JP2014001255A - Compressor and air conditioner - Google Patents

Compressor and air conditioner Download PDF

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JP2014001255A
JP2014001255A JP2012135295A JP2012135295A JP2014001255A JP 2014001255 A JP2014001255 A JP 2014001255A JP 2012135295 A JP2012135295 A JP 2012135295A JP 2012135295 A JP2012135295 A JP 2012135295A JP 2014001255 A JP2014001255 A JP 2014001255A
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compressor
oil
polyol ester
refrigerant
ester oil
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JP5872387B2 (en
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Akira Ota
亮 太田
Takashi Izeki
崇 井関
Kuninari Araki
邦成 荒木
Akihiro Murakami
晃啓 村上
Ryoichi Takato
亮一 高藤
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Hitachi Appliances Inc
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Hitachi Appliances Inc
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Priority to JP2012135295A priority Critical patent/JP5872387B2/en
Priority to CN201380031349.5A priority patent/CN104379713B/en
Priority to PCT/JP2013/053351 priority patent/WO2013187084A1/en
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-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
    • C09K5/02Materials undergoing a change of physical state when used
    • C09K5/04Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
    • C09K5/041Materials 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
    • C09K5/044Materials 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
    • C09K5/045Materials 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
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M105/00Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
    • C10M105/08Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing oxygen
    • C10M105/32Esters
    • C10M105/38Esters of polyhydroxy compounds
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M171/00Lubricating 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
    • C10M171/008Lubricant compositions compatible with refrigerants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component 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
    • F04B39/02Lubrication
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2205/00Aspects relating to compounds used in compression type refrigeration systems
    • C09K2205/24Only one single fluoro component present
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/022Ethene
    • C10M2205/0225Ethene used as base material
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/028Organic 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
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/028Organic 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
    • C10M2205/0285Organic 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/283Esters of polyhydroxy compounds
    • C10M2207/2835Esters of polyhydroxy compounds used as base material
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/30Complex esters, i.e. compounds containing at leasst three esterified carboxyl groups and derived from the combination of at least three different types of the following five types of compounds: monohydroxyl compounds, polyhydroxy xompounds, monocarboxylic acids, polycarboxylic acids or hydroxy carboxylic acids
    • C10M2207/301Complex esters, i.e. compounds containing at leasst three esterified carboxyl groups and derived from the combination of at least three different types of the following five types of compounds: monohydroxyl compounds, polyhydroxy xompounds, monocarboxylic acids, polycarboxylic acids or hydroxy carboxylic acids used as base material
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01Physico-chemical properties
    • C10N2020/02Viscosity; Viscosity index
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    • C10N2020/00Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01Physico-chemical properties
    • C10N2020/071Branched chain compounds
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    • C10N2020/00Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/09Characteristics associated with water
    • C10N2020/097Refrigerants
    • C10N2020/101Containing Hydrofluorocarbons
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/06Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
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    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/10Inhibition of oxidation, e.g. anti-oxidants
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    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/70Soluble oils
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    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/30Refrigerators lubricants or compressors lubricants

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  • Lubricants (AREA)
  • Compressor (AREA)
  • Applications Or Details Of Rotary Compressors (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve the efficiency of a compressor by inhibiting leakage of a refrigerant.SOLUTION: In a compressor which is provided with a compression chamber having a sliding part and includes difluoromethane as a refrigerant and a refrigerating machine oil. The refrigerating machine oil is a polyol ester oil which is a mixture of a compound represented by a chemical formula (1) (wherein Ris an alkyl group having 3-8 carbon atoms) and a compound represented by a chemical formula (2), contains 20 mol% or more of the compound represented by the chemical formula (2), and has a kinematic viscosity of 30-90 mm/s at 40°C, the low temperature-side critical solution temperature of the refrigerant and the polyol ester oil is +10°C or lower, and the polyol ester oil contains 1-30 wt% of a compression part sealant having a kinematic viscosity of more than 180 mm/s at 40°C based on the polyol ester oil.

Description

本発明は、圧縮機及び空調装置に関する。   The present invention relates to a compressor and an air conditioner.

空調機器分野に使用される冷媒のR410Aは、HFC(Hydrofluorocarbons)32/HFC125(50/50重量%)の混合物であり、GWP(Global Warming Potential)=2088と高いため、GWPが低い代替冷媒を用いた空調装置の開発が急務である。   R410A, a refrigerant used in the field of air conditioning equipment, is a mixture of HFC (Hydrofluorocarbons) 32 / HFC125 (50/50 wt%) and has a high GWP (Global Warming Potential) = 2088. Therefore, an alternative refrigerant with a low GWP is used. There is an urgent need to develop an air conditioning system.

この代替冷媒としては、熱物性、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(Hydrofluoroolefin)(GWP=4)、1,3,3,3−テトラフルオロプロペン(HFO1234ze)(GWP=10)若しくはジフルオロメタン(HFC32)の単独冷媒又はこれらの混合冷媒が候補とされている。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、及びフルオロエタン(HFC161)、ジフルオロエタン(HFC152a)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。これらの冷媒候補の中で、可燃性、冷暖房能力、非共沸冷媒の温度勾配による機器効率低下、取り扱い易さ、冷媒コスト、機器の変更(開発)などを考慮すると、ジフルオロメタン(HFC32)が最も良い。   As this alternative refrigerant, 2,3,3,3-tetrafluoropropene (HFO1234yf (Hydrofluoroolefin) (GWP = 4), 1,3,3) is used for reasons such as thermophysical properties, low GWP, low toxicity, and low flammability. , 3-tetrafluoropropene (HFO1234ze) (GWP = 10) or difluoromethane (HFC32) alone or a mixture of these refrigerants, other refrigerants include hydrocarbons such as propane and propylene, and Low GWP hydrofluorocarbons such as fluoroethane (HFC161), difluoroethane (HFC152a), etc. Among these refrigerant candidates, combustibility, cooling / heating capability, equipment efficiency decrease due to temperature gradient of non-azeotropic refrigerant, handling Considering ease, refrigerant costs, equipment changes (development), etc. Trifluoromethane (HFC32) is the best.

