WO2016206246A1 - Base oil for refrigeration oil composition, refrigeration oil composition and composition for cooling - Google Patents

Base oil for refrigeration oil composition, refrigeration oil composition and composition for cooling Download PDF

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WO2016206246A1
WO2016206246A1 PCT/CN2015/092167 CN2015092167W WO2016206246A1 WO 2016206246 A1 WO2016206246 A1 WO 2016206246A1 CN 2015092167 W CN2015092167 W CN 2015092167W WO 2016206246 A1 WO2016206246 A1 WO 2016206246A1
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oil
base oil
composition
ester
acid
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PCT/CN2015/092167
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French (fr)
Chinese (zh)
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汪孟言
于谦
朱胜
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北京福润联石化科技开发有限公司
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Publication of WO2016206246A1 publication Critical patent/WO2016206246A1/en

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    • CCHEMISTRY; METALLURGY
    • 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
    • C10M105/02Well-defined hydrocarbons
    • C10M105/06Well-defined hydrocarbons aromatic
    • CCHEMISTRY; METALLURGY
    • 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
    • CCHEMISTRY; METALLURGY
    • 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
    • C10M111/00Lubrication compositions characterised by the base-material being a mixture of two or more compounds covered by more than one of the main groups C10M101/00 - C10M109/00, each of these compounds being essential
    • C10M111/02Lubrication compositions characterised by the base-material being a mixture of two or more compounds covered by more than one of the main groups C10M101/00 - C10M109/00, each of these compounds being essential at least one of them being a non-macromolecular organic compound
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Definitions

  • the present invention relates to the field of refrigeration oils, and in particular to a base oil and a refrigerating machine oil composition for a refrigerating machine oil composition and a composition for refrigerating.
  • the compression refrigeration system consists of a refrigeration compressor, a condenser, an expansion valve, an evaporator, etc.
  • the working principle is to absorb the heat of the surrounding medium when the refrigerant is vaporized and volatilized, to lower the temperature for cooling, and then to pass the refrigerant through the compressor. Revert to liquid, re-gasification, and so on.
  • This kind of refrigeration system is widely used in household appliances such as refrigerators and air conditioners, industrial equipment such as cold storage and cold storage rooms, and commercial equipment such as display cabinets, beverages, and ice cream machines.
  • the compressor is the heart of the above-mentioned compression refrigeration system, and the refrigeration oil that acts as lubrication, heat dissipation, sealing and anti-corrosion in the compressor has a very important influence on the performance and life of the compressor and the refrigeration system, so the performance is selected. Excellent refrigeration oil is very important for compression refrigeration systems.
  • CN 1099454 A discloses a hydrocarbon-containing refrigerator oil composition
  • a hydrocarbon oil as a base oil selected from at least one of a mineral oil, an olefin polymer, a naphthalene compound and an alkylbenzene.
  • the olefin polymer comprises a C 16 -C 20 alpha olefin oligomer, which comprises a Ziegler catalyst method, a radical polymerization method, an aluminum chloride method, a boron fluoride by using ethylene as a raw material.
  • a known polymerization method such as a method is obtained by oligomerization.
  • the ⁇ -olefin polymer obtained by this method generally has a viscosity at 40 ° C of more than 6 mm 2 /sec and is 6.5 to 8.0 mm 2 /sec, making it difficult to obtain a lower viscosity oil.
  • An object of the present invention is to provide a base oil and a refrigerating machine oil composition for a refrigerating machine oil composition and a composition for refrigerating to reduce the viscosity of the refrigerating machine oil while improving the viscosity-temperature characteristics thereof, thereby achieving energy saving and emission reduction.
  • a base oil for a refrigerating machine oil composition comprising an alkyl benzene oil and an ester oil, and the base oil has a kinematic viscosity at 120 ° C and a kinematic viscosity at 40 ° C
  • the ratio is 0.23-0.30.
  • a refrigerating machine oil composition comprising a base oil and an additive, wherein the base oil is a base oil for the above refrigerating machine oil composition.
  • composition for refrigeration comprising a refrigerating machine oil composition and a refrigerant, wherein the refrigerating machine oil composition is the above refrigerating machine oil composition.
  • the base oil and refrigerating machine oil composition for a refrigerating machine oil composition according to the above aspect of the present invention and the composition for refrigerating are advantageously obtained by using an alkyl benzene oil to obtain a base oil having a low viscosity and excellent overall performance, and at the same time, by using an alkyl group
  • the benzene oil is used in combination with the low viscosity and high viscosity index ester oil, and by adjusting the ratio of the kinematic viscosity of the base oil to 120 ° C and the kinematic viscosity at 40 ° C, the viscosity is not excessively formed as the temperature increases. Reduced base oil.
  • viscosity means “kinetic viscosity”
  • kinetic viscosity refers to the ratio of the dynamic viscosity of a fluid to the density of the fluid at the same temperature; in the present invention, it is based on the national standard GB/T 265-1988.
  • the kinematic viscosity measurement method is measured.
  • viscosity index refers to the extent to which the viscosity of all fluids varies with temperature. The higher the viscosity index, the smaller the viscosity of the fluid is affected by the temperature, and the less sensitive the viscosity is to temperature; in the present invention, it is measured according to the viscosity index calculation method of the petroleum product GB/T 1995-1998.
  • This phenomenon may occur because, as the viscosity of the refrigerating machine oil decreases, the oil film at the friction pair and the piston connecting rod becomes thinner, and the oil film is too thin to cause a decrease in sealing performance, which affects the cooling efficiency, resulting in a cooling efficiency that does not rise and fall. .
  • too low a thickness of the oil film may cause a decrease in boundary lubricity or even dry friction of the compressor components, resulting in damage to the compressor.
  • a base oil for a refrigerating machine oil composition contains an alkylbenzene oil and an ester oil, and the ratio of the kinematic viscosity at 120 ° C of the base oil to the kinematic viscosity at 40 ° C is 0.23-0.30.
  • the base oil for the above-mentioned refrigerating machine oil composition of the present invention is advantageous for obtaining a base oil having a low viscosity and excellent comprehensive performance by using an alkyl benzene oil, and at the same time by synergizing an alkyl benzene oil with a low viscosity, high viscosity index ester oil.
  • By using, and by adjusting the ratio of the obtained base oil 120 ° C kinematic viscosity to 40 ° C kinematic viscosity it is advantageous to form a base oil which does not excessively decrease in viscosity with an increase in temperature.
  • the content of the hydrocarbon refrigerant to be used in combination with the liquid refrigerant in the liquid phase may be lowered to some extent.
  • the content of the hydrocarbon refrigerant used in the gas phase which will increase the pressure of the hydrocarbon refrigeration system, which is beneficial to improve the efficiency of the refrigeration system (about 0.5% to 1%), which is beneficial to achieve The effect of energy saving.
  • the present invention adjusts the viscosity of the base oil by adjusting the ratio of the kinematic viscosity at 120 ° C to the kinematic viscosity at 40 ° C to effectively adjust the viscosity of the base oil, and the viscosity of the oil at 100 ° C is less than 2 mm 2 / After s, the viscosity index is difficult to get. While simplifying the detection steps of the base oil during the adjustment process, the base oil meeting the requirements of the present invention is more accurately described.
  • the object of the present invention can be achieved as long as the ratio of the base oil 120 ° C kinematic viscosity to the 40 ° C kinematic viscosity is in the range of 0.23 - 0.30.
  • the base oil has a kinematic viscosity at 40 ° C of 2-15 mm 2 /s, and the base oil has a kinematic viscosity of 120 ° C and a movement of 40 ° C.
  • the viscosity ratio is 0.24-0.29.
  • the base oil has a kinematic viscosity at 40 ° C of 3 to 7 mm 2 /s, and when the base oil has a kinematic viscosity at 40 ° C of 3 to 5 mm 2 /s, the ratio of the kinematic viscosity at 120 ° C to the kinematic viscosity at 40 ° C is 0.24 to 0.29; when the kinematic viscosity of the base oil at 40 ° C is more than 5 to less than or equal to 7 mm 2 /s, the ratio of the kinematic viscosity at 120 ° C to the kinematic viscosity at 40 ° C is 0.23 to 0.28.
