammability, etc., 2, 3, 3, 3-tetrafluoropropene (HFO1234yf (Hydrofluorinefine) (GWP = 4) or 1,3,3,3-tetrafluoropropene (HFO1234ze) (GWP = 10) alone or a mixed refrigerant thereof is a candidate, and is mixed with 2,3,3,3-tetrafluoropropene. As the refrigerant, difluoromethane (HFC32) is mainly used.
さらに、低燃焼性のために許容されるGWPによっては、HFC134aやHFC125を混合することも考えられる。その他の冷媒としては、プロパン、プロピレンなどのハイドロカーボンやフルオロエタン(HFC161)、ジフルオロエタン(HFC152a)、ジフルオロメタン(HFC32)などの低GWPのハイドロフルオロカーボンが挙げられている。 Furthermore, HFC134a and HFC125 may be mixed depending on the GWP allowed for low combustibility. Other refrigerants include hydrocarbons such as propane and propylene, and low GWP hydrofluorocarbons such as fluoroethane (HFC161), difluoroethane (HFC152a), and difluoromethane (HFC32).
一方、冷凍機油は、密閉型電動圧縮機に使用され、その摺動部の潤滑、密封、冷却等の役割を果たすものである。 On the other hand, refrigeration oil is used in a hermetic electric compressor and plays a role of lubrication, sealing, cooling and the like of a sliding portion thereof.
エアコンにおいては2006年から改正された省エネ法(エネルギーの使用の合理化に関する法律)により、実使用状態に沿った省エネ性能を示す指標としてAPF(Annual Performance Factor)が採用され、圧縮機にも更なる省エネルギー化及び高効率化が必要とされている。このように使用条件が厳しくなることから、信頼性確保の面において潤滑性が良い冷凍機油が要求される。 In the air conditioner, APF (Annual Performance Factor) is adopted as an index indicating energy saving performance in accordance with the actual use state according to the Energy Saving Law (Act on the Rational Use of Energy) revised from 2006. There is a need for energy saving and high efficiency. Since use conditions become severe in this way, refrigerating machine oil with good lubricity is required in terms of ensuring reliability.
2、3、3、3−テトラフルオロプロペン(HFO1234yf)及び1、3、3、3−テトラフルオロプロペン(HFO1234ze)の単独冷媒若しくはこれらの冷媒を含む混合冷媒を用いた圧縮機に用いる冷凍機油としては、上記の状況から、ポリアルキレングリコール油、鉱油、ポリαオレフィン油及びアルキルベンゼン油が開示されている(例えば、特許文献1)。 As refrigerating machine oil used in a compressor using a single refrigerant of 2,3,3,3-tetrafluoropropene (HFO1234yf) and 1,3,3,3-tetrafluoropropene (HFO1234ze) or a mixed refrigerant containing these refrigerants From the above situation, polyalkylene glycol oil, mineral oil, poly α-olefin oil and alkylbenzene oil are disclosed (for example, Patent Document 1).
特許文献2には、パラフィン系冷凍機油、ナフテン系冷凍機油及び合成冷凍機油の中の少なくとも一種から成る冷凍機油中に、常圧で沸点が50〜250℃で、かつ、粘度が5センチストークス/40℃以下である留分を含む冷凍機油組成物が開示されている。 Patent Document 2 discloses that a refrigerating machine oil composed of at least one of paraffinic refrigerating machine oil, naphthenic refrigerating machine oil, and synthetic refrigerating machine oil has a boiling point of 50 to 250 ° C. at normal pressure and a viscosity of 5 centistokes / A refrigerating machine oil composition comprising a fraction that is 40 ° C. or lower is disclosed.
このほか、特許文献3及び4〜9には、HFO−1234yf、HFO−1225yeZ、トランス−1、3、3、3 −ペンタフルオロプロパン(transHFO−1234ze)、1、1−ジフルオロエタン(HFC−152a)、1、1、1、2、3、3、3−ヘプタフルオロプロパン(HFC−227ea)、1、1、1、2−テトラフルオロエタン(HFC−134a)、1、1、1、2、2−ペンタフルオロエタン(HFC−125)等を含む共沸混合物様組成物、及び鉱物油(パラフィン油又はナフテン油を含む。)、シリコーン油、ポリアルキルベンゼン、ポリオールエステル、ポリアルキレングリコール、ポリアルキレングリコールエステル、ポリビニルエーテル、ポリ(α−オレフィン)、ハロカーボンオイル等の潤滑剤が開示されている。 In addition, Patent Documents 3 and 4-9 include HFO-1234yf, HFO-1225yeZ, trans-1,3,3,3-pentafluoropropane (transHFO-1234ze), 1,1-difluoroethane (HFC-152a). 1, 1, 1, 2, 3, 3, 3-heptafluoropropane (HFC-227ea), 1, 1, 1, 2-tetrafluoroethane (HFC-134a), 1, 1, 1, 2, 2 -An azeotrope-like composition containing pentafluoroethane (HFC-125), etc., and mineral oil (including paraffin oil or naphthenic oil), silicone oil, polyalkylbenzene, polyol ester, polyalkylene glycol, polyalkylene glycol ester , Polyvinyl ether, poly (α-olefin), halocarbon oil, etc. There has been disclosed.
2、3、3、3−テトラフルオロプロペン(HFO1234yf)及び1、3、3、3−テトラフルオロプロペン(HFO1234ze)は、R410Aと比較して低圧冷媒であるため、冷媒循環量を得るために圧縮機押除の大容量化や高速回転化が必須である。このため、上記の冷凍機油の場合、圧縮機軸受などの摺動部において耐摩耗性に関する課題が残る。 2,3,3,3-tetrafluoropropene (HFO1234yf) and 1,3,3,3-tetrafluoropropene (HFO1234ze) are low-pressure refrigerants compared to R410A, so they are compressed to obtain a refrigerant circulation rate. It is essential to increase the capacity and speed of the machine. For this reason, in the case of the above-described refrigerating machine oil, a problem relating to wear resistance remains in a sliding portion such as a compressor bearing.
また、HFO1234yf、HFO1234ze、プロパン、プロピレン、フルオロエタン等の冷媒は、上記の冷凍機油との溶解性が非常に高く、圧縮機内において冷媒の溶け込みが大きいことから、冷凍機油における冷媒溶解粘度が低下する。このため、圧縮部のシール性の低下、さらには、摺動部の摩耗量の増加という問題が生じる。 In addition, refrigerants such as HFO1234yf, HFO1234ze, propane, propylene, and fluoroethane have a very high solubility in the above-described refrigerating machine oil, and the refrigerant has a high solubility in the compressor, so that the refrigerant melt viscosity in the refrigerating machine oil decreases. . For this reason, the problem of the fall of the sealing performance of a compression part and the increase in the amount of wear of a sliding part arises.
上述の理由から、冷凍空調装置には、機器の効率向上と耐摩耗性とを両立できる冷凍機油を用いることが好ましい。 For the reasons described above, it is preferable to use a refrigerating machine oil that can achieve both improvement in equipment efficiency and wear resistance for the refrigerating and air-conditioning apparatus.
本発明の目的は、冷媒として2、3、3、3−テトラフルオロプロペン、1、3、3、3−テトラフルオロプロペン等を含む冷媒、又はプロパン、プロピレン等のハイドロカーボン、フルオロエタン(HFC161)、ジフルオロエタン(HFC152a)、ジフルオロメタン(HFC32)、R410A等の冷凍空調用冷媒を用いる冷凍空調用圧縮機の耐摩耗性を向上するとともに、この圧縮機を用いた冷凍空調機器の高効率化を実現することにある。 An object of the present invention is to provide a refrigerant containing 2,3,3,3-tetrafluoropropene, 1,3,3,3-tetrafluoropropene or the like as a refrigerant, or a hydrocarbon such as propane or propylene, or fluoroethane (HFC161). In addition to improving the wear resistance of refrigeration and air conditioning compressors that use refrigerants for refrigeration and air conditioning such as difluoroethane (HFC152a), difluoromethane (HFC32), R410A, etc., and realizing higher efficiency in refrigeration and air conditioning equipment using this compressor There is to do.
本発明の冷凍空調用圧縮機は、2、3、3、3−テトラフルオロプロペン、1、3、3、3−テトラフルオロプロペン等を含む冷媒に、ポリオールエステル油等の冷凍機油主剤と、添加ポリオールエステル油とを含む冷凍機油を混合して封入したものであり、前記添加ポリオールエステル油の組成が1〜30重量%であることを特徴とする。 The compressor for refrigerating and air-conditioning of the present invention is added to a refrigerant containing 2, 3, 3, 3-tetrafluoropropene, 1, 3, 3, 3-tetrafluoropropene and the like, and a refrigerating machine oil main component such as polyol ester oil, and the like A refrigerating machine oil containing a polyol ester oil is mixed and sealed, and the composition of the added polyol ester oil is 1 to 30% by weight.
本発明によれば、冷凍機油の添加剤として環境に有害なリン系極圧剤を用いずに圧縮機の性能向上と耐摩耗性とを両立した圧縮機を得ることができる。 ADVANTAGE OF THE INVENTION According to this invention, the compressor which was compatible with the performance improvement of a compressor, and abrasion resistance can be obtained, without using the phosphorus extreme pressure agent harmful | toxic to an environment as an additive of refrigerating machine oil.
また、本発明によれば、冷凍機油の添加剤として環境に有害なリン系極圧剤を用いずに冷凍空調装置の性能向上と長期信頼性とを両立できる環境に配慮した冷凍空調装置を得ることができる。 In addition, according to the present invention, an environment-friendly refrigeration air conditioner that can achieve both improved performance and long-term reliability of a refrigeration air conditioner without using a phosphorous extreme pressure agent harmful to the environment as an additive for refrigeration oil is obtained. be able to.
以下、本発明の一実施形態に係る冷凍空調用圧縮機及びこれを用いた冷凍空調装置について説明する。 Hereinafter, a refrigerating and air conditioning compressor according to an embodiment of the present invention and a refrigerating and air conditioning apparatus using the same will be described.
前記冷凍空調用圧縮機は、2、3、3、3−テトラフルオロプロペン、1、3、3、3−テトラフルオロプロペン若しくはジフルオロメタンを含む冷媒又はR410Aである封入冷媒に、下記化学式(1)及び(2)で表されるポリオールエステル油(式中、R1は炭素数5〜9のアルキル基を表す。)からなる群から選択される少なくとも一種類の基油を含む冷凍機油主剤と、下記化学式(3)で表される添加ポリオールエステル油(式中、R2は炭素数7〜9のアルキル基を表す。)とを含む冷凍機油を混合して封入したものである。 The compressor for refrigerating and air-conditioning uses a refrigerant containing 2,3,3,3-tetrafluoropropene, 1,3,3,3-tetrafluoropropene or difluoromethane, or an enclosed refrigerant which is R410A, represented by the following chemical formula (1) And a refrigerating machine main agent containing at least one kind of base oil selected from the group consisting of polyol ester oils represented by (2) (wherein R 1 represents an alkyl group having 5 to 9 carbon atoms); A refrigerating machine oil containing an additive polyol ester oil represented by the following chemical formula (3) (wherein R 2 represents an alkyl group having 7 to 9 carbon atoms) is mixed and enclosed.