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。冷凍機油で重要な特性の一つが、冷媒との相溶性である。しかし、HFC32では冷凍機油との相溶性が低いため、例えば特許文献1、特許文献2、特許文献3には、HFC32との相溶性を向上した冷凍機油が開示されている。   The refrigeration oil is used in a hermetic electric compressor and plays a role of lubrication, sealing, cooling and the like of the sliding part. One of the important characteristics of refrigeration oil is its compatibility with refrigerants. However, since HFC32 has low compatibility with refrigerating machine oil, for example, Patent Document 1, Patent Document 2, and Patent Document 3 disclose refrigerating machine oil having improved compatibility with HFC32.

特開2010−235960号公報JP 2010-235960 A 特開2002−129178号公報JP 2002-129178 A

しかし、HFC32は断熱指数が小さいことにより、吐出温度が高くなり、これによって圧縮機の温度も高くなることから冷媒吸い込み時に過熱損失が起こる。さらに分子量が小さく分子速度が速いため圧縮機の圧縮部からの冷媒漏れが生じ易い。このため体積効率低下に起因する圧縮機効率の低下が発生してしまう。上記の特許文献のものは、いずれも冷媒漏れについて十分考慮されていない。   However, since the HFC 32 has a small adiabatic index, the discharge temperature becomes high, and thus the temperature of the compressor also becomes high, so that overheating loss occurs when the refrigerant is sucked. Furthermore, since the molecular weight is small and the molecular velocity is high, refrigerant leakage from the compression part of the compressor is likely to occur. For this reason, a decrease in compressor efficiency due to a decrease in volumetric efficiency occurs. None of the above-mentioned patent documents sufficiently considers refrigerant leakage.

本発明の目的は、冷媒漏れを抑制して圧縮機効率を向上させることにある。   An object of the present invention is to improve refrigerant efficiency by suppressing refrigerant leakage.

上記目的を達成するために、本発明は、摺動部を有する圧縮室を備え、冷媒であるジフルオロメタンと、冷凍機油とを封入した圧縮機において、前記冷凍機油は、化学式(1)で表される化合物(式中、R1〜R6は炭素数3〜8のアルキル基)と化学式(2)で表される化合物との混合物であり、前記化学式(2)で表される化合物を20モル%以上含み、40℃における動粘度が30〜90mm2/sのポリオールエステル油であり、前記冷媒と前記ポリオールエステル油との低温側臨界溶解温度が+10℃以下であり、前記ポリオールエステル油に40℃における動粘度が180mm2/sを超える圧縮部シール剤を前記ポリオールエステル油に対して1〜30重量%含むことを特徴とする。 In order to achieve the above object, the present invention is a compressor including a compression chamber having a sliding portion and enclosing difluoromethane, which is a refrigerant, and refrigerating machine oil, wherein the refrigerating machine oil is represented by the chemical formula (1). Is a mixture of the compound represented by the chemical formula (2) and the compound represented by the chemical formula (2), wherein R 1 to R 6 are alkyl groups having 3 to 8 carbon atoms. It is a polyol ester oil having a kinematic viscosity at 40 ° C. of 30 to 90 mm 2 / s, containing at least mol%, and having a low temperature side critical solution temperature of + 10 ° C. or less between the refrigerant and the polyol ester oil. 1-30 weight% of the compression part sealing agent with a kinematic viscosity in 40 degreeC exceeding 180 mm < 2 > / s is included with respect to the said polyol ester oil, It is characterized by the above-mentioned.

本発明によれば、冷媒漏れを抑制して圧縮機効率を向上させることができる。   According to the present invention, it is possible to improve refrigerant efficiency by suppressing refrigerant leakage.

空調装置の構成を示す概略図である。It is the schematic which shows the structure of an air conditioner. スクロール式密閉型圧縮機を示す断面図である。It is sectional drawing which shows a scroll-type hermetic compressor.

以下、本発明の実施例について詳細に説明する。
圧縮機は、摺動部を有する圧縮室を備え、冷媒であるジフルオロメタンと、冷凍機油とを封入したものである。ここで、冷凍機油は、40℃における動粘度が30〜90mm2/sの下記化学式(1)で表される化合物及び化学式(2)で表される化合物(式中、R1〜R6は、炭素数3〜8のアルキル基を表し、同じでも異なってもよい)からなる混合物であり、化学式(2)で表される化合物を20モル%以上含むポリオールエステル油である。そして、冷媒とポリオールエステル油との低温側臨界溶解温度が+10℃以下であり、40℃における動粘度が180mm2/sを超える圧縮部シール剤を、ポリオールエステル油に対して1〜30重量%含む冷凍機油である。
Examples of the present invention will be described in detail below.
The compressor includes a compression chamber having a sliding portion, and encloses difluoromethane, which is a refrigerant, and refrigerating machine oil. Here, the refrigerating machine oil is a compound represented by the following chemical formula (1) having a kinematic viscosity of 30 to 90 mm 2 / s at 40 ° C. and a compound represented by the chemical formula (2) (wherein R 1 to R 6 are Represents a C 3-8 alkyl group, which may be the same or different, and is a polyol ester oil containing 20 mol% or more of the compound represented by the chemical formula (2). And the low temperature side critical melt | dissolution temperature of a refrigerant | coolant and a polyol ester oil is +10 degrees C or less, and 1-30 weight% with respect to a polyol ester oil is a compression part sealing agent with a kinematic viscosity in 40 degreeC exceeding 180 mm < 2 > / s. Contains refrigeration oil.