  • the base oil contains both an alkylbenzene oil and an ester oil, and the above requirements are satisfied, there is no particular requirement for the amount of the alkylbenzene oil and the ester oil.
  • the content of the alkyl benzene oil is 40-80 wt.%
  • the content of the ester oil is 20-60 wt.%, based on the total amount of the above base oil, preferably an alkyl benzene oil.
  • the content is 40-75 wt.%
  • the content of the ester oil is 25-60 wt.%.
  • the inventors of the present invention have found that when the ester oil selected for the base oil has a viscosity in the range of 2 to 15 mm 2 /s and a viscosity index of more than 90, The viscosity-temperature characteristics of the refrigerating machine oil obtained using the base oil can be further improved. Accordingly, in the present invention, it is preferred that the above ester oil has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, more preferably 8 to 15 mm 2 /s, and the ester oil has a viscosity index of more than 90, more preferably more than 120.
  • the ester oils usable in the above base oils include, but are not limited to, C 6 -C 14 monohydric alcohol esters, C 8 -C 18 monobasic acid esters, C 4 -C 12 a monool ester, a C 4 -C 12 dibasic acid ester, a C 3 -C 6 polyhydric alcohol ester, a C 3 -C 6 polybasic acid ester, and a polyalkyleneoxy ether monoester having a specific structural formula and a polyalkylene oxide One or more of the ether diesters.
  • the above C 6 -C 14 monool ester refers to an ester synthesized from a monohydric alcohol having a total of 6-14 carbon atoms, including but not limited to a monohydric alcohol selected from the group consisting of isohexanol, isoheptanol, and isooctanol. , C 1 -C 6 acid esters of isodecyl alcohol, isodecyl alcohol and isotridecyl alcohol. Wherein the C 1 -C 6 acid is formic acid, acetic acid, propionic acid, butyric acid, valeric acid or caproic acid.
  • the above C 6 -C 14 monool esters include, but are not limited to, isotridecyl esters, isodecyl alcohol esters, isodecyl alcohol esters, isooctanol esters, isoheptyl esters, and isohexyl alcohol esters. One or more.
  • the above C 8 -C 18 monobasic acid ester refers to an ester synthesized from a monobasic acid having a total number of carbon atoms of 8-18, including but not limited to C 1 -C 8 positive of C 10 -C 18 monobasic fatty acid.
  • the or isomeric alcohol ester preferably includes, but is not limited to, a C 1 -C 8 normal or isomeric alcohol ester of a monobasic acid selected from the group consisting of citric acid, dodecanoic acid, myristic acid, palmitic acid or octadecanoic acid.
  • C 1 -C 8 normal or isomeric alcohols include, for example but are not limited to, methanol, ethanol, propanol, butanol, pentanol, hexanol, heptanol or octanol.
  • the above C 8 -C 18 monobasic acid ester includes, but is not limited to, di(2-ethylhexyl) dodecanoate, di(2-ethylhexyl) phthalate, methyl stearate.
  • the above C 4 -C 12 glycol ester refers to an ester synthesized from a glycol having a total number of carbon atoms of 4 to 12, which includes but is not limited to a glycol selected from its own diol and methyl hexane.
  • the above C 4 -C 12 glycol esters include, but are not limited to, 3-methyl-1,6-ethylene glycol di-n-octanoate, 1,10-nonanediol di(2- One or more of ethylhexyl)ester and hexanediol diisooctanoate.
  • the above C 4 -C 12 dibasic acid ester refers to a monoester and/or diester synthesized from a dibasic acid having a total number of carbon atoms of 4 to 12, which includes, but is not limited to, a dibasic acid selected from the group consisting of a C 4 -C 10 normal or isomeric alcohol ester of a diacid, adipic acid, pimelic acid, sebacic acid, sebacic acid or phthalic acid, wherein the C 4 -C 10 normal or isomeric alcohol, For example, including but not limited to, one or more of butanol, pentanol, hexanol, heptanol, octanol, decyl alcohol, and decyl alcohol; in a more preferred case, the above C 4 -C 12 dibasic acid ester includes But not limited to di-n-octyl adipate, di-n-octyl 3-methyladipate
  • the above C 3 -C 6 polyol ester is a monoester, diester and/or polyester synthesized from a polyol having a hydroxyl functional group of 3-6, including but not limited to a polyol selected from the group consisting of a C 4 -C 10 normal or isomeric acid ester of a triol, trimethylolpropane or pentaerythritol, wherein the C 4 -C 10 normal or isomeric acid, for example but not limited to butyric acid, valeric acid, One or more of acid, heptanoic acid, octanoic acid, citric acid, and citric acid.
  • the above C 6 -C 20 polyol esters include, but are not limited to, glycerol trihexanoate, pentaerythritol tetrahexanoate, trimethylolpropane trihexanoate, and trimethylolpropane One or more of valerate.
  • the above C 3 -C 6 polyacid ester is an ester synthesized from a polybasic acid having a carboxyl functional group of 3-6, including but not limited to a polybasic acid selected from the group consisting of trimellitic acid and pyromellitic acid.
  • C 4 -C 10 normal or isomeric alcohol esters, wherein C 4 -C 10 normal or isomeric alcohols include, but are not limited to, for example, butanol, pentanol, hexanol, heptanol, octanol, decyl alcohol or hydrazine alcohol.
  • the above polyalkoxy ether monoester is a polyalkyleneoxy ether monoester having the following structural formula,
  • n 1 is an integer in 0 or 1-3
  • n 2 is an integer in 1-3
  • R 1 is in C 4 H 9 -, C 5 H 11 , C 6 H 13 -, and C 7 H 15 -
  • the R 2 is one of C 11 H 23 -, C 6 H 13 -, C 7 H 15 -, C 8 H 17 -, C 9 H 19 - and C 10 H 21 -
  • the above polyalkoxy ether monoester has the following structural formula:
  • the above polyalkoxy ether diester is a polyalkyleneoxy glycol double having the following structural formula ester,
  • n is an integer in 1-3
  • R 3 and R 4 are each independently selected from the group consisting of C 6 H 13 -, C 7 H 15 -, C 8 H 17 -, C 19 H 19 - and C 10 H 21 - One kind.
  • the above polyalkoxy ether diester has the following structural formula:
  • the inventors of the present invention have found that when the above-mentioned alkylbenzene oil has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, the use of the alkylbenzene is contained.
  • the viscosity of the refrigerating machine oil obtained from the base oil of the oil is better in accordance with the application requirements. Accordingly, in the present invention, it is preferred that the above alkylbenzene oil has a viscosity in the range of 2 to 15 mm 2 /s, preferably 3 to 7 mm 2 /s.
  • the alkylbenzene oil usable in the above base oil includes, but is not limited to, an alkylbenzene oil having an alkyl group having 8 to 18 carbon atoms, and preferably, the above
  • the alkyl benzene oil is a single chain alkyl benzene oil including, but not limited to, mercaptobenzene, undecylbenzene, dodecylbenzene, tridecylbenzene, pentadecylbenzene, hexadecylbenzene One or two or a mixture of two or more.
  • the inventors of the present invention have found that when another hydrocarbon oil different from alkylbenzene oil is further added to the above base oil, further The viscosity of the base oil is lowered, and the compatibility with the hydrocarbon refrigerant is better, which is favorable for promoting the obtained refrigerator oil to have better low-temperature fluidity and lubricity and a lower friction coefficient, thereby being better.
  • the base oil there is no particular requirement for another hydrocarbon oil other than alkyl benzene oil to be added to the base oil and the amount thereof, as long as the addition of the other hydrocarbon oil different from the alkyl benzene oil , can still meet the ratio of the base oil 120 ° C kinematic viscosity and 40 ° C kinematic viscosity in the range of 0.23-0.30.
  • the other hydrocarbon oil different from the alkyl benzene oil has a 40 ° C kinematic viscosity of 4 mm 2 /s or less, a pour point of less than -30 ° C, and a boiling point of less than 280 ° C.
  • the content of another hydrocarbon oil different from the alkylbenzene oil is from 0.1 to 20% by weight based on the total amount of the above base oil.