前記冷凍空調用圧縮機は、2、3、3、3−テトラフルオロプロペン、1、3、3、3−テトラフルオロプロペン、プロパン、プロピレン若しくはフルオロエタンを含む冷媒である封入冷媒に、鉱油若しくはポリビニルエーテル油又は上記化学式(1)及び(2)で表されるポリオールエステル油(式中、R1は炭素数5〜9のアルキル基を表す。)からなる群から選択される少なくとも一種類の基油を含み低温側臨界溶解温度が−30℃以下である冷凍機油主剤と、上記化学式(3)で表される添加ポリオールエステル油(式中、R2は炭素数7〜9のアルキル基を表す。)とを含む冷凍機油を混合して封入したものである。そして、添加ポリオールエステル油の組成は1〜30重量%である。 The compressor for refrigerating and air-conditioning uses mineral oil or polyvinyl as an enclosed refrigerant, which is a refrigerant containing 2, 3, 3, 3-tetrafluoropropene, 1, 3, 3, 3-tetrafluoropropene, propane, propylene, or fluoroethane. At least one group selected from the group consisting of an ether oil or a polyol ester oil represented by the above chemical formulas (1) and (2) (wherein R 1 represents an alkyl group having 5 to 9 carbon atoms). Refrigerating machine oil main agent containing oil and having a low temperature side critical dissolution temperature of −30 ° C. or less, and an added polyol ester oil represented by the above chemical formula (3) (wherein R 2 represents an alkyl group having 7 to 9 carbon atoms) )) Is mixed and sealed. The composition of the added polyol ester oil is 1 to 30% by weight.
前記冷凍空調用圧縮機においては、冷凍機油主剤の40℃における動粘度が25〜120mm2/sの範囲であり、添加ポリオールエステル油の40℃における動粘度が180mm2/s以上であることが望ましい。 In the refrigerating and air-conditioning compressor, kinematic viscosity at 40 ° C. of the refrigerating machine oil base resin is in the range of 25~120mm 2 / s, that kinematic viscosity at 40 ° C. for the addition polyol ester oil is 180 mm 2 / s or more desirable.
前記冷凍空調装置は、前記冷凍空調用圧縮機と、前記冷凍空調用圧縮機から吐出された封入冷媒の熱を放熱するための熱交換器と、熱交換器から流出する封入冷媒を減圧するための減圧部と、減圧部にて減圧された封入冷媒を加熱するための熱交換器とを備えている。 The refrigerating and air-conditioning apparatus depressurizes the refrigerating and air-conditioning compressor, a heat exchanger for dissipating heat of the enclosed refrigerant discharged from the refrigerating and air-conditioning compressor, and the enclosed refrigerant flowing out of the heat exchanger. And a heat exchanger for heating the sealed refrigerant decompressed by the decompression unit.
前記冷凍空調装置においては、冷凍機油主剤の40℃における動粘度は、25〜120mm2/sであり、添加ポリオールエステル油の鉄系材料に対する吸着能力は、冷凍機油主剤に比べて2倍以上高いことが望ましい。 In the refrigerating and air-conditioning apparatus, the kinematic viscosity at 40 ° C. of the refrigerating machine oil main agent is 25 to 120 mm 2 / s, and the adsorption ability of the added polyol ester oil to the iron-based material is twice or more higher than that of the refrigerating machine oil main agent. It is desirable.
前記冷凍空調用圧縮機は、地球温暖化係数が1000以下である冷媒、又はR410Aである冷凍空調用冷媒に、上記化学式(1)及び(2)で表されるポリオールエステル油(式中、R1は炭素数5〜9のアルキル基を表す。)からなる群から選択される少なくとも一種類の基油を含み40℃における動粘度が25〜120mm2/sである冷凍機油主剤と、上記化学式(3)で表される添加ポリオールエステル油(式中、R2は炭素数7〜9のアルキル基を表す。)とを含む冷凍機油を混合して封入したものである。 The compressor for refrigerating and air-conditioning is obtained by adding a polyol ester oil represented by the above chemical formulas (1) and (2) to a refrigerant having a global warming potential of 1000 or less or a refrigerating and air-conditioning refrigerant having R410A (wherein R 1 represents an alkyl group having 5 to 9 carbon atoms.) A main component of a refrigerating machine oil containing at least one base oil selected from the group consisting of: a kinematic viscosity at 40 ° C. of 25 to 120 mm 2 / s, and the above chemical formula Refrigerating machine oil containing additive polyol ester oil represented by (3) (wherein R 2 represents an alkyl group having 7 to 9 carbon atoms) is mixed and enclosed.
添加ポリオールエステル油の組成は、1〜30重量%であることが望ましい。 The composition of the added polyol ester oil is desirably 1 to 30% by weight.
前記冷凍空調用圧縮機は、モータが内蔵されたスクロール式もしくはロータリー式密閉型圧縮機、このほか、ツインロータリー式圧縮機、2段圧縮ロータリー式圧縮機、及びローラ及びベーンが一体化されたスイング式圧縮機であり、冷凍機油主剤の40℃における動粘度が25mm2/sから120mm2/s以下であり、添加ポリオールエステル油の40℃における動粘度が180mm2/s以上であることが望ましい。 The compressor for refrigeration and air conditioning includes a scroll type or rotary type hermetic compressor with a built-in motor, a twin rotary type compressor, a two-stage compression rotary type compressor, and a swing in which rollers and vanes are integrated. It is desirable that the kinematic viscosity at 40 ° C. of the refrigerating machine oil main component is 25 mm 2 / s to 120 mm 2 / s or less, and the kinematic viscosity at 40 ° C. of the added polyol ester oil is preferably 180 mm 2 / s or more. .
前記冷凍空調用圧縮機は、鉄系材料で形成された摺動部を含み、摺動部における接触面圧が10MPa以上である。 The compressor for refrigerating and air-conditioning includes a sliding portion formed of an iron-based material, and a contact surface pressure at the sliding portion is 10 MPa or more.
前記冷凍空調用圧縮機において、添加ポリオールエステル油は、鉄系材料に対する吸着能力が冷凍機油主剤より2倍以上高い。さらに、添加ポリオールエステル油の鉄系材料に対する吸着能力は、2倍以上が望ましく、4倍以上が更に望ましい。 In the compressor for refrigerating and air-conditioning, the added polyol ester oil has an adsorption capacity for iron-based materials that is twice or more higher than that of the refrigerating machine oil main agent. Furthermore, the adsorption capacity of the added polyol ester oil to the iron-based material is preferably 2 times or more, and more preferably 4 times or more.
前記冷凍空調装置は、上記のスクロール式もしくはロータリー式圧縮機を用いるものである。 The refrigeration air conditioner uses the scroll type or rotary type compressor described above.
以下、実施例を用いて詳細に説明する。 Hereinafter, it demonstrates in detail using an Example.
実施例は、冷媒として2、3、3、3−テトラフルオロプロペン若しくは1、3、3、3−テトラフルオロプロペン又はこれらを含む混合冷媒、又はプロパン、プロピレン、フルオロエタン、ジフルオロメタン若しくはR410Aを用いた圧縮機及びこの圧縮機を用いた冷凍空調装置について開示するものである。 The examples use 2,3,3,3-tetrafluoropropene or 1,3,3,3-tetrafluoropropene or a mixed refrigerant containing these, or propane, propylene, fluoroethane, difluoromethane or R410A as the refrigerant. A compressor and a refrigerating and air-conditioning apparatus using the compressor are disclosed.
本明細書において、冷凍空調用冷媒は、2、3、3、3−テトラフルオロプロペン若しくは1、3、3、3−テトラフルオロプロペン又はこれらを含む混合冷媒、又はプロパン、プロピレン、フルオロエタン、ジフルオロメタン等のGWPが1000以下である冷媒、及びR410Aを含む。 In this specification, the refrigerant for refrigerating and air-conditioning is 2, 3, 3, 3-tetrafluoropropene, 1, 3, 3, 3-tetrafluoropropene or a mixed refrigerant containing these, propane, propylene, fluoroethane, difluoro. A refrigerant having a GWP of 1000 or less, such as methane, and R410A.
実施例の冷凍機油は、鉄系材料に対する吸着能力が基油よりも極めて高い添加ポリオールエステル油を含む。 The refrigerating machine oil of an Example contains the addition polyol ester oil whose adsorption capacity with respect to an iron-type material is very higher than a base oil.
添加ポリオールエステル油と比較して吸着能力が低い基油としては、鉱油、ポリビニルエーテル油、及び分子構造中にエステル基を有するポリオールエステル油が挙げられる。 Examples of the base oil having a low adsorption capacity as compared with the added polyol ester oil include mineral oil, polyvinyl ether oil, and polyol ester oil having an ester group in the molecular structure.
鉱油としては、ナフテン系鉱油及びパラフィン系鉱油を用いることができる。これらの鉱油としては、例えば、パラフィン基系原油、中間基系原油若しくはナフテン基系原油を常圧蒸留する、又は常圧蒸留の残渣油を減圧蒸留して得られる留出油を常法に従って精製することによって得られる精製油、精製後に更に深脱ロウ処理することによって得られる深脱ろう油、水素化処理によって得られる水素化処理油などが挙げられる。その際の精製法に特に制限はなく、様々な方法が使用される。 As mineral oil, naphthenic mineral oil and paraffinic mineral oil can be used. As these mineral oils, for example, a distillate obtained by subjecting paraffin-based crude oil, intermediate-based crude oil, or naphthenic-based crude oil to atmospheric distillation, or distilling the residual oil of atmospheric distillation under reduced pressure is refined according to a conventional method. Refined oil obtained by the above, deep dewaxed oil obtained by further deep dewaxing after purification, hydrotreated oil obtained by hydrotreatment, and the like. There are no particular limitations on the purification method at that time, and various methods can be used.
ポリオールエステル油は、多価アルコールと一価の脂肪酸との縮合反応により得られる。 The polyol ester oil is obtained by a condensation reaction between a polyhydric alcohol and a monovalent fatty acid.
ポリオールエステル油としては、熱安定性に優れるヒンダードタイプが好ましく、多価アルコールとして好ましいものは、例えば、ネオペンチルグリコール、トリメチロールプロパン、ペンタエリスリトール等である。 As the polyol ester oil, a hindered type having excellent thermal stability is preferable, and as the polyhydric alcohol, neopentyl glycol, trimethylolpropane, pentaerythritol and the like are preferable.
一価の脂肪酸としては、n−ペンタン酸、n−ヘキサン酸、n−ヘプタン酸、n−オクタン酸、2−メチルブタン酸、2−メチルペンタン酸、2−メチルヘキサン酸、2−エチルヘキサン酸、イソオクタン酸、3、5、5−トリメチルヘキサン酸等があり、これらを単独又は2種類以上を混合して用いる。 Monovalent fatty acids include n-pentanoic acid, n-hexanoic acid, n-heptanoic acid, n-octanoic acid, 2-methylbutanoic acid, 2-methylpentanoic acid, 2-methylhexanoic acid, 2-ethylhexanoic acid, There are isooctanoic acid, 3,5,5-trimethylhexanoic acid and the like, which are used alone or in combination of two or more.