実施例は、ジフルオロメタンを用いた圧縮機及びこれを用いた空調装置について開示するものである。冷媒は、ジフルオロメタンであり、冷凍機油は、ポリオールエステル油である。   The embodiment discloses a compressor using difluoromethane and an air conditioner using the compressor. The refrigerant is difluoromethane, and the refrigerating machine oil is polyol ester oil.

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。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、原料となる多価アルコールとして好ましいものは、ペンタエリスリトール、ジペンタエリスリトールである。   The polyol ester oil is obtained by a condensation reaction between a polyhydric alcohol and a monovalent fatty acid. As the polyol ester oil, a hindered type having excellent heat stability is preferable, and as the polyhydric alcohol used as a raw material, pentaerythritol and dipentaerythritol are preferable.

また、原料となる一価の脂肪酸としては、n−ブタン酸、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−メチルプロピオン酸、2−メチルブタン酸、3−メチルブタン酸、2−メチルペンタン酸、2−エチルブタン酸、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。   Examples of the monovalent fatty acid used as a raw material include n-butanoic acid, n-pentanoic acid, n-hexanoic acid, n-heptanoic acid, n-octanoic acid, 2-methylpropionic acid, 2-methylbutanoic acid, 3- There are methylbutanoic acid, 2-methylpentanoic acid, 2-ethylbutanoic acid, 2-methylhexanoic acid, 2-ethylhexanoic acid, isooctanoic acid, 3,5,5-trimethylhexanoic acid, etc. Used by mixing.

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においては、40℃における動粘度が46〜90mm2/sの範囲であることが好ましい。また、ロータリー式圧縮機においては、40℃における動粘度が30〜70mm2/sの範囲であることが好ましい。 The viscosity grade of the refrigerating machine oil varies depending on the type of the compressor, but in the scroll compressor, the kinematic viscosity at 40 ° C. is preferably in the range of 46 to 90 mm 2 / s. In the rotary compressor, the kinematic viscosity at 40 ° C. is preferably in the range of 30 to 70 mm 2 / s.

圧縮部シール剤は、40℃における動粘度が180mm2/sを超える液状化合物である。ヒンダードタイプのポリオールエステル油の場合は、ジペンタエリスリトール系の脂肪酸エステル(化学式(3)(式中、R7、R8は炭素数7〜8のアルキル基))が高粘度となりやすく、冷媒漏れを低減することができる。ジペンタエリスリトールは、原料にペンタエリスリトールやトリペンタエリスリトールなどを多く含むため純物質ではないがここではジペンタエリスリトール系と表記することにする。また、コンプレックスタイプのポリオールエステル油(コンプレックスエステル油)(化学式(4)(式中、R9、R10は炭素数3〜9のアルキル基、R11は炭素数1〜9のアルキル基、nは正数))は、多価アルコールと二価の脂肪酸と一価の脂肪酸とが結合したエステル化合物である。 The compression part sealant is a liquid compound having a kinematic viscosity at 40 ° C. exceeding 180 mm 2 / s. In the case of a hindered type polyol ester oil, dipentaerythritol fatty acid ester (chemical formula (3) (wherein R 7 and R 8 are alkyl groups having 7 to 8 carbon atoms)) tends to have high viscosity, Leakage can be reduced. Dipentaerythritol is not a pure substance because it contains a large amount of pentaerythritol, tripentaerythritol, and the like as raw materials, but here it will be expressed as dipentaerythritol. Also, complex type polyol ester oil (complex ester oil) (chemical formula (4) (wherein R 9 and R 10 are alkyl groups having 3 to 9 carbon atoms, R 11 is an alkyl group having 1 to 9 carbon atoms, n Is an ester compound in which a polyhydric alcohol, a divalent fatty acid and a monovalent fatty acid are bonded.

ここで、原料となる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及びペンタエリスリトールである。また、原料となる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。さらに、原料となる二価の脂肪酸としては、プロパン二酸、ブタン二酸、ペンタン二酸、ヘキサン二酸、ヘプタン二酸、オクタン二酸等があり、これらを単独又は2種類以上を混合して用いる。前記したジペンタエリスリトール系の脂肪酸エステルを混合したり、また、粘度調整用として通常のポリオールエステル油成分などを混ぜてもよい。   Here, what is preferable as a polyhydric alcohol used as a raw material is, for example, neopentyl glycol, trimethylolpropane and pentaerythritol. The monovalent fatty acid used as a raw material includes n-pentanoic acid, n-hexanoic acid, n-heptanoic acid, n-octanoic acid, 2-methylbutanoic acid, 2-methylpentanoic acid, 2-methylhexanoic acid, 2 -Ethylhexanoic acid, isooctanoic acid, 3,5,5-trimethylhexanoic acid and the like are used alone or in combination of two or more. Furthermore, as the divalent fatty acid as a raw material, there are propanedioic acid, butanedioic acid, pentanedioic acid, hexanedioic acid, heptanedioic acid, octanedioic acid, etc., and these may be used alone or in combination of two or more. Use. The dipentaerythritol fatty acid ester described above may be mixed, or a normal polyol ester oil component or the like may be mixed for viscosity adjustment.