  • the content of the alkylbenzene oil is 40-74.9 wt.%
  • the content of the ester oil is 25-60 wt.%
  • the other is different from the alkylbenzene oil based on the total amount of the above base oil.
  • the hydrocarbon oil is present in an amount of from 0.1 to 20% by weight. More preferably, the content of another hydrocarbon oil different from the alkylbenzene oil is from 5 to 10% by weight based on the total amount of the above base oil.
  • hydrocarbon oil other than the alkyl benzene oil that meets the above requirements to obtain the base oil of the present invention.
  • another hydrocarbon oil different from alkyl benzene oil which may be used in the above base oil includes, but is not limited to, Fischer-Tropsch synthesized isoparaffins, hydroisomerized alkanes, One or more of hydrocracking isoparaffins, polyalphaolefins, olefin stacking oils, polyalkylcyclopentanes, polyalkylcyclohexanes.
  • These optional hydrocarbon oils may be any commercially available products or synthetic or by-products of any petrochemical, coal chemical and other chemical processes, as long as they are tested or treated to meet a 40 ° C kinematic viscosity of 4 mm 2 /s.
  • the pour point is less than -30 ° C
  • the boiling point is less than 280 ° C, which can be used as an active ingredient of the base oil for the refrigerating machine oil composition of the present invention.
  • the present invention also provides a refrigerating machine oil composition comprising a base oil and an additive, wherein the base oil is a base oil for the above refrigerating machine oil composition.
  • the refrigerating machine oil composition provided by the present invention, in the refrigerating machine oil composition, by adding an additive to the base oil, the ratio of the 120 ° C kinematic viscosity of the base oil to the 40 ° C kinematic viscosity is slightly changed, in the present invention.
  • the ratio of the 120 ° C kinematic viscosity of the refrigerator oil composition to the 40 ° C kinematic viscosity is from 0.23 to 0.30, more preferably from 0.24 to 0.29.
  • the ratio of the 120 ° C kinematic viscosity of the refrigerating machine oil composition to the 40 ° C kinematic viscosity is controlled within this range, which is advantageous in improving the viscosity-temperature characteristics of the oil by lowering the low-temperature viscosity of the oil (low viscosity tendency). Increase the thickness of the oil film at high temperature, improve the boundary lubrication and sealing, and thus improve the COP value of the refrigeration efficiency of the compressor, and finally achieve the purpose of energy saving and environmental protection.
  • the oil composition has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, preferably 3 to 7 mm 2 /s, a flash point of more than 140 ° C, and a flash point of more than 150. °C, the pour point is less than -50 ° C; in another preferred case, the above-mentioned refrigerator oil composition is based on the total amount of the composition, the base oil content is 94-98 wt.%, and the content of the additive is 2-6wt.%.
  • the preparation of the refrigerating machine oil composition of the present invention is not particularly required, and if the refrigerating machine oil composition of the present invention is mixed with a base oil and an additive, the base oil for the refrigerating machine oil composition may be obtained first, and then mixed with the additive, or directly The components constituting the refrigerator oil composition with the base oil are directly mixed with the additive to obtain a refrigerating machine oil composition, which is not particularly required in the present invention.
  • the above additive is selected from one or more of a lubricant, an antifriction agent, an antioxidant, an anticorrosive agent, and an antifoaming agent.
  • the above additives and their contents may be various conventional additives for refrigerating machine oil compositions and their conventional contents.
  • the above additives may be a lubricant for improving the lubricating properties of the refrigerating machine oil, an antifriction agent for improving the antifriction property, and an antioxidant, an anticorrosive agent, an antifoaming agent and the like for improving the thermal oxidation stability.
  • the above lubricant may be a phosphate ester lubricant commonly used in the art, such as tricresyl phosphate, triphenyl phosphate, octyl diphenyl phosphate, benzyl diphenyl phosphate, phenyl phosphorothioate. One or more of them.
  • the lubricant may be included in an amount of from 0 to 6.0% by weight, based on the total amount of the composition, preferably from 1.0 to 3.5% by weight.
  • the antifriction agent may be one or more of long-chain fatty acids, long-chain fatty alcohols, long-chain fatty esters, amides, phosphonates and commercially available energy-saving antifriction agents which are generally used in the art, and may specifically be oils. Acid, dimerized linoleic acid, dodecyl alcohol, butyl stearate, ethylene glycol oleate, oleic acid amide, benzotriazole dodecylamine, etc., diisooctylphosphonate and eutectic ball One or more of them.
  • the antifriction agent may be included in an amount of from 0 to 0.8% by weight, preferably from 0.02 to 0.6% by weight, based on the total amount of the composition.
  • the above antioxidants may be various phenolic antioxidants commonly used in the art, such as 2,6-di-tert-butyl-p-cresol, 2,3-di-tert-butyl-4-cresol, 2,6-di One or more of tert-butylphenol, 4,4'-tetramethylbis(2,6-di-tert-butylphenol), hydroquinone, and ⁇ -naphthol.
  • the antioxidant may be included in an amount of from 0 to 3% by weight, preferably from 0.2 to 0.8% by weight, based on the total amount of the composition.
  • the above anticorrosive agent may be a benzotriazole derivative and a thiadiazole derivative anticorrosive agent commonly used in the art, such as N,N-dialkylaminomethylene benzotriazole, 2,5-dimercapto-1,3 One or more of a 4-thiadiazole derivative, a dimercapto-benzothiadiazole, and a sodium dimercaptothiadiazole.
  • the anticorrosive agent may be included in an amount of from 0 to 0.1% by weight, preferably from 0.02 to 0.05% by weight, based on the total amount of the composition.
  • the antifoaming agent may be an antifoaming agent generally used in the art, such as one or more of a dimethicone, a homopolymer or a copolymer of an acrylate.
  • the antifoaming agent may be included in an amount of from 0 to 0.01% by weight, preferably from 0.001 to 0.005% by weight, based on the total amount of the composition.
  • the present invention also provides a composition for refrigeration, the composition comprising a refrigerating machine oil composition and a refrigerant, wherein the refrigerating machine oil composition is the above refrigerating machine oil composition.
  • the refrigerant may be any refrigerant known to those skilled in the art.
  • the refrigerant is a hydrocarbon refrigerant such as R600A or R290 or R134A.
  • the composition of the refrigerator oil composition is 70-90 wt.%, more preferably 75-90 wt.%, and the content of the refrigerant is 10-30 wt.%, more preferably in the composition. It is 10-25wt.%.
  • the present invention also provides a method of refrigeration, comprising: mixing or recombining a refrigerating machine oil composition and a refrigerant into a compressor of a refrigerating device for compression, wherein the refrigerating machine
  • the oil composition is the above-described refrigerating machine oil composition; the refrigerating machine oil composition is added in an amount of 70-90 wt.%, more preferably 75-90 wt.%, based on the total amount of the refrigerating machine oil composition and the refrigerant.
  • the amount of the refrigerant to be added is 10 to 30 wt.%, more preferably 10 to 25 wt.%.
  • the refrigerating machine oil composition may be added after being mixed, and the components constituting the refrigerating machine oil composition may be directly added, which is not particularly required in the present invention.
  • the refrigerator oil composition is used in an amount of 0.2 to 0.5 kg with respect to a cooling capacity of 3.5 kW.
  • the invention is further illustrated by the following examples.
  • the following Examples 1-10 are used to illustrate the base oil, the refrigerator oil composition for a refrigerating machine oil composition provided by the present invention, and a preparation method thereof.
  • Alkyl benzene oil commercially available from Pt. Unggul Indah Cahaya Tbk. (Indonesian company) alkyl benzene oil (which includes 10% by weight of decyl benzene, 25% by weight of undecyl benzene, and 35% by weight of twelve An alkylbenzene and 30% tridecylbenzene having a kinematic viscosity at 40 ° C of 4.2 mm 2 /s) in an amount of 35 parts by weight;
  • Ester oil di-n-octyl 3-methyladipate (kinematic viscosity at 40 ° C is 8.38 mm 2 / s, viscosity index is 170), the amount is 45 parts by weight;
  • Fischer-Tropsch synthesized isoparaffin produced by the SHELL company (indirect coal liquefaction) in the Netherlands (the main component of which is isoparaffin, 40 ° C kinematic viscosity is 2.8 mm 2 / s, pour point is -32 ° C, boiling point is 270 ⁇ 280 ° C), and the amount is 5 parts by weight.