鉄系材料に吸着能力が高い添加ポリオールエステル油としては、分子構造中にエステル基を多く含むポリオールエステル油が望ましく、多価アルコールと一価の脂肪酸とから合成されるヒンダードタイプであるジペンタエリスリトールが挙げられる。 As an added polyol ester oil having a high adsorption capacity for iron-based materials, a polyol ester oil containing a large number of ester groups in its molecular structure is desirable, and dipenta is a hindered type synthesized from a polyhydric alcohol and a monovalent fatty acid. Erythritol is mentioned.
一価の脂肪酸としては、n−ペンタン酸、n−ヘキサン酸、n−ヘプタン酸、n−オクタン酸、2−メチルブタン酸、2−メチルペンタン酸、2−メチルヘキサン酸、2−エチルヘキサン酸、イソオクタン酸、3、5、5−トリメチルヘキサン酸等があり、これらを単独又は2種類以上を混合して用いる。 Monovalent fatty acids include n-pentanoic acid, n-hexanoic acid, n-heptanoic acid, n-octanoic acid, 2-methylbutanoic acid, 2-methylpentanoic acid, 2-methylhexanoic acid, 2-ethylhexanoic acid, There are isooctanoic acid, 3,5,5-trimethylhexanoic acid and the like, which are used alone or in combination of two or more.
実施例の空調装置及び冷凍機に用いる冷凍機油の粘度グレードは、圧縮機の種類により異なるが、スクロール式圧縮機では、40℃における動粘度が46〜120mm2/sの範囲が好ましい。また、ロータリー式圧縮機では、40℃における動粘度が25〜70mm2/sの範囲が好ましい。 Although the viscosity grade of the refrigerating machine oil used for the air conditioner and refrigerator of an Example changes with kinds of compressors, in the scroll type compressor, the range whose kinematic viscosity in 40 degreeC is 46-120 mm < 2 > / s is preferable. In the rotary compressor, the kinematic viscosity at 40 ° C. is preferably in the range of 25 to 70 mm 2 / s.
電気絶縁の耐熱クラスは、電気絶縁の耐熱クラスおよび耐熱性評価JEC−6147(電気学会電気規格調査標準規格)で規定されており、冷凍空調機用圧縮機に採用されている絶縁材料も前記規格の耐熱種により選定される。しかし、冷凍空調機器用の有機絶縁材料の場合、冷媒雰囲気中という特殊な環境で使用されるため、温度以外にも圧力による変形・変性を抑制することを考慮する必要がある。また、冷媒や冷凍機油といった有極性化合物にも接触するため、耐溶剤性、耐抽出性、熱的・化学的・機械的安定性、耐冷媒性(クレージング(皮膜にストレスを与えた後、冷媒に浸漬すると発生する微細な蛇腹状クラック)、ブリスタ(皮膜に吸収された冷媒が、温度上昇によって引き起こされる皮膜の気泡))等も考慮しなくてはいけない。 The heat insulation class of electrical insulation is defined by the heat insulation class of electrical insulation and the heat resistance evaluation JEC-6147 (The Institute of Electrical Engineers of Japan, electrical standard survey standard), and the insulation materials used in compressors for refrigeration and air conditioners are also the above standards Selected by the heat-resistant species. However, since organic insulating materials for refrigeration and air-conditioning equipment are used in a special environment in a refrigerant atmosphere, it is necessary to consider suppressing deformation / denaturation due to pressure in addition to temperature. It also contacts polar compounds such as refrigerants and refrigerating machine oils, so solvent resistance, extraction resistance, thermal / chemical / mechanical stability, refrigerant resistance (crazing (after applying stress to the film, In addition, fine bellows-like cracks that occur when immersed in the film), blisters (film bubbles caused by temperature rise of the refrigerant absorbed in the film), etc. must also be taken into consideration.
このため、高い耐熱クラス(E種120℃以上)の絶縁材料を使用する必要がある。 For this reason, it is necessary to use an insulating material of a high heat resistance class (E type 120 ° C. or higher).
圧縮機内で最も多く使用される絶縁材料は、PET(ポリエチレンテレフタレート)である。用途としては、分布巻モータの鉄心とのコイル絶縁にフィルム材が用いられ、コイルの縛り糸、モータの口出し線の被覆材に繊維状のPETが使用されている。 The insulating material most frequently used in the compressor is PET (polyethylene terephthalate). As a use, a film material is used for coil insulation with an iron core of a distributed winding motor, and a fibrous PET is used as a coil binding thread and a covering material for a lead wire of a motor.
これ以外の絶縁フィルムとしては、PPS(ポリフェニレンサルファイド)、PEN(ポリエチレンナフタレート)、PEEK(ポリエーテルエーテルケトン)、PI(ポリイミド)、PA(ポリアミド)などが挙げられる。 Other insulating films include PPS (polyphenylene sulfide), PEN (polyethylene naphthalate), PEEK (polyether ether ketone), PI (polyimide), PA (polyamide), and the like.
また、コイルの主絶縁被覆材料には、THEIC変性ポリエステル、ポリアミド、ポリアミドイミド、ポリエステルイミド、ポリエステルアミドイミド等が使用され、ポリエステルイミド−アミドイミドのダブルコートを施した二重被覆銅線が好ましく使用される。 The main insulation coating material for the coil is THEIC modified polyester, polyamide, polyamideimide, polyesterimide, polyesteramideimide, etc., and double coated copper wire with double coating of polyesterimide-amideimide is preferably used. The
上記の冷凍機油に潤滑性向上剤、酸化防止剤、酸捕捉剤、消泡剤、金属不活性剤等を添加しても全く問題はない。特に、ポリオールエステル油は、水分共存下で加水分解に起因する劣化が生じるため、酸化防止剤及び酸捕捉剤の配合は必須である。 Even if a lubricity improver, an antioxidant, an acid scavenger, an antifoaming agent, a metal deactivator, or the like is added to the above refrigerating machine oil, there is no problem. In particular, since the polyol ester oil deteriorates due to hydrolysis in the presence of moisture, the blending of an antioxidant and an acid scavenger is essential.
酸化防止剤としては、フェノール系であるDBPC(2、6−ジ−t−ブチル−p−クレゾール)が好ましい。 As the antioxidant, DBPC (2,6-di-t-butyl-p-cresol) which is a phenol type is preferable.
酸捕捉剤としては、一般に、エポキシ環を有する化合物として脂肪族のエポキシ系化合物やカルボジイミド系化合物が使用される。特に、カルボジイミド系化合物は、脂肪酸との反応性が極めて高く、脂肪酸から解離した水素イオンを捕捉することから、ポリオールエステル油の加水分解反応が抑制される効果が非常に大きい。 As the acid scavenger, an aliphatic epoxy compound or a carbodiimide compound is generally used as a compound having an epoxy ring. In particular, carbodiimide compounds are extremely reactive with fatty acids and capture hydrogen ions dissociated from fatty acids, so the effect of suppressing the hydrolysis reaction of polyol ester oil is very large.
カルボジイミド系化合物としては、ビス(2、6−イソプロピルフェニル)カルボジイミドが挙げられる。酸捕捉剤の配合量は、冷凍機油に対して0.05〜1.0重量%とすることが好ましい。 Examples of the carbodiimide compound include bis (2,6-isopropylphenyl) carbodiimide. The compounding amount of the acid scavenger is preferably 0.05 to 1.0% by weight with respect to the refrigerating machine oil.
なお、一般に、圧縮機に用いる冷媒に極圧剤を混合する場合がある。極圧剤としては、従来、トリクレジルフォスフェート、トリフェニルフォスフェート等の第三級フォスフェートが用いられている。 In general, an extreme pressure agent may be mixed with the refrigerant used in the compressor. As extreme pressure agents, tertiary phosphates such as tricresyl phosphate and triphenyl phosphate are conventionally used.
本発明の冷凍空調用圧縮機においては、上記の冷媒及び冷凍機油を用いることにより、耐摩耗性を向上することができるため、極圧剤を用いる必要がない。 In the compressor for refrigerating and air-conditioning of the present invention, since the wear resistance can be improved by using the refrigerant and the refrigerating machine oil, it is not necessary to use an extreme pressure agent.
(実施例1〜12)
(冷凍機油成分)
冷凍空調用圧縮機の高効率化には、冷媒と冷凍機油とが溶解した状態における溶解粘度(以下、単に「溶解粘度」という。)が重要な因子となる。
(Examples 1-12)
(Refrigerating machine oil component)
In order to increase the efficiency of a compressor for refrigeration and air conditioning, the dissolution viscosity (hereinafter simply referred to as “dissolution viscosity”) in a state where the refrigerant and the refrigeration oil are dissolved is an important factor.
低温において液液二層分離を起こし始める低温側臨界溶解温度が−30℃以下の冷媒と冷凍機油とを組み合わせた場合、圧縮機運転条件により冷凍機油に対して冷媒が多く溶け込むため、溶解粘度が大幅に低下する。圧縮機内の溶解粘度が低いと、圧縮部シール性が低下するのみならず、圧縮機摺動部における油膜強度が低下してしまうため、摩耗が進行し、冷凍空調装置の信頼性も低下してしまう。このため、冷凍機油成分の摺動部に対する吸着性が重要なパラメータとなる。 When a refrigerant having a low-temperature side critical solution temperature of −30 ° C. or less and refrigeration oil that begins to cause liquid-liquid two-layer separation at a low temperature is combined with the refrigeration oil depending on the compressor operating conditions, Decrease significantly. If the melt viscosity in the compressor is low, not only the sealing performance of the compression section will deteriorate, but also the oil film strength at the compressor sliding section will decrease, so wear will progress and the reliability of the refrigeration air conditioner will also decrease. End up. For this reason, the adsorptivity with respect to the sliding part of a refrigerator oil component becomes an important parameter.
摺動部は、鉄系材料で構成されている部位が多く、その表面には酸化鉄が形成されている。 The sliding portion has many parts made of an iron-based material, and iron oxide is formed on the surface thereof.
本明細書における冷凍機油の鉄系材料への吸着能力は、実質的に冷凍機油の酸化鉄への吸着能力と考える。 The adsorption capacity of the refrigerating machine oil to the iron-based material in this specification is considered to be substantially the adsorption capacity of the refrigerating machine oil to the iron oxide.
この考え方に基づいて、本実施例においては、平均粒径1μmのFe3O4(四三酸化鉄)の粉末(比表面積1.57m2/g)を用いて冷凍機油の吸着能力の評価を行った。 Based on this concept, in this example, the adsorption capacity of refrigerating machine oil was evaluated using powder (specific surface area 1.57 m 2 / g) of Fe 3 O 4 (iron trioxide) having an average particle diameter of 1 μm. went.
溶媒に希釈した冷凍機油成分の吸着前後の濃度を核磁気共鳴分析(NMR)により定量し、酸化鉄粉に吸着した量を算出した。溶媒にはヘキサンを用い、各冷凍機油成分が0.3mol−ppmとなるように調整した。20mlスクリュー管に酸化鉄粉を3g採取後、冷凍機油成分の溶液を10g入れ、超音波洗浄器において30分間分散させて48時間放置後の上澄み液の1H−NMR分析を行った。 The concentration of the refrigerating machine oil component diluted in the solvent before and after adsorption was quantified by nuclear magnetic resonance analysis (NMR), and the amount adsorbed on the iron oxide powder was calculated. Hexane was used as the solvent, and each refrigerating machine oil component was adjusted to 0.3 mol-ppm. After 3 g of iron oxide powder was collected in a 20 ml screw tube, 10 g of a solution of a refrigerator oil component was added, dispersed in an ultrasonic cleaner for 30 minutes, and allowed to stand for 48 hours for 1H-NMR analysis of the supernatant.