また、エチレン−α−オレフィン共重合体は任意の高粘度が得られやすく、せん断安定性にも優れており、数平均分子量が800〜4000のものが良い。エチレン−α−オレフィン共重合体を構成するα−オレフィンとしては、炭素数が、3〜10のものが用いられ、プロピレン、1−ブテン、イソブテン、1−ペンテン、1−ヘキセン、1−オクテン、1−デセンなどが挙げられる。これらのα−オレフィンは一種を用いてもよく、二種以上を組合せて用いてもよい。また、エチレンの含有量は、20〜80モル%がより好ましく、α−オレフィンとランダム及びブロック共重合のいずれであってもよい。   In addition, the ethylene-α-olefin copolymer is easy to obtain an arbitrary high viscosity, is excellent in shear stability, and has a number average molecular weight of 800 to 4000. As the α-olefin constituting the ethylene-α-olefin copolymer, those having 3 to 10 carbon atoms are used, and propylene, 1-butene, isobutene, 1-pentene, 1-hexene, 1-octene, Examples include 1-decene. These α-olefins may be used singly or in combination of two or more. Moreover, as for ethylene content, 20-80 mol% is more preferable, Any of an alpha olefin and random and block copolymerization may be sufficient.

前記した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が望ましい。   Even if a lubricity improver, an antioxidant, an acid scavenger, an antifoaming agent, a metal deactivator, etc. are added to the refrigerating machine oil, there is no problem. In particular, the polyol ester oil is deteriorated due to hydrolysis in the presence of moisture, and therefore, an antioxidant and an acid scavenger are preferably blended.

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。酸捕捉剤としては、一般に、エポキシ環を有する化合物である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。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。   As the antioxidant, DBPC (2,6-di-t-butyl-p-cresol) which is a phenol type is preferable. As the acid scavenger, an aliphatic epoxy compound or a carbodiimide compound, which is a compound having an epoxy ring, is generally used. 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. Examples of the carbodiimide compound include bis (2,6-isopropylphenyl) carbodiimide. The amount of the acid scavenger is preferably 0.05 to 1.0% by weight with respect to the refrigerating machine oil.

図1は、空調装置の概略を示したものである。空調装置は、室内機1と室外機2を備えている。室内機1には、室内熱交換器5が内蔵されている。また、室外機2には、圧縮機3、四方弁4、室外熱交換器7及び膨張装置6が内蔵されている。   FIG. 1 shows an outline of an air conditioner. The air conditioner includes an indoor unit 1 and an outdoor unit 2. An indoor heat exchanger 5 is built in the indoor unit 1. The outdoor unit 2 includes a compressor 3, a four-way valve 4, an outdoor heat exchanger 7, and an expansion device 6.

室内を冷房する場合、圧縮機3にて断熱的に圧縮された高温高圧の冷媒ガスは、吐出パイプ及び四方弁4を通って室内熱交換器5(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、膨張装置6(例えば、温度式膨張弁など)で膨張し、僅かにガスを含む低温低圧液となって室外熱交換器7(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4を通って圧縮機3に至る。室内を暖房する場合は、四方弁4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 compressed in an adiabatic manner by the compressor 3 is cooled by the indoor heat exchanger 5 (used as a condensing means) through the discharge pipe and the four-way valve 4, It becomes a high-pressure liquid refrigerant. This refrigerant expands in the expansion device 6 (for example, a temperature type expansion valve), becomes a low-temperature low-pressure liquid containing a slight amount of gas, reaches the outdoor heat exchanger 7 (used as an evaporation means), and indoor air Then, the heat is obtained, and the refrigerant reaches the compressor 3 through the four-way valve 4 again 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 4, and the reverse action occurs.

圧縮機3としては、スクロール式圧縮機を用いた。図2は、スクロール式圧縮機の概略構造を示したものである。圧縮機3は、端板9に垂直に設けられた渦巻状ラップ10を有する固定スクロール部材8と、この固定スクロール部材8と実質的に同一形状のラップ12を有する旋回スクロール部材11と、旋回スクロール部材11を支持するフレーム16と、旋回スクロール部材11を旋回運動させるクランクシャフト13と、電動モータ19と、これらを内蔵する圧力容器17とを含む。渦巻状ラップ10とラップ12とは、互いに向い合わせにして噛み合わせ、圧縮部を形成してある。   As the compressor 3, a scroll type compressor was used. FIG. 2 shows a schematic structure of the scroll compressor. The compressor 3 includes a fixed scroll member 8 having a spiral wrap 10 provided perpendicularly to an end plate 9, a revolving scroll member 11 having a wrap 12 having substantially the same shape as the fixed scroll member 8, and a revolving scroll. It includes a frame 16 that supports the member 11, a crankshaft 13 that orbits the orbiting scroll member 11, an electric motor 19, and a pressure vessel 17 that houses these. The spiral wrap 10 and the wrap 12 are engaged with each other so as to form a compression portion.

旋回スクロール部材11は、クランクシャフト13によって旋回運動させると、固定スクロール部材8と旋回スクロール部材11との間に形成される圧縮室14のうち、最も外側に位置している圧縮室14が旋回運動に伴って容積を次第に縮小しながら、固定スクロール部材8及び旋回スクロール部材11の中心部に向かって移動していく。圧縮室14が固定スクロール部材8及び旋回スクロール部材11の中心部近傍に達すると、圧縮室14が吐出口15と連通し、圧縮室14の内部の圧縮ガスが吐出パイプ18から圧縮機3の外部に吐出される。   When the orbiting scroll member 11 is orbitally moved by the crankshaft 13, the outermost compression chamber 14 of the compression chambers 14 formed between the fixed scroll member 8 and the orbiting scroll member 11 is orbitally moved. As the volume is gradually reduced, the fixed scroll member 8 and the orbiting scroll member 11 move toward the center. When the compression chamber 14 reaches the vicinity of the center of the fixed scroll member 8 and the orbiting scroll member 11, the compression chamber 14 communicates with the discharge port 15, and the compressed gas inside the compression chamber 14 is discharged from the discharge pipe 18 to the outside of the compressor 3. Discharged.