  • the above-mentioned refrigerator oil composition is used with a base oil and 0.1 part by weight of 2,6-di-tert-butyl-p-cresol, 3 Parts by weight of tricresyl phosphate, 0.2 parts by weight of ethylene oleate and 0.03 parts by weight of N,N-dialkylaminomethylene benzenetriazole were uniformly mixed and formulated into a refrigerating machine oil composition, which was designated as S1.
  • Alkyl benzene oil commercially available from Tianjin Haote Chemical Co., Ltd., the main raw material is alkyl benzene oil of dodecyl benzene (the kinematic viscosity at 40 ° C is 4.2 mm 2 / s), the amount is 60 parts by weight;
  • Ester oil 1,10-nonanediol di(2-ethylhexyl) ester (kinetic viscosity at 40 ° C of 12.1 mm 2 / s, viscosity index of 133), the amount is 30 parts by weight;
  • Another hydrocarbon oil different from alkyl benzene oil Hydroisomerized alkane produced by the hydroisomerization process of YOUGONG (Korea) Co., Ltd. (the main component of which is isoparaffin, 40 ° C kinematic viscosity is 3.2 mm 2 /s The pour point is -38 ° C, the boiling point is 270 to 280 ° C), and the amount is 10 parts by weight.
  • the foregoing refrigerator oil composition is used with a base oil and 0.2 parts by weight of 2,6-di-tert-butyl-p-cresol, 3.5 parts by weight of tricresyl phosphate, 0.18 parts by weight of ethylene oleate, and 0.04 parts by weight of N,N.
  • - Dialkylaminomethylene benzotriazole was uniformly mixed and formulated into a refrigerating machine oil composition, which was designated as S2.
  • Alkyl benzene oil commercially available from Korea's dominant company, the main raw material is dodecylbenzene alkyl benzene oil (40 ° C kinematic viscosity of 3.8 mm 2 / s), the amount of 50 parts by weight;
  • Ester oil glycerol trihexanoate (kinematic viscosity at 40 ° C is 8.93 mm 2 / s, viscosity index is 170), the amount is 40 parts by weight;
  • hydrocarbon oil different from alkyl benzene oil polyalphaolefin produced by Mobil (USA) (the main component of which is isoparaffin, having a kinematic viscosity at 40 ° C of 3.2 mm 2 /s and a pour point of -60 ° C, The boiling point is 270 to 280 ° C), and the amount is 10 parts by weight.
  • the foregoing refrigerator oil composition is used with a base oil and 0.5 parts by weight of 2,6-di-tert-butyl-p-cresol, 5 parts by weight of tricresyl phosphate, 0.2 parts by weight of ethylene oleate, and 0.05 parts by weight of N,N.
  • - Dialkylaminomethylene benzotriazole was uniformly mixed and formulated into a refrigerating machine oil composition, designated as S3.
  • Alkyl benzene oil same as in Example 1, the amount is 60 parts by weight;
  • Ester oil same as in Example 1, the amount is 40 parts by weight;
  • the refrigerating machine oil composition prepared in the step (2) of the embodiment 6 was replaced with a base oil in the base oil of the refrigerating machine oil composition prepared in the step (2) of the first embodiment, and was formulated into a refrigerating machine oil composition.
  • S4 the refrigerating machine oil composition prepared in the step (2) of the embodiment 6 was replaced with a base oil in the base oil of the refrigerating machine oil composition prepared in the step (2) of the first embodiment, and was formulated into a refrigerating machine oil composition.
  • alkylbenzenes are all alkylbenzene oils commercially available from Pt. Unggul Indah Cahaya Tbk. (Indonesia).
  • the refrigerating machine oil composition prepared in the step (2) of the embodiment 5-10 was replaced with a base oil to replace the refrigerating machine oil composition prepared in the step (2) of the first embodiment with a base oil, and was formulated into a refrigerating machine oil combination.
  • the record is S5-S10.
  • Alkyl benzene oil same as in Example 1, the amount is 100 parts by weight;
  • Refrigerator oil composition and preparation method thereof Referring to Example 1, the refrigerator oil composition prepared in the step (1) of Comparative Example 1 was replaced with the base oil to replace the refrigerator oil composition prepared in the step (1) of Example 1. The base oil was used to prepare a refrigerating machine oil composition as D1.
  • Alkyl benzene oil commercially available from Pt. Unggul Indah Cahaya Tbk. (Indonesian company) alkyl benzene oil (ingredients including 55 wt% of tridecyl benzene, 25 wt% of tetradecyl benzene and 20 wt% of ten Pentaalkylbenzene has a kinematic viscosity at 40 ° C of 5.21 mm 2 /s) in an amount of 100 parts by weight.
  • Refrigerating machine oil composition and preparation method thereof Referring to Example 1, the refrigerating machine oil composition prepared in the step (1) of Comparative Example 2 was replaced with the base oil to replace the refrigerating machine oil composition prepared in the step (1) of Example 1. The base oil was used to prepare a refrigerating machine oil composition as D2.
  • Raw material and amount of base oil for refrigerating machine oil composition Refer to Comparative Example 1, except that it does not contain alkyl benzene oil, and the amount of the ester oil is 50 parts by weight, which is different from the alkyl benzene oil.
  • a hydrocarbon oil is used in an amount of 50 parts by weight.
  • Refrigerator oil composition and preparation method thereof Referring to Example 1, the composition of the refrigerator oil was designated as D3.
  • D4 hydrocarbon-based refrigerating machine oil CS1 (trade name: suniso1GS Aj sun oil Co.) using R600A as a refrigerant is referred to as D4.
  • the hydrocarbon refrigeration oil K7P which has been promoted on the market with R600A as refrigerant, is recorded as D5.
  • the 120 ° C kinematic viscosity of "Example 1" is equal to "120 ° C kinematic viscosity of Comparative Example 2; the 120 ° C kinematic viscosity of "Example 7" is higher than the “Comparative Example 1" of 120 ° C Kinematic viscosity; it can be seen that by selecting an appropriate alkyl benzene oil and an ester oil, and reasonably adjusting the ratio of the two, the ratio of the viscosity of the base oil at 120 ° C to the viscosity at 40 ° C meets the requirements of the present invention, and the present invention can be improved. Claim The viscosity-temperature characteristics of the protected base oil.
  • Examples 11-20 are used to illustrate the compositions for refrigeration provided by the present invention.
  • compositions T1-T10 for refrigeration are shown in Table 4.
  • compositions E1-E5 for refrigeration.
  • the composition of the compositions E1-E5 used for refrigeration is shown in Table 4.
  • Test method 27 g (about 300 mL) of each sample of the refrigerating machine oil composition prepared in Examples 1-10 and Comparative Examples 1-5 was injected into a refrigerator compressor (PZ89DIY-4DV), and 30 g of R600A was used as a refrigerant. Performance tests were performed on the compressor performance test bench.
  • Wear spot diameter according to GB/T3142 (30kg, 30min, 1200 rpm, room temperature);
  • COP value refrigeration efficiency: The ratio of the amount of cooling (heat) to the input power that can be achieved by the heat pump system; and the energy saving effect (energy saving rate) is derived from the COP value.
  • the energy saving rate is the percentage increase of COP based on the value of solar oil SUNISO 1GSAJ.
  • the refrigerator oil composition provided by the present invention has excellent compatibility with the R600A refrigerant and thermochemical stability, and has excellent viscosity temperature characteristics, a high flash point, Excellent low temperature fluidity, good lubricity and low coefficient of friction show significant energy savings.
  • the base oil for the above-mentioned refrigerator oil composition of the present invention is advantageous in obtaining a base oil having a lower viscosity by using an alkylbenzene oil, and at the same time, by using an alkylbenzene oil in combination with a low viscosity, high viscosity index ester oil,
  • By adjusting the ratio of the viscosity of the base oil at 120 ° C to the viscosity at 40 ° C it is advantageous to form a base oil whose viscosity does not excessively decrease as the temperature increases.