ここで、mol−ppmは、モル基準のppm(parts per million)である。すなわち、溶液(溶媒及び溶質の混合物)のモル数を分母とし、溶質のモル数を分子として算出した百万分率である。 Here, mol-ppm is ppm (parts per million) on a molar basis. In other words, it is a percentage calculated using the number of moles of the solution (mixture of solvent and solute) as the denominator and the number of moles of the solute as the numerator.
冷凍機油成分として用いた基油は、下記の通りである。ここで、40℃動粘度は、40℃における動粘度を意味する。 The base oil used as the refrigerating machine oil component is as follows. Here, 40 degreeC kinematic viscosity means kinematic viscosity in 40 degreeC.
(A)ヒンダードタイプポリオールエステル油(POE)(ペンタエリスリトール系の2−メチルヘキサン酸/2−エチルヘキサン酸の混合脂肪酸エステル油):40℃動粘度31.8mm2/s
(B)ヒンダードタイプポリオールエステル油(POE)(ネオペンチルグリコール/ペンタエリスリトール系の2−エチルヘキサン酸/3、5、5−トリメチルヘキサン酸の混合脂肪酸エステル油):40℃動粘度46.9mm2/s
(C)ヒンダードタイプポリオールエステル油(POE)(ネオペンチルグリコール/ペンタエリスリトール系の2−エチルヘキサン酸/3、5、5−トリメチルヘキサン酸の混合脂肪酸エステル油):40℃動粘度64.8mm2/s
(D)ヒンダードタイプポリオールエステル油(POE)(ペンタエリスリトール系の2−エチルヘキサン酸/3、5、5−トリメチルヘキサン酸の混合脂肪酸エステル油):40℃動粘度91.3mm2/s
(E)ヒンダードタイプポリオールエステル油(POE)(ジペンタエリスリトール系の2−エチルヘキサン酸/3、5、5−トリメチルヘキサン酸の混合脂肪酸エステル油):40℃動粘度190mm2/s
(F)ヒンダードタイプポリオールエステル油(POE)(ジペンタエリスリトール系の2−エチルヘキサン酸/3、5、5−トリメチルヘキサン酸の混合脂肪酸エステル油):40℃動粘度217mm2/s
(G)ヒンダードタイプポリオールエステル油(POE)(ジペンタエリスリトール系の3、5、5−トリメチルヘキサン酸エステル油):40℃動粘度417mm2/s
(H)ポリビニルエーテル油(PVE):40℃動粘度50.1mm2/s
(I)ポリビニルエーテル油(PVE):40℃動粘度65mm2/s
(J)ポリアルキレングリコール油(PAG)(ポリプロピレングリコールジメチルエーテル):40℃動粘度112mm2/s
(K)ナフテン系鉱油:40℃動粘度54.1mm2/s
(L)ポリαオレフィン油:40℃動粘度61.8mm2/s
酸化鉄粉に対する化合物の吸着量を測定した結果を表1に示す。
(A) Hindered type polyol ester oil (POE) (pentaerythritol-based mixed fatty acid ester oil of 2-methylhexanoic acid / 2-ethylhexanoic acid): 40 ° C. kinematic viscosity 31.8 mm 2 / s
(B) Hindered type polyol ester oil (POE) (neopentyl glycol / pentaerythritol-based 2-ethylhexanoic acid / 3,5,5-trimethylhexanoic acid mixed fatty acid ester oil): 40 ° C. kinematic viscosity 46.9 mm 2 / s
(C) Hindered type polyol ester oil (POE) (neopentyl glycol / pentaerythritol-based 2-ethylhexanoic acid / 3,5,5-trimethylhexanoic acid mixed fatty acid ester oil): 40 ° C. kinematic viscosity 64.8 mm 2 / s
(D) Hindered-type polyol ester oil (POE) (pentaerythritol-based 2-ethylhexanoic acid / 3, 5,5-trimethylhexanoic acid mixed fatty acid ester oil): 40 ° C. kinematic viscosity 91.3 mm 2 / s
(E) Hindered type polyol ester oil (POE) (dipentaerythritol-based 2-ethylhexanoic acid / 3, 5,5-trimethylhexanoic acid mixed fatty acid ester oil): 40 ° C. kinematic viscosity 190 mm 2 / s
(F) Hindered type polyol ester oil (POE) (dipentaerythritol-based 2-ethylhexanoic acid / 3, 5,5-trimethylhexanoic acid mixed fatty acid ester oil): 40 ° C. kinematic viscosity 217 mm 2 / s
(G) Hindered type polyol ester oil (POE) (dipentaerythritol-based 3,5,5-trimethylhexanoic acid ester oil): 40 ° C. kinematic viscosity 417 mm 2 / s
(H) Polyvinyl ether oil (PVE): 40 ° C. kinematic viscosity 50.1 mm 2 / s
(I) Polyvinyl ether oil (PVE): 40 ° C. kinematic viscosity 65 mm 2 / s
(J) Polyalkylene glycol oil (PAG) (polypropylene glycol dimethyl ether): 40 ° C. kinematic viscosity 112 mm 2 / s
(K) Naphthenic mineral oil: 40 ° C kinematic viscosity 54.1 mm 2 / s
(L) Poly α-olefin oil: 40 ° C. kinematic viscosity 61.8 mm 2 / s
Table 1 shows the results of measuring the amount of the compound adsorbed on the iron oxide powder.
各化合物により酸化鉄粉に対する吸着量(吸着能力)が異なっており、有極性化合物の方が鉄系材料に吸着し易いことがわかる。 The adsorption amount (adsorption ability) with respect to the iron oxide powder differs depending on each compound, and it is understood that the polar compound is more easily adsorbed to the iron-based material.
有極性化合物においても、分子構造中にエステル基が多く存在する化合物(E)、(F)及び(G)が特に吸着量が多いことがわかる。すなわち、(E)、(F)及び(G)は、鉄系材料(酸化鉄)に対する吸着能力が他の冷凍機油成分(A)〜(D)及び(H)〜(L)に比べて2.0倍以上高いことがわかる。 It can be seen that even in polar compounds, compounds (E), (F) and (G) having a large number of ester groups in the molecular structure have a particularly large amount of adsorption. That is, (E), (F), and (G) have an adsorption capacity for iron-based materials (iron oxide) that is 2 compared to other refrigeration oil components (A) to (D) and (H) to (L). It can be seen that it is more than 0 times higher.
このことから、冷凍機油成分(E)、(F)及び(G)は、圧縮機摺動部において膜を形成しやすいことが考えられる。 From this, it is considered that the refrigerating machine oil components (E), (F), and (G) are likely to form a film in the compressor sliding portion.
これは、次の理由によると考えられる。 This is considered to be due to the following reason.
エステル基に含まれるカルボニル(C=O)の酸素は、負に帯電する傾向がある。これに対して、酸化鉄の表面は、一般に、水和され、水酸基を有する構造となっている。このため、酸化鉄の表面の水酸基に含まれる水素とエステル基に含まれる酸素との間にクーロン力による引力が生じ、吸着しやすくなると考えられる。 The oxygen of carbonyl (C = O) contained in the ester group tends to be negatively charged. On the other hand, the surface of iron oxide is generally hydrated and has a structure having a hydroxyl group. For this reason, it is thought that the attractive force by a Coulomb force arises between the hydrogen contained in the hydroxyl group of the surface of iron oxide, and the oxygen contained in the ester group, and it becomes easy to adsorb | suck.
この結果から、(E)、(F)及び(G)を本発明における添加ポリオールエステル油として用いることとした。 From these results, (E), (F) and (G) were used as the added polyol ester oil in the present invention.
(実施例13〜25)
冷凍空調用圧縮機には、冷媒と冷凍機油とが封入される。
(Examples 13 to 25)
A refrigerant and refrigerating machine oil are enclosed in the compressor for refrigerating and air conditioning.
冷媒と冷凍機油との相溶性は、冷凍サイクルから圧縮機への油戻り(圧縮機内部の油量を確保)あるいは熱交換効率の低下等、圧縮機の信頼性を保証する面で重要な特性の一つである。しかし、冷媒が存在するため、冷凍機油に対する冷媒の溶け込み量によって混合液の溶解粘度は大幅に変化し、溶け込み量が多いと、油の粘度低下が著しくなり、摺動部では十分な油膜強度が得られず、さらに、圧縮部のシール材としての機能が損なわれてしまう。 The compatibility between the refrigerant and the refrigeration oil is an important characteristic for ensuring the reliability of the compressor, such as returning the oil from the refrigeration cycle to the compressor (securing the amount of oil inside the compressor) or reducing the heat exchange efficiency. one of. However, since there is a refrigerant, the melt viscosity of the mixed solution varies greatly depending on the amount of refrigerant in the refrigerating machine oil, and when the amount of penetration is large, the viscosity of the oil decreases significantly, and the sliding part has sufficient oil film strength. In addition, the function of the compression part as a sealing material is impaired.
冷媒と冷凍機油との相溶性の評価は、JIS K 2211に準じて測定した。 The evaluation of the compatibility between the refrigerant and the refrigerating machine oil was measured according to JIS K 2211.
耐圧ガラス容器に任意の油濃度において冷媒を封入し、温度を変化させて内容物の観察を行った。このとき、内容物が白濁していれば二層分離、透明であれば溶解と判定した。この二層に分離する温度の油濃度依存性は、一般に、極大値を有する曲線となる。この極大値を低温側臨界溶解温度とした。低温側臨界溶解温度は、冷媒と冷凍機油との相溶性の度合いを示すパラメータである。 A refrigerant was sealed in a pressure-resistant glass container at an arbitrary oil concentration, and the contents were observed by changing the temperature. At this time, if the contents were cloudy, it was determined that the two layers were separated, and if the contents were transparent, it was determined to be dissolved. The oil concentration dependency of the temperature at which the two layers are separated is generally a curve having a maximum value. This maximum value was taken as the low temperature side critical dissolution temperature. The low temperature side critical dissolution temperature is a parameter indicating the degree of compatibility between the refrigerant and the refrigerating machine oil.
各冷媒と相溶する冷凍機油を選定し、低温側臨界溶解温度を測定した結果を表2に示す。 Table 2 shows the results of selecting the refrigerating machine oil compatible with each refrigerant and measuring the low temperature side critical dissolution temperature.
冷媒と冷凍機油との相溶性の度合いにより、低温側臨界溶解温度が大きく異なっている。特に、冷媒としてHFO1234yf、プロパン、プロピレン又はフルオロエタンを用いた場合、冷凍機油に対する溶解性が非常に高く、圧縮機の運転条件において大幅な粘度低下を引き起こす。通常、冷凍機油の粘度グレードを上げて対応するが、冷凍空調用圧縮機の運転条件では、温度及び圧力により冷媒溶解量が大きくなり、実際には粘度があまり増加しない。 Depending on the degree of compatibility between the refrigerant and the refrigerating machine oil, the low temperature side critical dissolution temperature varies greatly. In particular, when HFO1234yf, propane, propylene, or fluoroethane is used as the refrigerant, the solubility in refrigerating machine oil is very high, causing a significant decrease in viscosity under compressor operating conditions. Usually, the viscosity grade of refrigerating machine oil is raised, but under the operating conditions of the compressor for refrigerating and air conditioning, the amount of dissolved refrigerant increases with temperature and pressure, and the viscosity does not increase much in practice.