圧縮機3においては、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13が回転し、圧縮動作を行う。また、電動モータ19の下方には、油溜め部22が設けられており、油溜め部22の油は、圧力差によってクランクシャフト13に設けられた油孔21を通って、旋回スクロール部材11とクランクシャフト13との摺動部、滑り軸受け20等の潤滑に供される。   In the compressor 3, the crankshaft 13 rotates at a constant speed or at a rotational speed corresponding to a voltage controlled by an inverter (not shown) to perform a compression operation. An oil reservoir 22 is provided below the electric motor 19, and the oil in the oil reservoir 22 passes through an oil hole 21 provided in the crankshaft 13 due to a pressure difference, and the orbiting scroll member 11. This is used for lubrication of the sliding portion with the crankshaft 13, the sliding bearing 20, and the like.

(実施例1〜3及び比較例1、2)
日本工業規格(JIS C 9612−2005;ルームエアコンディショナ)に基づき、通年エネルギー消費効率APFを算出した。また、別途、圧縮機の性能試験を実施し、代表条件からの体積効率を測定した。実施例に用いた冷媒は、ジフルオロメタンであり、主剤である冷凍機油と添加剤である圧縮部シール剤を下記に示す。
(Examples 1 to 3 and Comparative Examples 1 and 2)
Based on the Japanese Industrial Standard (JIS C 9612-2005; room air conditioner), year-round energy consumption efficiency APF was calculated. Separately, a compressor performance test was performed to measure volumetric efficiency from representative conditions. The refrigerant used in the examples is difluoromethane, and the refrigerating machine oil as the main agent and the compression part sealing agent as the additive are shown below.

(冷凍機油)
(A)ヒンダードタイプポリオールエステル油(ペンタエリスリトール/ジペンタエリス
リトール系の2−メチルブタン酸/2−エチルヘキサン酸の混合脂肪酸エステル油)
:40℃粘度68.7mm2/s
(B)ヒンダードタイプポリオールエステル油(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℃粘
度64.9mm2/s
(Refrigerator oil)
(A) Hindered type polyol ester oil (pentaerythritol / dipentaerythritol 2-methylbutanoic acid / 2-ethylhexanoic acid mixed fatty acid ester oil)
: 40 ° C viscosity 68.7 mm 2 / s
(B) hindered type polyol ester oil (pentaerythritol-based 2-ethylhexanoic acid / 3,5,5-trimethylhexanoic acid mixed fatty acid ester oil): 40 ° C. viscosity 64.9 mm 2 / s

(圧縮部シール剤)
(F)ヒンダードタイプポリオールエステル油(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℃
粘度217mm2/s
(G)コンプレックスタイプポリオールエステル油(ネオペンチルグリコールとジカルボ
ン酸とモノカルボン酸とが結合したエステルであり、ジカルボン酸としてアジピン酸
、モノカルボン酸として3,5,5−トリメチルヘキサン酸を用いたエステル油):
40℃粘度260mm2/s
(H)エチレン−α−オレフィン共重合体(商品名:ルーカントHC−40:三井化学株
式会社製、ルーカントは同社の登録商標):40℃粘度380mm2/s
(Compression part sealant)
(F) Hindered type polyol ester oil (dipentaerythritol-based 2-ethylhexanoic acid / 3,5,5-trimethylhexanoic acid mixed fatty acid ester oil): 40 ° C.
Viscosity 217mm 2 / s
(G) Complex type polyol ester oil (neopentyl glycol, dicarboxylic acid, and monocarboxylic acid ester, adipic acid as dicarboxylic acid, 3,5,5-trimethylhexanoic acid as monocarboxylic acid Ester oil):
40 ° C viscosity 260mm 2 / s
(H) ethylene-α-olefin copolymer (trade name: Lucant HC-40: manufactured by Mitsui Chemicals, Lucant is a registered trademark of the company): 40 ° C. viscosity 380 mm 2 / s

実施例1〜3では、冷凍機油(A)に圧縮部シール剤として(F)(G)(H)をそれぞれ5.0重量%配合した。いずれも配合後の冷凍機油の動粘度は70mm2/s近傍である。冷凍機油(A)はジフルオロメタンとの低温側臨界溶解温度が−2℃であり、相溶性を示す冷凍機油である。圧縮機に封入される冷媒及び冷凍機油の相溶性は、前述したように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維持等、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。ジフルオロメタンと冷凍機油との相溶性評価は、JIS K 2211に準じて測定した。相溶性評価においては、冷媒に混合した油の濃度(油濃度)を横軸とし、溶解温度を縦軸としたグラフを作成した。このグラフは、一般に、二層に分離する温度の油濃度依存性を示すものであり、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定義した。 In Examples 1 to 3, 5.0% by weight of (F), (G), and (H) as blending part sealants was blended with the refrigerating machine oil (A). In any case, the kinematic viscosity of the refrigerating machine oil after blending is around 70 mm 2 / s. The refrigerating machine oil (A) is a refrigerating machine oil having a low-temperature side critical dissolution temperature with difluoromethane of −2 ° C. and exhibiting compatibility. As described above, the compatibility of refrigerant and refrigeration oil enclosed in the compressor is the reliability of the compressor, such as the return of oil from the refrigeration cycle to the compressor (to ensure the amount of oil inside the compressor) or the maintenance of heat exchange efficiency. This is one of the important characteristics in terms of guaranteeing safety. The compatibility evaluation of difluoromethane and refrigerating machine oil was measured according to JIS K 2211. In the compatibility evaluation, a graph was created with the horizontal axis representing the concentration of oil mixed in the refrigerant (oil concentration) and the vertical axis representing the dissolution temperature. This graph generally shows the oil concentration dependence of the temperature at which the two layers are separated, and is a curve having a maximum value. This maximum value was defined as the low temperature critical solution temperature.