  • By increasing its viscosity-temperature characteristics it increases the thickness of the oil film at high temperatures, improves the boundary lubricity and sealing performance, and further improves the refrigeration efficiency of the compressor, ultimately achieving the goal of further energy saving and environmental protection.

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Abstract

A base oil for a refrigeration oil composition and refrigeration oil composition. The base oil comprises an alkylbenzene oil and an ester oil. The ratio of the 120˚C kinetic viscosity of the base oil to the 40˚C kinetic viscosity thereof is 0.23-0.30. A base oil having a viscosity overly decreasing with the increase of the temperature is formed by combining an alkylbenzene oil and an ester oil having a low viscosity and high viscosity index for use and adjusting the ratio of the 120˚C kinetic viscosity of the base oil to the 40˚C kinetic viscosity thereof.

Description

冷冻机油组合物用基础油和冷冻机油组合物及用于制冷的组合物Base oil and refrigerating machine oil composition for refrigerating machine oil composition and composition for refrigeration 技术领域Technical field
本发明涉及制冷用机油领域,具体地,涉及一种冷冻机油组合物用基础油和冷冻机油组合物及用于制冷的组合物。The present invention relates to the field of refrigeration oils, and in particular to a base oil and a refrigerating machine oil composition for a refrigerating machine oil composition and a composition for refrigerating.
背景技术Background technique
压缩式制冷系统由制冷压缩机、冷凝器、膨胀阀、蒸发器等构成,工作原理是利用制冷剂气化挥发时,吸收周围介质的热量,使温度降低进行冷却,然后通过压缩机将制冷剂复原为液体,再重新气化,如此循环往复。这种制冷系统大量用于冰箱、空调等家用电器,冷库、冷藏室等工业设备和陈列柜、饮料、冰淇淋机等商用设备。压缩机是上述压缩式制冷系统的心脏,而在压缩机内起润滑、散热、密封和防腐等作用的冷冻机油则对压缩机和制冷系统的性能发挥及寿命有着十分重要的影响,因此选择性能优异的冷冻机油对压缩制冷系统来说是十分重要的。The compression refrigeration system consists of a refrigeration compressor, a condenser, an expansion valve, an evaporator, etc. The working principle is to absorb the heat of the surrounding medium when the refrigerant is vaporized and volatilized, to lower the temperature for cooling, and then to pass the refrigerant through the compressor. Revert to liquid, re-gasification, and so on. This kind of refrigeration system is widely used in household appliances such as refrigerators and air conditioners, industrial equipment such as cold storage and cold storage rooms, and commercial equipment such as display cabinets, beverages, and ice cream machines. The compressor is the heart of the above-mentioned compression refrigeration system, and the refrigeration oil that acts as lubrication, heat dissipation, sealing and anti-corrosion in the compressor has a very important influence on the performance and life of the compressor and the refrigeration system, so the performance is selected. Excellent refrigeration oil is very important for compression refrigeration systems.
随着我国环境问题日益突出,保护环境成为各行各业所面临的重要问题。对于采用这种压缩式制冷系统的家电行业而言,实现节能减排是其保护环境的一种重要手段。为了实现节能减排的目的,本领域技术人员往往通过选择粘度较低,且与制冷剂相容性较好的冷冻机油,以实现减摩,节能的目的。As China's environmental problems become more and more prominent, protecting the environment has become an important issue facing all walks of life. For the home appliance industry using this compression refrigeration system, achieving energy conservation and emission reduction is an important means of protecting the environment. In order to achieve the purpose of energy saving and emission reduction, those skilled in the art often achieve the purpose of reducing friction and saving energy by selecting a refrigerating machine oil having a lower viscosity and better compatibility with a refrigerant.
CN 1099454A公开了一种含烃冷冻机油组合物,该组合物含有烃类油作为基础油,所述烃类油选自矿油、烯烃聚合物、萘化合物和烷基苯中的至少一种。所述烯烃聚合物包括C16-C20的α烯烃低聚物,所述α烯烃低聚物通过以乙烯为原料采用齐格勒催化剂法、自由基聚合法、氯化铝法、氟化硼法等公知的聚合方法齐聚得到。采用这种方法获得的α烯烃聚合物在40℃时的粘度一般大于6平方毫米/秒,为6.5-8.0平方毫米/秒,难以得到更低粘度的 油品。CN 1099454 A discloses a hydrocarbon-containing refrigerator oil composition comprising a hydrocarbon oil as a base oil selected from at least one of a mineral oil, an olefin polymer, a naphthalene compound and an alkylbenzene. The olefin polymer comprises a C 16 -C 20 alpha olefin oligomer, which comprises a Ziegler catalyst method, a radical polymerization method, an aluminum chloride method, a boron fluoride by using ethylene as a raw material. A known polymerization method such as a method is obtained by oligomerization. The α-olefin polymer obtained by this method generally has a viscosity at 40 ° C of more than 6 mm 2 /sec and is 6.5 to 8.0 mm 2 /sec, making it difficult to obtain a lower viscosity oil.
一般地,冷冻机油的粘度越低、低温流动性越好,节能效果就越好。因此,为了实现节能减排的目的,有人试图用环烷基矿油切割适宜的馏分生产低粘度冷冻机油。尽管这种油品在40℃的粘度能达到5平方毫米/秒的低粘度,然而这种油品的闪点、燃点太低,安全性差,难以达到制冷压缩机对冷冻机油最低闪点(大于140℃)的要求,再加上这种油品的馏分宽、挥发性大,容易在压缩机中发生携油问题。Generally, the lower the viscosity of the refrigerating machine oil, the better the low-temperature fluidity, and the better the energy saving effect. Therefore, in order to achieve energy saving and emission reduction, some people have tried to produce a low-viscosity refrigeration oil by cutting a suitable fraction with naphthenic mineral oil. Although the viscosity of this oil can reach a low viscosity of 5 mm 2 / sec at 40 ° C, the flash point and ignition point of this oil are too low, and the safety is poor. It is difficult to reach the minimum flash point of the refrigeration compressor to the refrigerating machine oil (greater than The requirement of 140 ° C), together with the wide fraction and high volatility of this oil, makes it easy to carry oil in the compressor.
而且,对于冷冻机油而言,也并非粘度越低,低温流动性越好,节能效果就越好。很多情况下,即便选择了粘度较低,且低温流动性较好的冷冻机油组合物,还是会出现制冷效率不升反降的情况。由此可见,在选择冷冻机油的过程中,不能仅考虑低温(100℃及以下)时冷冻机油粘度,还需要考虑进一步优化冷冻机油的使用性能。Moreover, for refrigerating machine oil, the lower the viscosity, the better the low-temperature fluidity, and the better the energy saving effect. In many cases, even if a refrigerating machine oil composition having a low viscosity and a good low-temperature fluidity is selected, there is a case where the cooling efficiency does not rise and fall. It can be seen that in the process of selecting the refrigerating machine oil, it is not only possible to consider the viscosity of the refrigerating machine oil at a low temperature (100 ° C or less), and further to optimize the performance of the refrigerating machine oil.
总之,目前市场上还没有节能效果十分理想的低粘度冷冻机油供使用。因此,迫切需要开发一种能够进一步提高节能率的低粘度冷冻机油组合物产品。In short, there is currently no low-viscosity refrigeration oil that is ideal for energy saving. Therefore, there is an urgent need to develop a low viscosity refrigerator oil composition product capable of further increasing the energy saving rate.
发明内容Summary of the invention
本发明的目的是提供一种冷冻机油组合物用基础油和冷冻机油组合物及用于制冷的组合物,以在降低冷冻机油低温粘度的同时,提高其粘温特性,进而实现节能减排,保护环境的目的。An object of the present invention is to provide a base oil and a refrigerating machine oil composition for a refrigerating machine oil composition and a composition for refrigerating to reduce the viscosity of the refrigerating machine oil while improving the viscosity-temperature characteristics thereof, thereby achieving energy saving and emission reduction. The purpose of protecting the environment.