(実施例26〜31、比較例1〜6)
シェル式四球摩擦摩耗試験機を用い、冷凍機油の潤滑性を評価した。
(Examples 26-31, Comparative Examples 1-6)
The lubricity of refrigeration oil was evaluated using a shell-type four-ball frictional wear tester.
1/2インチSUJ2鋼球を試験片とし、荷重:280N、温度:120℃、回転速度:1200/min、時間:10minで試験した後の固定試験片の摩耗痕径(3個平均)及び摩擦係数を測定した。 Wear mark diameter (average of 3 pieces) and friction of a fixed test piece after being tested with a 1/2 inch SUJ2 steel ball as a test piece, load: 280 N, temperature: 120 ° C., rotation speed: 1200 / min, time: 10 min The coefficient was measured.
冷凍機油主剤としては、ポリオールエステル油(A)〜(D)、ポリビニルエーテル油(I)及びナフテン系鉱油(K)を用い、そこに添加ポリオールエステル油(F)を5.0wt%配合したものを評価した。 As the refrigerating machine oil main component, polyol ester oils (A) to (D), polyvinyl ether oil (I), and naphthenic mineral oil (K) are used, and added polyol ester oil (F) is blended at 5.0 wt%. Evaluated.
比較例としては、ポリオールエステル油(A)〜(D)をそれぞれ単独の場合、ポリビニルエーテル油(I)単独の場合及びナフテン系鉱油(K)単独の場合について評価した。 As comparative examples, the case of each of the polyol ester oils (A) to (D), the case of the polyvinyl ether oil (I) alone and the case of the naphthenic mineral oil (K) alone were evaluated.
各冷凍機油の潤滑性を評価した結果を表3に示す。 Table 3 shows the results of evaluating the lubricity of each refrigeration oil.
この結果から、添加ポリオールエステル油(F)を配合していない比較例1〜4の冷凍機油は、摩耗痕径が大きく、摩擦係数が高い。比較例5及び6の場合、試験開始直後に焼付きを発生したため試験を中断した。 From this result, the refrigerating machine oils of Comparative Examples 1 to 4 in which the added polyol ester oil (F) is not blended have a large wear scar diameter and a high friction coefficient. In the case of Comparative Examples 5 and 6, since the seizure occurred immediately after the start of the test, the test was interrupted.
これに対して、実施例26〜31で示す添加ポリオールエステル油(F)を配合した冷凍機油は、冷凍機油主剤の油種に関係なく、摩耗痕径及び摩擦係数が抑制されており、潤滑性の向上効果が得られた。これは、添加ポリオールエステル油(F)の鉄系材料に対する吸着能力が冷凍機油主剤よりも大きいことから、摩擦面が低表面エネルギー化され、耐摩耗性と摩擦係数の低減効果が得られたことによる。冷凍機油主剤がポリビニルエーテル油(I)及びナフテン系鉱油(K)においても焼付きを発生することはなかった。特に、冷凍機油主剤が表1で示したように添加ポリオールエステル油(F)と比べて吸着量が少ないポリビニルエーテル油(I)やナフテン系鉱油(K)である場合、添加ポリオールエステル油(F)が摩擦面に吸着しやすくなるため、潤滑性向上の効果が得られやすい。 On the other hand, the refrigerating machine oil blended with the added polyol ester oil (F) shown in Examples 26 to 31 has a reduced wear scar diameter and a coefficient of friction regardless of the oil type of the refrigerating machine oil main component, and has a lubricating property. The improvement effect was obtained. This is because the adsorption capacity of the added polyol ester oil (F) to the iron-based material is greater than that of the main component of the refrigeration oil, so that the friction surface is reduced in surface energy, and the effect of reducing wear resistance and friction coefficient is obtained. by. The refrigerator oil main component did not cause seizure even in the polyvinyl ether oil (I) and the naphthenic mineral oil (K). In particular, as shown in Table 1, when the main component of the refrigerating machine oil is a polyvinyl ether oil (I) or a naphthenic mineral oil (K) having a smaller adsorption amount than the added polyol ester oil (F), the added polyol ester oil (F ) Tends to be adsorbed on the friction surface, and the effect of improving lubricity is easily obtained.
(実施例32〜37、比較例7〜8)
添加ポリオールエステル油(E)及び(G)の効果を確認するため、シェル式四球摩擦摩耗試験機を用いて、添加ポリオールエステル油の種類及び添加量を変えて実施例26と同様な試験を実施した。
(Examples 32-37, Comparative Examples 7-8)
In order to confirm the effects of the added polyol ester oils (E) and (G), the same test as in Example 26 was performed using a shell-type four-ball frictional wear tester and changing the type and added amount of the added polyol ester oil. did.
各冷凍機油の潤滑性を評価した結果を表4に示す。 Table 4 shows the results of evaluating the lubricity of each refrigeration oil.
本表に示す実施例32〜37の冷凍機油は、冷凍機油主剤として(C)を用い、添加剤を加えない比較例3(表3に示す。)の冷凍機油と比べて摩耗痕径及び摩擦係数が抑制されており、潤滑性の向上効果が確認できた。 The refrigerating machine oils of Examples 32 to 37 shown in this table use (C) as a refrigerating machine oil main component, and wear scar diameter and friction as compared with the refrigerating machine oil of Comparative Example 3 (shown in Table 3) to which no additive is added. The coefficient was suppressed, and the improvement effect of lubricity could be confirmed.
また、添加ポリオールエステル油(F)の添加量が少ない比較例7及び8の場合では、摩耗痕径が大きく、摩擦係数が高くなり、潤滑性の向上効果が発現しにくい。これに対して、実施例32〜35で示す添加ポリオールエステル油(F)を冷凍機油主剤に対して1.0重量%以上配合した冷凍機油は、摩耗痕径及び摩擦係数が抑制されており、潤滑性の向上効果が得られた。 In Comparative Examples 7 and 8, in which the added amount of the added polyol ester oil (F) is small, the wear scar diameter is large, the friction coefficient is high, and the effect of improving the lubricity is hardly exhibited. On the other hand, the refrigerating machine oil in which the additive polyol ester oil (F) shown in Examples 32-35 is blended in an amount of 1.0% by weight or more with respect to the refrigerating machine main agent has a reduced wear scar diameter and a friction coefficient. The effect of improving lubricity was obtained.
(実施例38、39、比較例9、10)
図1は、本実施例で用いた冷暖房兼用のルームエアコンの概略を示したものである。
(Examples 38 and 39, Comparative Examples 9 and 10)
FIG. 1 shows an outline of a room air conditioner that is also used in the present embodiment.
室内を冷房する場合、圧縮機1の吐出パイプより断熱的に圧縮された高温高圧の冷媒ガス(封入冷媒)は、四方弁2を通って室外熱交換器3(凝縮手段として使用される)で冷却され、高圧の液冷媒となる。この冷媒は、膨張手段4(例えば、キャピラリーチューブや温度式膨張弁などである。減圧部とも呼ぶ。)で膨張され、僅かにガスを含む低温低圧液となって室内熱交換器5(蒸発手段として使用される。)に至り、室内の空気から熱を得て低温ガスの状態で再び四方弁2を通って圧縮機1に至る。室内を暖房する場合は、四方弁2によって冷媒の流れが逆方向に変えられ、逆作用となる。 When the room is cooled, the high-temperature and high-pressure refrigerant gas (encapsulated refrigerant) compressed adiabatically from the discharge pipe of the compressor 1 passes through the four-way valve 2 in the outdoor heat exchanger 3 (used as a condensing means). It is cooled and becomes a high-pressure liquid refrigerant. This refrigerant is expanded by expansion means 4 (for example, a capillary tube or a temperature type expansion valve, which is also referred to as a decompression section), and becomes a low-temperature and low-pressure liquid containing a slight amount of gas to form an indoor heat exchanger 5 (evaporation means). To obtain the heat from the indoor air and reach the compressor 1 again through the four-way valve 2 in the state of low-temperature gas. When the room is heated, the flow of the refrigerant is changed in the reverse direction by the four-way valve 2, and the reverse action occurs.
本実施例においては、圧縮機としてスクロール式圧縮機を用いた。 In this embodiment, a scroll compressor is used as the compressor.
図2は、その概略構造を示したものである。 FIG. 2 shows the schematic structure.
圧縮機は、固定スクロール部材6の端板7に直立する渦巻状のラップ8と、この固定スクロール部材6と実質的に同一形状のラップ10を有する旋回スクロール部材9とをお互いにラップ8とラップ10とを向い合わせにして噛み合わせて圧縮機構部を形成し、旋回スクロール部材9をクランクシャフト11によって旋回運動させる。固定スクロール部材6及び旋回スクロール部材9によって形成される圧縮室12a、12bのうち、最も外側に位置している圧縮室は、旋回運動にともなって容積が次第に縮小しながら、固定スクロール部材6と旋回スクロール部材9とで構成された中心部に向かって移動していく。圧縮室12a、12bが固定スクロール部材6と旋回スクロール部材9とで構成された中心部近傍に達したとき、圧縮室12a、12bが吐出口13と連通し、圧縮室12a、12bの内部の圧縮ガスが吐出パイプ16から圧縮機外に吐出される。
The compressor wraps a
本実施例の圧縮機においては、圧力容器15内に電動モータ17が内蔵されており、圧縮機は、一定速あるいは図示していないインバータによって制御された電圧に応じた回転速度でクランクシャフト11が回転し、圧縮動作を行う。また、モータ17の下方には油溜め部20が設けられており、油溜め部20の油は、圧力差によってクランクシャフト11に設けられた油孔19を通り、旋回スクロール部材9とクランクシャフト11との摺動部、滑り軸受け18等の潤滑に供される。
In the compressor of the present embodiment, an
実施例38、39、比較例9、10においては、図1に示すルームエアコンを用いて、室内機を恒温室(35℃、湿度75%)に設置して2160時間運転する実機試験を行った。 In Examples 38 and 39 and Comparative Examples 9 and 10, an actual machine test was performed in which the indoor unit was installed in a temperature-controlled room (35 ° C., humidity 75%) and operated for 2160 hours using the room air conditioner shown in FIG. .