比較例1では、現行の機器で使用される冷媒R410Aと冷凍機油(B)を用いた組合せとした。低温側臨界溶解温度は+9℃であり、圧縮部シール剤は配合されていない。この比較例1を効率の基準値(APF比)100%とした。比較例2は、実施例1〜3から圧縮機シール剤が配合されていない組合せとした。測定項目は、通年エネルギー消費効率APFと圧縮機の体積効率比を空調装置の代表運転条件である暖房定格、暖房中間、冷房定格、冷房中間の4条件において比較した。比較例1の現行機器を基準100%として、実施例1〜3と比較例2のAPFと体積効率比を検討した。   In the comparative example 1, it was set as the combination using refrigerant | coolant R410A and refrigeration oil (B) which are used with the present apparatus. The low temperature side critical dissolution temperature is + 9 ° C., and no compression part sealant is blended. The comparative example 1 was set to 100% efficiency reference value (APF ratio). The comparative example 2 was made into the combination by which the compressor sealing agent was not mix | blended from Examples 1-3. As the measurement items, the year-round energy consumption efficiency APF and the volumetric efficiency ratio of the compressor were compared under the four conditions of heating rating, heating middle, cooling rating, and cooling middle, which are typical operation conditions of the air conditioner. The APF and volumetric efficiency ratio of Examples 1 to 3 and Comparative Example 2 were examined using the current device of Comparative Example 1 as the reference 100%.

表1に結果を示す。比較例1と比較例2とを比べるとジフルオロメタンを用いた場合、APFが約1.0%向上している。これは、ジフルオロメタンの潜熱が大きく、圧力損失が小さいためにAPFが向上すると考えられる。しかし、圧縮機の体積効率をみると、APFは向上したにもかかわらず、ジフルオロメタンを用いた圧縮機では、体積効率がいずれの条件においても低下する。ジフルオロメタンは断熱指数が小さく吐出温度が高くなるため圧縮機の温度も高くなり、吸い込み時の過熱損失が生じ易い。さらに分子量が小さく分子速度が速いため圧縮機の圧縮部から冷媒が漏れやすいため、体積効率低下が発生してしまう。これに対して、実施例1〜3で示すようにジフルオロメタンと冷凍機油(A)に圧縮部シール剤を5重量%配合した空調機器では、比較例2と比べて圧縮機の体積効率が向上しており、機器のAPFも増加することがわかった。   Table 1 shows the results. Comparing Comparative Example 1 and Comparative Example 2, when difluoromethane is used, the APF is improved by about 1.0%. This is considered that APF improves because the latent heat of difluoromethane is large and the pressure loss is small. However, when looking at the volumetric efficiency of the compressor, the volumetric efficiency of the compressor using difluoromethane decreases under any conditions, even though the APF has improved. Since difluoromethane has a small adiabatic index and a high discharge temperature, the temperature of the compressor is also high, and overheating loss during suction is likely to occur. Furthermore, since the molecular weight is small and the molecular velocity is high, the refrigerant is liable to leak from the compression part of the compressor, resulting in a decrease in volume efficiency. On the other hand, as shown in Examples 1 to 3, the volumetric efficiency of the compressor is improved as compared with Comparative Example 2 in the air conditioning apparatus in which 5% by weight of the compression sealant is blended with difluoromethane and the refrigerating machine oil (A). It has been found that the APF of the device also increases.

(実施例4〜6及び比較例3、4)
実施例4〜6で冷凍機油の潤滑性を評価した。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。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)と摩擦係数を測定した。冷凍機油(B)と圧縮部シール剤(F)は実施例1〜3のものと同じである。
(Examples 4 to 6 and Comparative Examples 3 and 4)
In Examples 4 to 6, the lubricity of the refrigerating machine oil was evaluated. The lubricity of refrigeration oil was evaluated using a shell-type four-ball frictional wear tester. Wear test piece diameters (average of 3 pieces) and friction after test with 1/2 inch SUJ2 steel ball as test piece, load: 280 N, temperature: 120 ° C., rotational speed: 1200 / min, time: 10 min The coefficient was measured. The refrigerating machine oil (B) and the compression part sealant (F) are the same as those in Examples 1 to 3.