为了实现上述目的,在本发明的一个方面,提供一种冷冻机油组合物用基础油,该基础油含有烷基苯油和酯类油,且该基础油120℃运动粘度与40℃运动粘度的比值为0.23-0.30。In order to achieve the above object, in one aspect of the invention, there is provided a base oil for a refrigerating machine oil composition, the base oil comprising an alkyl benzene oil and an ester oil, and the base oil has a kinematic viscosity at 120 ° C and a kinematic viscosity at 40 ° C The ratio is 0.23-0.30.
在本发明的另一个方面,提供了一种冷冻机油组合物,该组合物含有基础油和添加剂,其中,基础油为上述冷冻机油组合物用基础油。 In another aspect of the invention, there is provided a refrigerating machine oil composition comprising a base oil and an additive, wherein the base oil is a base oil for the above refrigerating machine oil composition.
在本发明的再一个方面,提供了一种用于制冷的组合物,该组合物包括冷冻机油组合物和制冷剂,其中,冷冻机油组合物为上述冷冻机油组合物。In still another aspect of the present invention, there is provided a composition for refrigeration, the composition comprising a refrigerating machine oil composition and a refrigerant, wherein the refrigerating machine oil composition is the above refrigerating machine oil composition.
本发明上述技术方案的冷冻机油组合物用基础油和冷冻机油组合物及用于制冷的组合物,通过使用烷基苯油有利于获得粘度较低综合性能优异的基础油,同时通过将烷基苯油与低粘度、高粘度指数的酯类油协同使用,并通过调整所得到的基础油120℃运动粘度与40℃运动粘度的比值,有利于形成随着温度的升高,粘度不会过分降低的基础油。进而在保证油品低温粘度较低的情况下(低粘度趋势下),通过提高其粘温特性,以增加高温下油膜的厚度,提高边界润滑性和密封性,进而提高压缩机制冷效率COP值,最终达到节能减排,保护环境的目的。The base oil and refrigerating machine oil composition for a refrigerating machine oil composition according to the above aspect of the present invention and the composition for refrigerating are advantageously obtained by using an alkyl benzene oil to obtain a base oil having a low viscosity and excellent overall performance, and at the same time, by using an alkyl group The benzene oil is used in combination with the low viscosity and high viscosity index ester oil, and by adjusting the ratio of the kinematic viscosity of the base oil to 120 ° C and the kinematic viscosity at 40 ° C, the viscosity is not excessively formed as the temperature increases. Reduced base oil. Further, in the case of ensuring low oil viscosity at low temperature (under low viscosity tendency), by increasing the viscosity-temperature characteristics, the thickness of the oil film at a high temperature is increased, the boundary lubricity and sealing property are improved, and the COP value of the compressor refrigeration efficiency is further improved. In the end, it will achieve the goal of energy saving and environmental protection.
本发明的其它特征和优点将在随后的具体实施方式部分予以详细说明。Other features and advantages of the invention will be described in detail in the detailed description which follows.
具体实施方式detailed description
以下对本发明的具体实施方式进行详细说明。应当理解的是,此处所描述的具体实施方式仅用于说明和解释本发明,并不用于限制本发明。Specific embodiments of the present invention will be described in detail below. It is to be understood that the specific embodiments described herein are merely illustrative and not restrictive.
在本发明中术语“粘度”均是指“运动粘度”,“运动粘度”是指流体的动力粘度与同温度下该流体密度之比;在本发明中其是根据国标GB/T 265-1988运动粘度测量方法进行测量的。术语“粘度指数”是指一切流体粘度随温度变化的程度。粘度指数越高,表示流体粘度受温度的影响越小,粘度对温度越不敏感;在本发明中其是根据国标号GB/T 1995-1998石油产品粘度指数计算方法进行测量的。In the present invention, the term "viscosity" means "kinetic viscosity", and "kinetic viscosity" refers to the ratio of the dynamic viscosity of a fluid to the density of the fluid at the same temperature; in the present invention, it is based on the national standard GB/T 265-1988. The kinematic viscosity measurement method is measured. The term "viscosity index" refers to the extent to which the viscosity of all fluids varies with temperature. The higher the viscosity index, the smaller the viscosity of the fluid is affected by the temperature, and the less sensitive the viscosity is to temperature; in the present invention, it is measured according to the viscosity index calculation method of the petroleum product GB/T 1995-1998.
正如背景技术部分所介绍的,目前市场上还没有节能效果十分理想的低粘度冷冻机油供使用。因此,迫切需要开发一种能够进一步提高节能率的低粘度冷冻机油组合物产品。针对于这一现状,本发明的发明人进行了大量的研究实验。在一次偶然的机会,发明人发现对于冷冻机油而言,也并非粘度 越低,低温流动性越好,节能效果就越好。在压缩机的某些部位,例如摩擦副和活塞连杆等处,使用温度往往会高达120℃,随着温度的升高,冷冻机油的粘度会随之变低,此时压缩机的能耗不但并未变低,反而还有升高的趋势。这种现象的产生可能是因为,随着冷冻机油粘度的降低,摩擦副和活塞连杆等处的油膜会变薄,油膜过薄造成密封性下降,影响制冷效率,导致制冷效率不升反降。此外,油膜厚度过低还会造成边界润滑性降低甚至压缩机部件干摩擦,从而造成压缩机损坏。As described in the background section, there is currently no low-viscosity refrigeration oil that is ideal for energy savings. Therefore, there is an urgent need to develop a low viscosity refrigerator oil composition product capable of further increasing the energy saving rate. In response to this situation, the inventors of the present invention conducted a large number of research experiments. At an accidental opportunity, the inventors found that it is not a viscosity for refrigerating machine oil. The lower the lower the low temperature fluidity, the better the energy saving effect. In some parts of the compressor, such as friction pairs and piston rods, the temperature is often as high as 120 ° C. As the temperature increases, the viscosity of the refrigeration oil will become lower. Not only has it not become lower, but there has been an upward trend. This phenomenon may occur because, as the viscosity of the refrigerating machine oil decreases, the oil film at the friction pair and the piston connecting rod becomes thinner, and the oil film is too thin to cause a decrease in sealing performance, which affects the cooling efficiency, resulting in a cooling efficiency that does not rise and fall. . In addition, too low a thickness of the oil film may cause a decrease in boundary lubricity or even dry friction of the compressor components, resulting in damage to the compressor.
为此,本发明的发明人在研发冷冻机油的过程中,在考虑低温(100℃及以下)时冷冻机油粘度的同时,还进一步考虑了高温(100℃以上)时冷冻机油的粘度,提出了一种冷冻机油组合物用基础油。该基础油含有烷基苯油和酯类油,且基础油120℃运动粘度与40℃运动粘度的比值为0.23-0.30。For this reason, in the process of developing the refrigerating machine oil, the inventors of the present invention have considered the viscosity of the refrigerating machine oil at a low temperature (100 ° C or lower), and further considered the viscosity of the refrigerating machine oil at a high temperature (above 100 ° C). A base oil for a refrigerating machine oil composition. The base oil contains an alkylbenzene oil and an ester oil, and the ratio of the kinematic viscosity at 120 ° C of the base oil to the kinematic viscosity at 40 ° C is 0.23-0.30.
本发明上述冷冻机油组合物用基础油,通过使用烷基苯油有利于获得粘度较低且综合性能优异的基础油,同时通过将烷基苯油与低粘度、高粘度指数的酯类油协同使用,并通过调整所得到的基础油120℃运动粘度与40℃运动粘度的比值,有利于形成随着温度的升高,粘度不会过分降低的基础油。进而在保证油品低温粘度较低的情况下(低粘度趋势下),通过提高其粘温特性,以增加高温下油膜的厚度,提高边界润滑性和密封性,进而提高压缩机制冷效率COP值,最终达到节能减排,保护环境的目的。The base oil for the above-mentioned refrigerating machine oil composition of the present invention is advantageous for obtaining a base oil having a low viscosity and excellent comprehensive performance by using an alkyl benzene oil, and at the same time by synergizing an alkyl benzene oil with a low viscosity, high viscosity index ester oil. By using, and by adjusting the ratio of the obtained base oil 120 ° C kinematic viscosity to 40 ° C kinematic viscosity, it is advantageous to form a base oil which does not excessively decrease in viscosity with an increase in temperature. Further, in the case of ensuring low oil viscosity at low temperature (under low viscosity tendency), by increasing the viscosity-temperature characteristics, the thickness of the oil film at a high temperature is increased, the boundary lubricity and sealing property are improved, and the COP value of the compressor refrigeration efficiency is further improved. In the end, it will achieve the goal of energy saving and environmental protection.