モータ17の鉄心とのコイル絶縁には、耐熱PETフィルム(B種130℃)を用い、コイル主絶縁には、ポリエステルイミド−アミドイミドのダブルコートを施した二重被覆銅線を用いた。
A heat-resistant PET film (Type B 130 ° C.) was used for coil insulation with the iron core of the
ルームエアコンの評価には、スクロール式圧縮機の摩耗状態に着眼し、試験前後でのフレーム14〜クランクシャフト11間(フレーム14とクランクシャフト11との間)の摩耗による隙間増加量を測定した。フレーム14〜クランクシャフト11間(以下、フレーム〜シャフト間ともいう。)の隙間増加量が増えるほど摩耗量が大きいことを示しており、一般に、隙間増加量が増えるに伴って振動や騒音が大きくなる。
For the evaluation of the room air conditioner, the amount of increase in the gap due to wear between the
HFO1234yf(2、3、3、3−テトラフルオロプロペン)を単独で冷媒として用いた。HFO1234yfは、低圧冷媒であり、冷媒循環量が少ないため配管内での圧損が大きくなる。このため、圧縮機押除量を通常の2倍とし、接続配管の広径化、熱交換器のパス数増加と分配バランスの調整を行った仕様で評価した。 HFO1234yf (2, 3, 3, 3-tetrafluoropropene) was used alone as a refrigerant. HFO1234yf is a low-pressure refrigerant, and since the refrigerant circulation amount is small, the pressure loss in the pipe increases. For this reason, the amount of pushing away from the compressor was doubled as usual, and the evaluation was made with the specifications in which the diameter of the connecting pipe was increased, the number of heat exchanger paths was increased, and the distribution balance was adjusted.
HFO1234yf及びHFO1234ze並びにこれらを含む混合冷媒を用いた冷凍空調サイクルにおいては、冷媒と冷凍機油との相溶性が圧縮機への油戻り量を確保するための重要な特性となる。冷凍空調サイクルでは、冷媒と同様に冷凍機油も循環することが必要である。相溶性が劣ると、圧縮機から機械的要素により吐出された冷凍機油が循環せず、特に低温部で分離した油が滞留するため、圧縮機の油量が少なくなり、摺動部の潤滑油支障をきたす。このため、サイクル中での運転条件温度範囲で冷媒と冷凍機油とが溶解していることが好ましい。 In the refrigerating and air-conditioning cycle using HFO1234yf and HFO1234ze and a mixed refrigerant containing these, the compatibility between the refrigerant and the refrigerating machine oil is an important characteristic for ensuring the amount of oil return to the compressor. In the refrigerating and air-conditioning cycle, it is necessary to circulate refrigerating machine oil as well as refrigerant. If the compatibility is inferior, the refrigerating machine oil discharged by the mechanical elements from the compressor will not circulate, and the oil separated especially at the low temperature part will stay, so the amount of oil in the compressor will decrease, and the lubricating oil in the sliding part It will cause trouble. For this reason, it is preferable that the refrigerant and the refrigerating machine oil are dissolved in the operating condition temperature range in the cycle.
HFO1234yfに対して、ナフテン系鉱油、パラフィン系鉱油、アルキルベンゼン油、ポリαオレフィン油などの炭化水素油は相溶しにくいため、ポリオールエステル油又はポリビニルエーテル油が好ましい。 Since hydrocarbon oils such as naphthenic mineral oil, paraffinic mineral oil, alkylbenzene oil, and poly-α-olefin oil are less compatible with HFO1234yf, polyol ester oil or polyvinyl ether oil is preferable.
実施例38においては、HFO1234yfと相溶性を有する実施例28で採用した冷凍機油((C)+(F))を用いて評価を行った。また、実施例39においては、実施例30で採用した冷凍機油((I)+(F))を用いて評価を行った。 In Example 38, evaluation was performed using the refrigerating machine oil ((C) + (F)) employed in Example 28 having compatibility with HFO1234yf. In Example 39, evaluation was performed using the refrigerating machine oil ((I) + (F)) employed in Example 30.
冷凍機油主剤として(C)または(I)を用い、これらに対して吸着能力が高い(F)を5重量%配合して、40℃における動粘度を68.6mm2/sまたは68.9mm2/sとした冷凍機油で試験を実施した。 (C) or (I) is used as the refrigerating machine oil main component, and 5% by weight of (F) having a high adsorption capacity is blended with them, and the kinematic viscosity at 40 ° C. is 68.6 mm 2 / s or 68.9 mm 2 The test was carried out with a refrigerating machine oil of / s.
比較例9及び10においては、実施例38及び39で添加ポリオールエステル油が配合されていない冷凍機油主剤のみで実施した。 In Comparative Examples 9 and 10, it was carried out only with the refrigerating machine oil main agent in which the added polyol ester oil was not blended in Examples 38 and 39.
本試験の目標値は、試験後のフレーム〜シャフト間の摩耗による隙間増加量が10μm以下である。 The target value of this test is that the amount of increase in the gap due to wear between the frame and the shaft after the test is 10 μm or less.
実施例38、39及び比較例9、10の結果を表5に示す。 The results of Examples 38 and 39 and Comparative Examples 9 and 10 are shown in Table 5.
表5から明らかなように、実施例38及び39のルームエアコンは、比較例9及び10と比べて、フレーム〜シャフト間の隙間増加量が大幅に低減でき、摩耗を抑制することから、ルームエアコンにおいて高い信頼性が得られる。 As is apparent from Table 5, the room air conditioners of Examples 38 and 39 can greatly reduce the amount of increase in the gap between the frame and the shaft, and suppress wear, compared with Comparative Examples 9 and 10. High reliability can be obtained.
また、表5には、冷媒と冷凍機油との組み合わせに関して、冷房中間条件における粘度及び効率の測定結果も示してある。 Table 5 also shows the measurement results of the viscosity and efficiency in the cooling intermediate condition regarding the combination of the refrigerant and the refrigerating machine oil.
粘度の測定は、ジャパンコントロール社のピストン式粘度計を用いた。 The viscosity was measured using a piston viscometer manufactured by Japan Control.
また、効率は、成績係数(COP:Coefficient of Performance)を用いて、比較例9を基準(100)として比率で表記した。 The efficiency was expressed as a ratio using the coefficient of performance (COP) as a reference (100) with Comparative Example 9 as the reference.
この結果より、比較例9及び10においては、粘度の低下が発生しており、圧縮部において十分なシール性が得られない。これに対して、実施例38及び39においては、粘度が増加している。 From this result, in Comparative Examples 9 and 10, a decrease in viscosity occurs, and a sufficient sealing performance cannot be obtained in the compressed portion. On the other hand, in Examples 38 and 39, the viscosity is increased.
さらに、表3の実施例28及び30で示したように、添加ポリオールエステル油による摩擦抑制効果が発現したため、比較例9(基準1)と比べて成績係数が向上した。 Furthermore, as shown in Examples 28 and 30 of Table 3, the coefficient of performance was improved as compared with Comparative Example 9 (Criteria 1) because the friction suppressing effect of the added polyol ester oil was exhibited.
以上の実施例の結果から、圧縮機の摩耗を抑制し、長期絶縁信頼性が十分に確保できる冷凍空調装置が得られることがわかった。 From the results of the above examples, it was found that a refrigeration air conditioner capable of suppressing compressor wear and sufficiently ensuring long-term insulation reliability can be obtained.
また、図示はしていないが、冷媒にHFO1234yf及びHFC32(20重量%及び40重量%)の混合冷媒と実施例28で採用した冷凍機油((C)+(F))との組み合わせにおいて同様な実機試験で評価を行ったが、実施例38及び39とほぼ同様な結果が得られ、混合冷媒を用いても効果が得られ、問題がないことを確認した。 Although not shown, the same applies to the combination of the refrigerant mixture of HFO1234yf and HFC32 (20 wt% and 40 wt%) and the refrigerating machine oil ((C) + (F)) employed in Example 28. Although evaluation was performed in an actual machine test, almost the same results as in Examples 38 and 39 were obtained, and it was confirmed that even if a mixed refrigerant was used, the effect was obtained and there was no problem.
(実施例40〜42、比較例11〜13)
実施例40〜42においては、冷媒にプロパン及びR410Aと用い、それぞれの冷媒に合う冷凍サイクルを組んで実施例38と同様な実機試験で評価を行った。
(Examples 40 to 42, Comparative Examples 11 to 13)
In Examples 40 to 42, propane and R410A were used as refrigerants, and refrigeration cycles suitable for the respective refrigerants were assembled, and evaluation was performed in the same actual machine test as in Example 38.
実施例40においては、冷媒としてプロパンを、冷凍機油主剤として(C)を、添加ポリオールエステル油として(F)を5.0重量%配合した冷凍機油をそれぞれ用いた。 In Example 40, propane was used as the refrigerant, (C) as the refrigerating machine main agent, and refrigerating machine oil blended with 5.0 wt% of (F) as the added polyol ester oil.
実施例41においては、冷媒としてプロパンを、冷凍機油主剤として(K)を、添加ポリオールエステル油として(F)を5.0重量%配合した冷凍機油をそれぞれ用いた。 In Example 41, propane was used as the refrigerant, (K) as the refrigerating machine main agent, and refrigerating machine oil blended with 5.0 wt% of (F) as the added polyol ester oil.
実施例42においては、冷媒としてR410Aを、冷凍機油主剤として(C)を、添加ポリオールエステル油として(F)を5.0重量%配合した冷凍機油をそれぞれ用いた。 In Example 42, R410A was used as the refrigerant, (C) as the refrigerating machine main agent, and refrigerating machine oil blended with 5.0 wt% of (F) as the added polyol ester oil.
比較例40〜42においては、添加ポリオールエステル油が配合されていない冷凍機油をそれぞれ評価した。 In Comparative Examples 40 to 42, refrigerating machine oils not containing any added polyol ester oil were evaluated.
評価結果は、表5に示す。 The evaluation results are shown in Table 5.
プロパンは、表2の相溶性の評価結果で示すように、ポリオールエステル油、鉱油などと溶解性が高いため、圧縮機内で大幅な粘度低下を起こす。さらに、分子構造中にハロゲン元素を含まないため、摩擦が生じる部位における潤滑性に寄与するハロゲン化鉄を生成しないため、比較例11及び12で示すように、フレーム〜シャフト間の摩耗による隙間増加量が大幅に増加してしまう。 As shown in the compatibility evaluation results in Table 2, propane is highly soluble in polyol ester oils, mineral oils, and the like, and causes a significant viscosity reduction in the compressor. Further, since no halogen element is contained in the molecular structure, iron halide that contributes to lubricity in a site where friction occurs is not generated, and therefore, as shown in Comparative Examples 11 and 12, an increase in the gap due to wear between the frame and the shaft. The amount will increase significantly.
これに対して、実施例40及び41で示すように、冷凍機油主剤に添加ポリオールエステル油(F)を配合した組み合わせについては、フレーム〜シャフト間の摩耗による隙間増加量が大幅に低減され、摩擦を緩和したことにより、比較例11(基準2)と比べて成績係数が向上した。 On the other hand, as shown in Examples 40 and 41, with respect to the combination in which the additive polyol ester oil (F) is blended with the refrigerating machine main agent, the increase in gap due to wear between the frame and the shaft is greatly reduced, and the friction As a result, the coefficient of performance was improved as compared with Comparative Example 11 (Criteria 2).
また、冷媒にR410Aを用いた実施例42においては、比較例13(基準3)と比べてフレーム〜シャフト間の摩耗による隙間増加量が抑制され、成績係数も向上した。 Further, in Example 42 using R410A as the refrigerant, an increase in gap due to wear between the frame and the shaft was suppressed and the coefficient of performance was improved as compared with Comparative Example 13 (Reference 3).
このことから、冷媒の種類によらず、ジフルオロメタン、フルオロエタン、プロピレンなどの冷媒でも同様な効果が得られる。 For this reason, the same effect can be obtained with refrigerants such as difluoromethane, fluoroethane, and propylene, regardless of the type of refrigerant.