(冷凍機油)
(A)ヒンダードタイプポリオールエステル油(ペンタエリスリトール/ジペンタエリス
リトール系の2−メチルブタン酸/2−エチルヘキサン酸の混合脂肪酸エステル油)
:40℃粘度68.7mm2/s
ジペンタエリスリトール配合量約50モル%
(C)ヒンダードタイプポリオールエステル油(ペンタエリスリトール/ジペンタエリス
リトール系の2−メチルブタン酸/2−エチルヘキサン酸の混合脂肪酸エステル油)
:40℃粘度67.3mm2/s
ジペンタエリスリトール配合量約35モル%
(D)ヒンダードタイプポリオールエステル油(ペンタエリスリトール/ジペンタエリス
リトール系の2−メチルブタン酸/2−エチルヘキサン酸の混合脂肪酸エステル油)
:40℃粘度66.2mm2/s
ジペンタエリスリトール配合量約25モル%
(E)ヒンダードタイプポリオールエステル油(ペンタエリスリトール/ジペンタエリス
リトール系の2−メチルブタン酸/2−エチルヘキサン酸の混合脂肪酸エステル油)
:40℃粘度65.3mm2/s
ジペンタエリスリトール配合量約10モル%
(Refrigerator oil)
(A) Hindered type polyol ester oil (pentaerythritol / dipentaerythritol 2-methylbutanoic acid / 2-ethylhexanoic acid mixed fatty acid ester oil)
: 40 ° C viscosity 68.7 mm 2 / s
Dipentaerythritol compounding amount about 50 mol%
(C) hindered type polyol ester oil (pentaerythritol / dipentaerythritol mixed fatty acid ester oil of 2-methylbutanoic acid / 2-ethylhexanoic acid)
: 40 ° C viscosity 67.3 mm 2 / s
Dipentaerythritol compounding amount about 35 mol%
(D) Hindered type polyol ester oil (pentaerythritol / dipentaerythritol 2-methylbutanoic acid / 2-ethylhexanoic acid mixed fatty acid ester oil)
: 40 ° C viscosity 66.2 mm 2 / s
Dipentaerythritol compounding amount approximately 25 mol%
(E) Hindered type polyol ester oil (pentaerythritol / dipentaerythritol 2-methylbutanoic acid / 2-ethylhexanoic acid mixed fatty acid ester oil)
: 40 ° C viscosity 65.3 mm 2 / s
Dipentaerythritol compounding amount about 10 mol%

冷凍機油として、(A)(C)(D)はジペンタエリスリトールを20モル%以上配合し、いずれの冷凍機油にも圧縮部シール剤として(F)を5.0重量%配合している。   As refrigerating machine oils, (A), (C), and (D) contain 20 mol% or more of dipentaerythritol, and 5.0% by weight of (F) is added to any refrigerating machine oil as a compression part sealant.

各冷凍機油の潤滑性を評価した結果を表2に示す。比較例4で示すように冷凍機油成分にジペンタエリスリトールが配合されていない場合は、摩耗痕径が大きく、摩擦係数が高い。これに対して、実施例4〜6で示すように冷凍機油成分にジペンタエリスリトールが20重量%以上配合されたものは、摩耗痕径と摩擦係数が抑制されており、潤滑性が優れていることがわかる。これはジペンタエリスリトールの摩擦面に対する吸着能力が大きく、摩擦面の表面エネルギーが低下し、耐摩耗性と摩擦係数の低減効果が得られたことによる。比較例3で示すように冷凍機油成分にジペンタエリスリトール配合量が20重量%未満のものは、摩耗痕径が大きく、摩擦係数も高く、十分な潤滑性が得られないことがわかった。   Table 2 shows the results of evaluating the lubricity of each refrigeration oil. As shown in Comparative Example 4, when dipentaerythritol is not blended in the refrigerator oil component, the wear scar diameter is large and the friction coefficient is high. On the other hand, as shown in Examples 4 to 6, a blend of 20% by weight or more of dipentaerythritol in the refrigerating machine oil component has reduced wear scar diameter and friction coefficient, and is excellent in lubricity. I understand that. This is because dipentaerythritol has a large adsorption capacity to the friction surface, the surface energy of the friction surface is reduced, and the effect of reducing wear resistance and friction coefficient is obtained. As shown in Comparative Example 3, it was found that when the amount of dipentaerythritol blended in the refrigerating machine oil component was less than 20% by weight, the wear scar diameter was large, the friction coefficient was high, and sufficient lubricity could not be obtained.

(実施例7〜9及び比較例5、6)
次に、実施例1で効果を確認した冷凍機油と圧縮部シール剤を用いて、圧縮機シール剤の配合量についての検討を行った。測定項目、測定方法、冷凍機油(A)、圧縮部シール剤(F)は実施例1〜3のものと同じである。
(Examples 7 to 9 and Comparative Examples 5 and 6)
Next, the refrigerating machine oil and the compression part sealant whose effects were confirmed in Example 1 were used to study the blending amount of the compressor sealant. Measurement items, measurement method, refrigerator oil (A), and compression section sealant (F) are the same as those in Examples 1-3.

実施例7〜9では、冷凍機油(A)に圧縮部シール剤として(F)を1〜30重量%の範囲で配合した。比較例5では圧縮部シール剤として(F)を0.5重量%とし、比較例6では圧縮部シール剤として(F)を40重量%配合して、試験を実施した。   In Examples 7-9, (F) was mix | blended with refrigeration oil (A) as a compression part sealing agent in the range of 1-30 weight%. In Comparative Example 5, (F) was 0.5% by weight as the compression part sealant, and in Comparative Example 6, 40% by weight (F) was blended as the compression part sealant.

結果を表3に示す。比較例2と比べると実施例7〜9では、APFが0.5〜1.0%向上している。これは、圧縮部シール剤により圧縮機の圧縮部のシール性が向上した効果による。これに対して比較例5で示すように、圧縮部シール剤として(F)を0.5重量%とした実施形態では、比較例2と比べて圧縮機の体積効率やAPFの向上は得られていない。また、比較例6で示すように圧縮部シール剤として(F)を40重量%も配合してしまうと、冷凍機油の動粘度も大きく増加してしまい、粘性抵抗が増大することによるAPFが低下する。このことから、冷凍機油に対して圧縮部シール剤の配合量は、1.0〜30重量%の範囲が良い。   The results are shown in Table 3. Compared with Comparative Example 2, in Examples 7 to 9, APF is improved by 0.5 to 1.0%. This is due to the effect of improving the sealing performance of the compression part of the compressor by the compression part sealant. On the other hand, as shown in Comparative Example 5, in the embodiment in which (F) is 0.5% by weight as the compression part sealant, the volume efficiency and APF of the compressor are improved as compared with Comparative Example 2. Not. Further, as shown in Comparative Example 6, when 40 wt% of (F) is blended as the compression part sealant, the kinematic viscosity of the refrigerating machine oil is greatly increased, and the APF is decreased due to an increase in the viscous resistance. To do. For this reason, the blending amount of the compression section sealant with respect to the refrigerating machine oil is preferably in the range of 1.0 to 30% by weight.