同时,在本发明上述冷冻机油组合物用基础油中通过加入的极性成分(酯类油),可能会在一定程度上降低与其配合使用的烃类制冷剂在液相中的含量,增加与其配合使用的烃类制冷剂在气相中的含量,这样将有可能提高烃类制冷系统的压力,这种压力的提高有利于提高制冷系统的效率(大约0.5%-1%),进而有利于达到节能的效果。Meanwhile, in the base oil for the above-mentioned refrigerating machine oil composition of the present invention, by adding a polar component (ester oil), the content of the hydrocarbon refrigerant to be used in combination with the liquid refrigerant in the liquid phase may be lowered to some extent. The content of the hydrocarbon refrigerant used in the gas phase, which will increase the pressure of the hydrocarbon refrigeration system, which is beneficial to improve the efficiency of the refrigeration system (about 0.5% to 1%), which is beneficial to achieve The effect of energy saving.
另外,本发明通过调整基础油120℃运动粘度与40℃运动粘度的比值,以调整基础油的粘温特性,能够有效地避开高温情况下,油品的100℃运动 粘度低于2mm2/s之后,粘度指数难以得到的问题。在简化基础油在调整过程中的检测步骤的同时,更准确的描述符合本发明要求的基础油。In addition, the present invention adjusts the viscosity of the base oil by adjusting the ratio of the kinematic viscosity at 120 ° C to the kinematic viscosity at 40 ° C to effectively adjust the viscosity of the base oil, and the viscosity of the oil at 100 ° C is less than 2 mm 2 / After s, the viscosity index is difficult to get. While simplifying the detection steps of the base oil during the adjustment process, the base oil meeting the requirements of the present invention is more accurately described.
根据本发明,只要基础油120℃运动粘度与40℃运动粘度的比值在0.23-0.30范围内即可实现本发明的目的。然而,为了进一步优化本发明基础油的粘温特性,在一种优选情况下,上述基础油的40℃运动粘度为2-15mm2/s,且所述基础油120℃运动粘度与40℃运动粘度的比值为0.24-0.29。According to the present invention, the object of the present invention can be achieved as long as the ratio of the base oil 120 ° C kinematic viscosity to the 40 ° C kinematic viscosity is in the range of 0.23 - 0.30. However, in order to further optimize the viscosity-temperature characteristics of the base oil of the present invention, in a preferred case, the base oil has a kinematic viscosity at 40 ° C of 2-15 mm 2 /s, and the base oil has a kinematic viscosity of 120 ° C and a movement of 40 ° C. The viscosity ratio is 0.24-0.29.
更优选地,上述基础油的40℃运动粘度为3~7mm2/s,且当基础油40℃运动粘度为3~5mm2/s时,其120℃运动粘度与40℃运动粘度的比值为0.24~0.29;当基础油40℃运动粘度为大于5~小于等于7mm2/s时,其120℃运动粘度与40℃运动粘度的比值为0.23~0.28。More preferably, the base oil has a kinematic viscosity at 40 ° C of 3 to 7 mm 2 /s, and when the base oil has a kinematic viscosity at 40 ° C of 3 to 5 mm 2 /s, the ratio of the kinematic viscosity at 120 ° C to the kinematic viscosity at 40 ° C is 0.24 to 0.29; when the kinematic viscosity of the base oil at 40 ° C is more than 5 to less than or equal to 7 mm 2 /s, the ratio of the kinematic viscosity at 120 ° C to the kinematic viscosity at 40 ° C is 0.23 to 0.28.
根据本发明,只要基础油中同时含有烷基苯油和酯类油,并满足如上要求即可,其中对于烷基苯油和酯类油的用量并没有特殊要求。然而为了兼顾本发明上述基础油在使用过程中与烃类制冷剂的溶解度,含有该基础油的制冷组合物的粘温特性,以及油墨厚度。在本发明的一种优选情况下,以上述基础油的总量为基准,烷基苯油的含量为40-80wt.%,酯类油的含量为20-60wt.%,优选烷基苯油的含量为40-75wt.%,酯类油的含量为25-60wt.%。According to the present invention, as long as the base oil contains both an alkylbenzene oil and an ester oil, and the above requirements are satisfied, there is no particular requirement for the amount of the alkylbenzene oil and the ester oil. However, in order to balance the solubility of the above-mentioned base oil with a hydrocarbon refrigerant during use, the viscosity-temperature characteristics of the refrigeration composition containing the base oil, and the thickness of the ink. In a preferred aspect of the present invention, the content of the alkyl benzene oil is 40-80 wt.%, and the content of the ester oil is 20-60 wt.%, based on the total amount of the above base oil, preferably an alkyl benzene oil. The content is 40-75 wt.%, and the content of the ester oil is 25-60 wt.%.
虽然满足上述条件的基础油均能达到本发明的目的,但是本发明的发明人发现,当上述基础油所选用的酯类油的粘度范围为2-15mm2/s,粘度指数大于90时,使用该基础油得到的冷冻机油的粘温特征能够得到更好的提高。因此,本发明优选上述酯类油的40℃运动粘度为2-15mm2/s,更优选为8-15mm2/s,且该酯类油的粘度指数大于90,更优选大于120。Although the base oil satisfying the above conditions can attain the object of the present invention, the inventors of the present invention have found that when the ester oil selected for the base oil has a viscosity in the range of 2 to 15 mm 2 /s and a viscosity index of more than 90, The viscosity-temperature characteristics of the refrigerating machine oil obtained using the base oil can be further improved. Accordingly, in the present invention, it is preferred that the above ester oil has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, more preferably 8 to 15 mm 2 /s, and the ester oil has a viscosity index of more than 90, more preferably more than 120.
根据本发明,本领域技术人员可以选择任意符合上述要求的酯类油以得到本发明基础油。在本发明的一种优选实施方式中,在上述基础油中可以使用的酯类油包括但不限于C6-C14一元醇酯、C8-C18一元酸酯、C4-C12二元醇酯、C4-C12二元酸酯、C3-C6多元醇酯、C3-C6多元酸酯、以及具有特定结构 式的聚亚烷氧基醚单酯和聚亚烷氧基醚双酯中的一种或多种。In accordance with the present invention, one skilled in the art can select any ester oil that meets the above requirements to obtain the base oil of the present invention. In a preferred embodiment of the present invention, the ester oils usable in the above base oils include, but are not limited to, C 6 -C 14 monohydric alcohol esters, C 8 -C 18 monobasic acid esters, C 4 -C 12 a monool ester, a C 4 -C 12 dibasic acid ester, a C 3 -C 6 polyhydric alcohol ester, a C 3 -C 6 polybasic acid ester, and a polyalkyleneoxy ether monoester having a specific structural formula and a polyalkylene oxide One or more of the ether diesters.
优选地,上述C6-C14一元醇酯是指由碳原子总数为6-14的一元醇为原料合成的酯,其包括但不限于一元醇选自异己醇、异庚醇、异辛醇、异壬醇、异癸醇和异十三醇的C1-C6酸酯。其中C1-C6酸为甲酸、乙酸、丙酸、丁酸、戊酸或己酸。在更优选的情况下,上述C6-C14一元醇酯包括但不限于异十三醇酯、异癸醇酯、异壬醇酯、异辛醇酯、异庚醇酯和异己醇酯中的一种或多种。Preferably, the above C 6 -C 14 monool ester refers to an ester synthesized from a monohydric alcohol having a total of 6-14 carbon atoms, including but not limited to a monohydric alcohol selected from the group consisting of isohexanol, isoheptanol, and isooctanol. , C 1 -C 6 acid esters of isodecyl alcohol, isodecyl alcohol and isotridecyl alcohol. Wherein the C 1 -C 6 acid is formic acid, acetic acid, propionic acid, butyric acid, valeric acid or caproic acid. In a more preferred case, the above C 6 -C 14 monool esters include, but are not limited to, isotridecyl esters, isodecyl alcohol esters, isodecyl alcohol esters, isooctanol esters, isoheptyl esters, and isohexyl alcohol esters. One or more.