このほか、ロータリー式圧縮機、ツインロータリー式圧縮機、2段圧縮ロータリー式圧縮機、及びローラ及びベーンが一体化されたスイング式圧縮機においても同様の効果が得られる。 In addition, the same effect can be obtained in a rotary compressor, a twin rotary compressor, a two-stage compression rotary compressor, and a swing compressor in which rollers and vanes are integrated.
本発明は、冷凍空調装置用冷媒圧縮機及び冷凍空調装置に適用可能である。 The present invention is applicable to a refrigerant compressor for a refrigeration air conditioner and a refrigeration air conditioner.
1:圧縮機、2:四方弁、3:室外熱交換器、4:膨張手段、5:室内熱交換器、6:固定スクロール部材、7:端板、8:ラップ、9:旋回スクロール部材、10:ラップ、11:クランクシャフト、12a、12b:圧縮室、13:吐出口、14:フレーム、15:圧力容器、16:吐出パイプ、17:電動モータ、18:滑り軸受け、19:油孔、20:油溜め部。 1: compressor, 2: four-way valve, 3: outdoor heat exchanger, 4: expansion means, 5: indoor heat exchanger, 6: fixed scroll member, 7: end plate, 8: wrap, 9: orbiting scroll member, 10: lap, 11: crankshaft, 12a, 12b: compression chamber, 13: discharge port, 14: frame, 15: pressure vessel, 16: discharge pipe, 17: electric motor, 18: sliding bearing, 19: oil hole, 20: Oil sump part.
Claims (8)
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2010169889A JP2012031239A (en) | 2010-07-29 | 2010-07-29 | Compressor for refrigeration and air-conditioning, and refrigeration and air-conditioning apparatus |
| KR1020110075007A KR101280701B1 (en) | 2010-07-29 | 2011-07-28 | Compressor for refrigerating air conditioning and refrigerating air conditioner |
| US13/193,655 US20120024007A1 (en) | 2010-07-29 | 2011-07-29 | Compressor for refrigeration and air-conditioning and refrigerating and air-conditioning apparatus |
| CN2011102140224A CN102408936A (en) | 2010-07-29 | 2011-07-29 | Compressor for refrigerating and air-conditioning, and refrigerating and air-conditioning device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2010169889A JP2012031239A (en) | 2010-07-29 | 2010-07-29 | Compressor for refrigeration and air-conditioning, and refrigeration and air-conditioning apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2012031239A true JP2012031239A (en) | 2012-02-16 |
Family
ID=45525342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2010169889A Withdrawn JP2012031239A (en) | 2010-07-29 | 2010-07-29 | Compressor for refrigeration and air-conditioning, and refrigeration and air-conditioning apparatus |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20120024007A1 (en) |
| JP (1) | JP2012031239A (en) |
| KR (1) | KR101280701B1 (en) |
| CN (1) | CN102408936A (en) |
Cited By (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013125528A1 (en) * | 2012-02-22 | 2013-08-29 | Jx日鉱日石エネルギー株式会社 | Refrigerator oil composition, method for producing same, and working fluid composition for refrigerators |
| WO2013147045A1 (en) * | 2012-03-29 | 2013-10-03 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerator |
| WO2013187084A1 (en) * | 2012-06-15 | 2013-12-19 | 日立アプライアンス株式会社 | Compressor and air conditioner |
| WO2014010693A1 (en) * | 2012-07-13 | 2014-01-16 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerating machine |
| WO2014156737A1 (en) * | 2013-03-25 | 2014-10-02 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerator |
| JP2015017730A (en) * | 2013-07-10 | 2015-01-29 | 日立アプライアンス株式会社 | Air conditioner |
| JP2015117923A (en) * | 2013-12-20 | 2015-06-25 | 日立アプライアンス株式会社 | Air conditioner |
| JP2015140994A (en) * | 2014-01-30 | 2015-08-03 | 日立アプライアンス株式会社 | Air conditioner, and refrigerator oil |
| JP2016000837A (en) * | 2015-10-07 | 2016-01-07 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerator |
| US9365484B2 (en) | 2012-10-24 | 2016-06-14 | Kh Neochem Co., Ltd. | Hexaester of mono-formal bis pentaerythritol |
| JP2016164274A (en) * | 2016-05-12 | 2016-09-08 | Jxエネルギー株式会社 | Actuation fluid composition for refrigerator |
| WO2016158306A1 (en) * | 2015-03-30 | 2016-10-06 | 出光興産株式会社 | Refrigerator lubricating oil and mixed composition for refrigerator |
| US9546334B2 (en) | 2013-07-31 | 2017-01-17 | Kh Neochem Co., Ltd. | Refrigerating machine oil, and working fluid composition for refrigerating machine which is produced using same |
| US9567284B2 (en) | 2012-10-24 | 2017-02-14 | Kh Neochem Co., Ltd. | Hexaester of mono-formal bis pentaerythritol |
| JP2017088978A (en) * | 2015-11-13 | 2017-05-25 | 日産自動車株式会社 | A sliding mechanism, a refrigerant compressor and an air conditioner using the sliding mechanism, and a method for manufacturing the sliding mechanism. |
| WO2017187828A1 (en) * | 2016-04-28 | 2017-11-02 | 東芝キヤリア株式会社 | Hermetic compressor and refrigeration cycle device |
| JPWO2017145278A1 (en) * | 2016-02-24 | 2018-10-11 | 三菱電機株式会社 | Refrigeration equipment |
| US10144855B2 (en) | 2012-03-27 | 2018-12-04 | Jxtg Nippon Oil And Energy Corporation | Working fluid composition for refrigerator |
| US10266788B2 (en) | 2014-05-30 | 2019-04-23 | Kh Neochem Co., Ltd. | Refrigerating-machine oil composition and working fluid composition including same for refrigerating machine |
| US10273394B2 (en) | 2011-10-26 | 2019-04-30 | Jx Nippon Oil & Energy Corporation | Refrigerating machine working fluid composition and refrigerant oil |
| WO2019102532A1 (en) * | 2017-11-22 | 2019-05-31 | 三菱電機株式会社 | Compressor and refrigeration cycle device |
| JP2019203138A (en) * | 2019-07-12 | 2019-11-28 | 出光興産株式会社 | Refrigerator lubricating oil and mixed composition for refrigerator |
| JPWO2018169039A1 (en) * | 2017-03-17 | 2020-01-23 | Agc株式会社 | Composition for heat cycle system and heat cycle system |
| JP2020031530A (en) * | 2018-08-20 | 2020-02-27 | ダイキン工業株式会社 | Refrigeration cycle device |
| WO2023162923A1 (en) * | 2022-02-22 | 2023-08-31 | ダイキン工業株式会社 | Refrigeration cycle device |
Families Citing this family (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009152117A1 (en) * | 2008-06-09 | 2009-12-17 | Bright Solutions International Llc | Lubricants for air donditioning systems |
| US8889031B2 (en) * | 2010-11-30 | 2014-11-18 | Jx Nippon Oil & Energy Corporation | Working fluid composition for refrigerator machine and refrigerating machine oil |
| US8685271B2 (en) * | 2012-02-08 | 2014-04-01 | Chemtura Corporation | Refrigeration oil and compositions with hydrocarbon refrigerants |
| CN104837966B (en) | 2012-12-05 | 2017-11-21 | 吉坤日矿日石能源株式会社 | Working fluid composition for refrigerating machine |
| CN103525370A (en) * | 2013-08-01 | 2014-01-22 | 广东美芝制冷设备有限公司 | Composition, compressor adopting composition and refrigeration equipment adopting composition |
| CN103486043B (en) * | 2013-08-26 | 2016-08-10 | 广东美芝制冷设备有限公司 | Compressor and there is the refrigeration plant of this compressor |
| JP6076876B2 (en) * | 2013-10-02 | 2017-02-08 | Jxエネルギー株式会社 | Refrigerator oil composition, working fluid composition for refrigerator |
| EP4063761A1 (en) * | 2015-03-30 | 2022-09-28 | Carrier Corporation | Low-oil refrigerants and vapor compression systems |
| CN106318516B (en) * | 2015-06-25 | 2019-02-01 | 北京福润联石化科技开发有限公司 | Refrigerated machine oil composition base oil and refrigerated machine oil composition and composition for refrigeration |
| US10837682B2 (en) * | 2015-12-18 | 2020-11-17 | Bry-Air [Asia] Pvt. Ltd. | Devices with hybrid vapour compression-adsorption cycle and method for implementation thereof |
| EP3460356B1 (en) * | 2016-05-17 | 2021-01-20 | Mitsubishi Electric Corporation | Refrigeration cycle device |
| CN106833536B (en) * | 2016-12-26 | 2019-08-20 | 浙江衢化氟化学有限公司 | A kind of refrigerant composition containing HF hydrocarbon |
| FR3077822B1 (en) | 2018-02-15 | 2020-07-24 | Arkema France | REPLACEMENT HEAT TRANSFER COMPOSITIONS FOR R-134A |
| FR3077773B1 (en) | 2018-02-15 | 2023-05-26 | Arkema France | PROCESS FOR HEATING AND/OR AIR CONDITIONING A VEHICLE |
| CN110428303A (en) * | 2019-07-31 | 2019-11-08 | 珠海格力电器股份有限公司 | Auxiliary model selection method, device, equipment, system and storage medium for commercial air conditioner |
| CN111423852B (en) * | 2020-03-30 | 2021-06-29 | 珠海格力电器股份有限公司 | Ternary refrigeration composition and refrigeration device comprising same |
| CN116323855B (en) * | 2020-10-08 | 2025-08-08 | 科慕埃弗西有限公司 | Refrigerant compositions for refrigerant compressor systems |
| DE102020213822B4 (en) * | 2020-10-28 | 2024-06-06 | JustAirTech GmbH | Gas refrigeration machine, method for operating a gas refrigeration machine and method for producing a gas refrigeration machine as an open system |
| JP2024506262A (en) | 2021-01-26 | 2024-02-13 | ザ ケマーズ カンパニー エフシー リミテッド ライアビリティ カンパニー | Vapor compression systems containing lubricant-refrigerant compositions |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1030095A (en) * | 1996-04-09 | 1998-02-03 | Mitsubishi Gas Chem Co Inc | Polyol ester lubricating oil |
| WO1999013824A1 (en) * | 1997-09-17 | 1999-03-25 | The Procter & Gamble Company | Hair care compositions comprising bulky optical brighteners |
| JP4564111B2 (en) * | 1998-09-02 | 2010-10-20 | Jx日鉱日石エネルギー株式会社 | Refrigeration oil |
| CA2487587C (en) * | 2003-11-21 | 2012-04-24 | Nof Corporation | A polyol ester for use within a refrigeration lubricant composition compatible with chlorine-free hydrofluorocarbon refrigerants |
| JP2009074018A (en) * | 2007-02-27 | 2009-04-09 | Nippon Oil Corp | Refrigerator oil and working fluid composition for refrigerator |
| CN101548001A (en) * | 2007-02-27 | 2009-09-30 | 新日本石油株式会社 | Refrigerating machine oil and working fluid composition for refrigerating machine |