以上の結果から、圧縮機の圧縮部からの冷媒漏れを低減し、圧縮機の体積効率を向上させることができ、空調装置の通年エネルギー消費効率APFを向上させることができる。   From the above results, it is possible to reduce refrigerant leakage from the compressor section of the compressor, improve the volume efficiency of the compressor, and improve the year-round energy consumption efficiency APF of the air conditioner.

圧縮機としては、スクロール式圧縮機の他、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、及びローラと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ことを確認した。   As a compressor, in addition to a scroll compressor, a rotary compressor, a twin rotary compressor, a two-stage compression rotary compressor, and a swing compressor in which a roller and a vane are integrated have the same effect. It was confirmed that it was obtained.

本発明は、圧縮機及び空調装置に適用可能である。   The present invention is applicable to a compressor and an air conditioner.

1 室内機
2 室外機
3 圧縮機
4 四方弁
5 室内熱交換器
6 膨張装置
7 室外熱交換器
8 固定スクロール部材
9 端板
10 渦巻状ラップ
11 旋回スクロール部材
12 ラップ
13 クランクシャフト
14 圧縮室
15 吐出口
16 フレーム
17 圧力容器
18 吐出パイプ
19 電動モータ
20 滑り軸受け
21 油孔
22 油溜め部
1 indoor unit 2 outdoor unit 3 compressor 4 four-way valve 5 indoor heat exchanger 6 expansion device 7 outdoor heat exchanger 8 fixed scroll member 9 end plate 10 spiral wrap 11 orbiting scroll member 12 lap 13 crankshaft 14 compression chamber 15 discharge Outlet 16 Frame 17 Pressure vessel 18 Discharge pipe 19 Electric motor 20 Sliding bearing 21 Oil hole 22 Oil reservoir

Claims (4)

摺動部を有する圧縮室を備え、冷媒であるジフルオロメタンと、冷凍機油とを封入した圧縮機において、
前記冷凍機油は、化学式(1)で表される化合物(式中、R1〜R6は炭素数3〜8のアルキル基)と化学式(2)で表される化合物との混合物であり、前記化学式(2)で表される化合物を20モル%以上含み、40℃における動粘度が30〜90mm2/sのポリオールエステル油であり、
前記冷媒と前記ポリオールエステル油との低温側臨界溶解温度が+10℃以下であり、
前記ポリオールエステル油に40℃における動粘度が180mm2/sを超える圧縮部シール剤を前記ポリオールエステル油に対して1〜30重量%含むことを特徴とする圧縮機。
In a compressor provided with a compression chamber having a sliding portion and enclosing difluoromethane, which is a refrigerant, and refrigerating machine oil,
The refrigerating machine oil is a mixture of a compound represented by the chemical formula (1) (wherein R 1 to R 6 are alkyl groups having 3 to 8 carbon atoms) and a compound represented by the chemical formula (2), A polyol ester oil containing 20 mol% or more of the compound represented by the chemical formula (2) and having a kinematic viscosity at 40 ° C. of 30 to 90 mm 2 / s,
The low-temperature side critical dissolution temperature of the refrigerant and the polyol ester oil is + 10 ° C. or lower,
The compressor characterized in that the polyol ester oil contains 1 to 30% by weight of a compression sealant having a kinematic viscosity at 40 ° C. exceeding 180 mm 2 / s with respect to the polyol ester oil.
前記圧縮部シール剤は、下記化学式(3)で表される化合物(式中、R7、R8は、炭素数7〜8のアルキル基)又は化学式(4)で表わされる化合物(式中、R9、R10は炭素数3〜9のアルキル基。R11は炭素数1〜9のアルキル基。nは正数)又は数平均分子量が800〜4000のエチレン−α−オレフィン共重合体であることを特徴とする請求項1記載の圧縮機。
The compression part sealant is a compound represented by the following chemical formula (3) (wherein R 7 and R 8 are alkyl groups having 7 to 8 carbon atoms) or a compound represented by the chemical formula (4) (wherein R 9 and R 10 are alkyl groups having 3 to 9 carbon atoms, R 11 is an alkyl group having 1 to 9 carbon atoms, and n is a positive number) or an ethylene-α-olefin copolymer having a number average molecular weight of 800 to 4000. The compressor according to claim 1, wherein the compressor is provided.
前記圧縮室が旋回スクロール部材と固定スクロール部材とで形成され、40℃における動粘度が46〜90mm2/sであることを特徴とする請求項1記載の圧縮機。 The compressor according to claim 1, wherein the compression chamber is formed of an orbiting scroll member and a fixed scroll member, and has a kinematic viscosity at 40 ° C. of 46 to 90 mm 2 / s. 請求項1乃至3のいずれかに記載の圧縮機と、凝縮器と、膨張装置と、蒸発器とが配管で接続された空調装置。   An air conditioner in which the compressor according to any one of claims 1 to 3, a condenser, an expansion device, and an evaporator are connected by piping.
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