| JP5572284B2 (en) * | 2007-02-27 | 2014-08-13 | Jx日鉱日石エネルギー株式会社 | Refrigerator oil and working fluid composition for refrigerator |
| RU2011134285A (en) * | 2009-01-16 | 2013-02-27 | Кемтура Корпорейшн | CARBON DIOXIDE WORKING FLUIDS FOR AIR COOLING AND AIR CONDITIONING |
| JP5390638B2 (en) * | 2009-01-26 | 2014-01-15 | ケムチュア コーポレイション | Manufacture of polyol ester lubricants for refrigerated systems. |
-
2010
- 2010-07-29 JP JP2010169889A patent/JP2012031239A/en not_active Withdrawn
-
2011
- 2011-07-28 KR KR1020110075007A patent/KR101280701B1/en not_active Expired - Fee Related
- 2011-07-29 CN CN2011102140224A patent/CN102408936A/en active Pending
- 2011-07-29 US US13/193,655 patent/US20120024007A1/en not_active Abandoned
Cited By (51)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10273394B2 (en) | 2011-10-26 | 2019-04-30 | Jx Nippon Oil & Energy Corporation | Refrigerating machine working fluid composition and refrigerant oil |
| JP2013170255A (en) * | 2012-02-22 | 2013-09-02 | Jx Nippon Oil & Energy Corp | Refrigerator oil composition, method for producing the same, and working fluid composition for refrigerator |
| WO2013125528A1 (en) * | 2012-02-22 | 2013-08-29 | Jx日鉱日石エネルギー株式会社 | Refrigerator oil composition, method for producing same, and working fluid composition for refrigerators |
| US9234155B2 (en) | 2012-02-22 | 2016-01-12 | Jx Nippon Oil & Energy Corporation | Refrigerator oil composition, method for producing same, and working fluid composition for refrigerators |
| US10414962B2 (en) | 2012-03-27 | 2019-09-17 | Jxtg Nippon Oil & Energy Corporation | Working fluid composition for refrigerator |
| US10144855B2 (en) | 2012-03-27 | 2018-12-04 | Jxtg Nippon Oil And Energy Corporation | Working fluid composition for refrigerator |
| WO2013147045A1 (en) * | 2012-03-29 | 2013-10-03 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerator |
| JP2013203953A (en) * | 2012-03-29 | 2013-10-07 | Jx Nippon Oil & Energy Corp | Working fluid composition for refrigerator |
| KR101879567B1 (en) * | 2012-03-29 | 2018-07-19 | 제이엑스티지 에네루기 가부시키가이샤 | Working fluid composition for refrigerator |
| CN104169405A (en) * | 2012-03-29 | 2014-11-26 | 吉坤日矿日石能源株式会社 | Working fluid composition for refrigerator |
| KR20140142265A (en) * | 2012-03-29 | 2014-12-11 | 제이엑스 닛코닛세키에너지주식회사 | Working fluid composition for refrigerator |
| CN104379713A (en) * | 2012-06-15 | 2015-02-25 | 日立空调·家用电器株式会社 | Compressor and air conditioner |
| JP2014001255A (en) * | 2012-06-15 | 2014-01-09 | Hitachi Appliances Inc | Compressor and air conditioner |
| WO2013187084A1 (en) * | 2012-06-15 | 2013-12-19 | 日立アプライアンス株式会社 | Compressor and air conditioner |
| KR20150035785A (en) * | 2012-07-13 | 2015-04-07 | 제이엑스 닛코닛세키에너지주식회사 | Working fluid composition for refrigerating machine |
| KR101957692B1 (en) * | 2012-07-13 | 2019-03-14 | 제이엑스티지 에네루기 가부시키가이샤 | Working fluid composition for refrigerating machine |
| JP2014019757A (en) * | 2012-07-13 | 2014-02-03 | Jx Nippon Oil & Energy Corp | Working fluid composition for refrigerator |
| WO2014010693A1 (en) * | 2012-07-13 | 2014-01-16 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerating machine |
| US9732263B2 (en) | 2012-07-13 | 2017-08-15 | Jx Nippon Oil & Energy Corporation | Working fluid composition for refrigerating machine |
| US9567284B2 (en) | 2012-10-24 | 2017-02-14 | Kh Neochem Co., Ltd. | Hexaester of mono-formal bis pentaerythritol |
| US9365484B2 (en) | 2012-10-24 | 2016-06-14 | Kh Neochem Co., Ltd. | Hexaester of mono-formal bis pentaerythritol |
| WO2014156737A1 (en) * | 2013-03-25 | 2014-10-02 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerator |
| US9719001B2 (en) | 2013-03-25 | 2017-08-01 | Jx Nippon Oil & Energy Corporation | Working fluid composition for refrigerator |
| JP2015017730A (en) * | 2013-07-10 | 2015-01-29 | 日立アプライアンス株式会社 | Air conditioner |
| US9546334B2 (en) | 2013-07-31 | 2017-01-17 | Kh Neochem Co., Ltd. | Refrigerating machine oil, and working fluid composition for refrigerating machine which is produced using same |
| WO2015093183A1 (en) * | 2013-12-20 | 2015-06-25 | 日立アプライアンス株式会社 | Air conditioner |
| JP2015117923A (en) * | 2013-12-20 | 2015-06-25 | 日立アプライアンス株式会社 | Air conditioner |
| JP2015140994A (en) * | 2014-01-30 | 2015-08-03 | 日立アプライアンス株式会社 | Air conditioner, and refrigerator oil |
| US10266788B2 (en) | 2014-05-30 | 2019-04-23 | Kh Neochem Co., Ltd. | Refrigerating-machine oil composition and working fluid composition including same for refrigerating machine |
| JP2016190892A (en) * | 2015-03-30 | 2016-11-10 | 出光興産株式会社 | Refrigerator lubricating oil and mixed composition for refrigerator |
| WO2016158306A1 (en) * | 2015-03-30 | 2016-10-06 | 出光興産株式会社 | Refrigerator lubricating oil and mixed composition for refrigerator |
| US10435641B2 (en) | 2015-03-30 | 2019-10-08 | Idemitsu Kosan Co., Ltd. | Refrigerator lubricating oil and mixed composition for refrigerator |
| KR20170132739A (en) * | 2015-03-30 | 2017-12-04 | 이데미쓰 고산 가부시키가이샤 | Mixing composition for refrigerator lubricating oil and refrigerator |
| KR102659403B1 (en) | 2015-03-30 | 2024-04-19 | 이데미쓰 고산 가부시키가이샤 | Refrigerator lubricants and mixed compositions for refrigerators |
| JP2016000837A (en) * | 2015-10-07 | 2016-01-07 | Jx日鉱日石エネルギー株式会社 | Working fluid composition for refrigerator |
| JP2017088978A (en) * | 2015-11-13 | 2017-05-25 | 日産自動車株式会社 | A sliding mechanism, a refrigerant compressor and an air conditioner using the sliding mechanism, and a method for manufacturing the sliding mechanism. |
| JPWO2017145278A1 (en) * | 2016-02-24 | 2018-10-11 | 三菱電機株式会社 | Refrigeration equipment |
| JPWO2017187828A1 (en) * | 2016-04-28 | 2019-02-14 | 東芝キヤリア株式会社 | Hermetic compressor and refrigeration cycle apparatus |
| WO2017187828A1 (en) * | 2016-04-28 | 2017-11-02 | 東芝キヤリア株式会社 | Hermetic compressor and refrigeration cycle device |
| JP2016164274A (en) * | 2016-05-12 | 2016-09-08 | Jxエネルギー株式会社 | Actuation fluid composition for refrigerator |
| US11390827B2 (en) | 2017-03-17 | 2022-07-19 | AGC Inc. | Composition for heat cycle system, and heat cycle system |
| JPWO2018169039A1 (en) * | 2017-03-17 | 2020-01-23 | Agc株式会社 | Composition for heat cycle system and heat cycle system |
| JP7108599B2 (en) | 2017-03-17 | 2022-07-28 | Agc株式会社 | COMPOSITION FOR THERMAL CYCLING SYSTEM AND THERMAL CYCLING SYSTEM |
| WO2019102532A1 (en) * | 2017-11-22 | 2019-05-31 | 三菱電機株式会社 | Compressor and refrigeration cycle device |
| JP2020031530A (en) * | 2018-08-20 | 2020-02-27 | ダイキン工業株式会社 | Refrigeration cycle device |
| US12085318B2 (en) | 2018-08-20 | 2024-09-10 | Daikin Industries, Ltd. | Refrigeration cycle apparatus |
| JP2019203138A (en) * | 2019-07-12 | 2019-11-28 | 出光興産株式会社 | Refrigerator lubricating oil and mixed composition for refrigerator |
| WO2023162923A1 (en) * | 2022-02-22 | 2023-08-31 | ダイキン工業株式会社 | Refrigeration cycle device |
| JP2023122122A (en) * | 2022-02-22 | 2023-09-01 | ダイキン工業株式会社 | Refrigeration cycle apparatus |
| JP7393680B2 (en) | 2022-02-22 | 2023-12-07 | ダイキン工業株式会社 | Refrigeration cycle equipment |
| US12228135B2 (en) | 2022-02-22 | 2025-02-18 | Daikin Industries, Ltd. | Refrigeration cycle apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| KR101280701B1 (en) | 2013-07-01 |
| CN102408936A (en) | 2012-04-11 |
| US20120024007A1 (en) | 2012-02-02 |
| KR20120023537A (en) | 2012-03-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101280701B1 (en) | Compressor for refrigerating air conditioning and refrigerating air conditioner | |
| JP5466772B2 (en) | Compressor for refrigeration and air-conditioning equipment | |
| JP5562920B2 (en) | Compressor for refrigeration and air-conditioning equipment | |
| JP6545337B1 (en) | Refrigeration cycle device | |
| CN104145008B (en) | Working fluid composition for refrigerating machine, refrigerator oil with and manufacture method | |
| CN104145006B (en) | Working fluid composition for refrigerating machine, refrigerating machine oil, and manufacturing method thereof | |
| JP2011052032A (en) | Refrigeration air-condition unit using 2,3,3,3-tetrafluoropropene | |
| WO2013146683A1 (en) | Working fluid composition for refrigerator | |
| WO2014134821A1 (en) | Low gwp heat transfer compositions including co2 | |
| CN103789070B (en) | refrigerating machine oil for refrigerant | |
| JP5872387B2 (en) | Compressor and air conditioner | |
| JPWO2019239528A1 (en) | Refrigerant composition and refrigeration cycle apparatus using the same | |
| JP5248960B2 (en) | Refrigerator oil, working fluid for refrigerator, and refrigerator | |
| JP2015529262A (en) | Low GWP heat transfer composition | |
| JP6522345B2 (en) | Refrigerating apparatus and sealed electric compressor | |
| JP6821075B1 (en) | Refrigeration cycle equipment | |
| KR20180017079A (en) | Ester for refrigeration oil and working fluid composition for refrigeration oil | |
| JP5667362B2 (en) | Reciprocating compressor and refrigerator using the same | |
| CN102732357A (en) | Refrigerator oil composition, preparation method thereof, and working fluid employing refrigerator oil composition |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20120824 |
|
| A761 | Written withdrawal of application |
Free format text: JAPANESE INTERMEDIATE CODE: A761 Effective date: 20130826 |