优选地,上述C8-C18一元酸酯是指由碳原子总数为8-18的一元酸为原料合成的酯,其包括但不限于C10-C18一元脂肪酸的C1-C8正构或异构醇酯,优选包括但不限于一元酸选自癸酸、十二酸、十四酸、十六酸或十八酸的C1-C8正构或异构醇酯。其中C1-C8正构或异构醇,例如包括但不限于甲醇、乙醇、丙醇、丁醇、戊醇、己醇、庚醇或辛醇。在更优选的情况下,上述C8-C18一元酸酯包括但不限于十二酸二(2-乙基己基)酯、癸酸二(2-乙基己基)酯、硬脂酸甲酯、月桂酸异丁酯和月桂酸异戊酯中的一种或多种。Preferably, the above C 8 -C 18 monobasic acid ester refers to an ester synthesized from a monobasic acid having a total number of carbon atoms of 8-18, including but not limited to C 1 -C 8 positive of C 10 -C 18 monobasic fatty acid. The or isomeric alcohol ester preferably includes, but is not limited to, a C 1 -C 8 normal or isomeric alcohol ester of a monobasic acid selected from the group consisting of citric acid, dodecanoic acid, myristic acid, palmitic acid or octadecanoic acid. Wherein C 1 -C 8 normal or isomeric alcohols include, for example but are not limited to, methanol, ethanol, propanol, butanol, pentanol, hexanol, heptanol or octanol. In a more preferred case, the above C 8 -C 18 monobasic acid ester includes, but is not limited to, di(2-ethylhexyl) dodecanoate, di(2-ethylhexyl) phthalate, methyl stearate. One or more of isobutyl laurate and isoamyl laurate.
优选地,上述C4-C12二元醇酯是指由碳原子总数为4-12的二元醇为原料合成的酯,其包括但不限于二元醇选自己二醇、甲基己二醇、新戊基乙二醇或1,10-癸二醇的C5-C10正构或异构酸酯;其中C5-C10正构或异构酸,例如包括但不限于戊酸、己酸、庚酸、辛酸,壬酸或癸酸。在更优选的情况下,上述C4-C12二元醇酯包括但不限于3-甲基-1,6-乙二醇二正辛酸酯、1,10-癸二醇二(2-乙基己基)酯和己二醇二异辛酸酯中的一种或多种。Preferably, the above C 4 -C 12 glycol ester refers to an ester synthesized from a glycol having a total number of carbon atoms of 4 to 12, which includes but is not limited to a glycol selected from its own diol and methyl hexane. a C 5 -C 10 normal or isomeric acid ester of an alcohol, neopentyl glycol or 1,10-decanediol; wherein the C 5 -C 10 normal or isomeric acid, for example including but not limited to valeric acid , hexanoic acid, heptanoic acid, octanoic acid, citric acid or citric acid. In a more preferred case, the above C 4 -C 12 glycol esters include, but are not limited to, 3-methyl-1,6-ethylene glycol di-n-octanoate, 1,10-nonanediol di(2- One or more of ethylhexyl)ester and hexanediol diisooctanoate.
优选地,上述C4-C12二元酸酯是指由碳原子总数为4-12的二元酸为原料合成的单酯和/或双酯,其包括但不限于二元酸选自丁二酸、己二酸、庚二酸、壬二酸、癸二酸或邻苯二甲酸的C4-C10正构或异构醇酯,其中C4-C10正构或异构醇,例如包括但不限于丁醇、戊醇、己醇、庚醇、辛醇、壬醇和癸醇中的一种或多种;在更优选的情况下,上述C4-C12二元酸酯包括但不限 于己二酸二正辛酯、3-甲基己二酸二正辛酯、己二酸二(2-乙基己基)酯、己二酸间甲基环己基二(2-乙基己基)酯、己二酸对甲基环己基二(2-乙基己基)酯、壬二酸二(2-乙基己基)酯、癸二酸二正丁酯中的一种或多种。Preferably, the above C 4 -C 12 dibasic acid ester refers to a monoester and/or diester synthesized from a dibasic acid having a total number of carbon atoms of 4 to 12, which includes, but is not limited to, a dibasic acid selected from the group consisting of a C 4 -C 10 normal or isomeric alcohol ester of a diacid, adipic acid, pimelic acid, sebacic acid, sebacic acid or phthalic acid, wherein the C 4 -C 10 normal or isomeric alcohol, For example, including but not limited to, one or more of butanol, pentanol, hexanol, heptanol, octanol, decyl alcohol, and decyl alcohol; in a more preferred case, the above C 4 -C 12 dibasic acid ester includes But not limited to di-n-octyl adipate, di-n-octyl 3-methyladipate, di(2-ethylhexyl) adipate, m-cyclohexyl di(2-ethyl) adipate One or more of hexyl)ester, adipic acid p-methylcyclohexyl bis(2-ethylhexyl) ester, di(2-ethylhexyl) sebacate, and di-n-butyl sebacate.
优选地,上述C3-C6多元醇酯是以羟基官能团的数量为3-6的多元醇为原料合成的单酯、双酯和/或多酯,其包括但不限于多元醇选自丙三醇、三羟甲基丙烷或季戊四醇中的C4-C10正构或异构酸酯,其中C4-C10正构或异构酸,例如包括但不限于丁酸、戊酸、己酸、庚酸、辛酸、壬酸和癸酸中的一种或多种。在更优选的情况下,上述C6-C20多元醇酯包括但不限于丙三醇三己酸酯、季戊四醇四己酸酯、三羟甲基丙烷三己酸酯和三羟甲基丙烷三戊酸酯中的一种或多种。Preferably, the above C 3 -C 6 polyol ester is a monoester, diester and/or polyester synthesized from a polyol having a hydroxyl functional group of 3-6, including but not limited to a polyol selected from the group consisting of a C 4 -C 10 normal or isomeric acid ester of a triol, trimethylolpropane or pentaerythritol, wherein the C 4 -C 10 normal or isomeric acid, for example but not limited to butyric acid, valeric acid, One or more of acid, heptanoic acid, octanoic acid, citric acid, and citric acid. In a more preferred case, the above C 6 -C 20 polyol esters include, but are not limited to, glycerol trihexanoate, pentaerythritol tetrahexanoate, trimethylolpropane trihexanoate, and trimethylolpropane One or more of valerate.
优选地,上述C3-C6多元酸酯是以羧基官能团的数量为3-6的多元酸为原料合成的酯,其包括但不限于多元酸选自偏苯三酸和均苯四甲酸的C4-C10正构或异构醇酯,其中C4-C10正构或异构醇,包括但不限于例如丁醇、戊醇、己醇、庚醇、辛醇,壬醇或癸醇。Preferably, the above C 3 -C 6 polyacid ester is an ester synthesized from a polybasic acid having a carboxyl functional group of 3-6, including but not limited to a polybasic acid selected from the group consisting of trimellitic acid and pyromellitic acid. C 4 -C 10 normal or isomeric alcohol esters, wherein C 4 -C 10 normal or isomeric alcohols include, but are not limited to, for example, butanol, pentanol, hexanol, heptanol, octanol, decyl alcohol or hydrazine alcohol.
优选地,上述聚亚烷氧基醚单酯为具有如下结构式的聚亚烷氧基醚单酯,Preferably, the above polyalkoxy ether monoester is a polyalkyleneoxy ether monoester having the following structural formula,
Figure PCTCN2015092167-appb-000001
Figure PCTCN2015092167-appb-000001
其中n1为0或1-3中的整数,n2为1-3中的整数,R1为C4H9-、C5H11、C6H13-和C7H15-中的一种,所述R2为C11H23-、C6H13-、C7H15-、C8H17-、C9H19-和C10H21-中的一种,在更优选的情况下,上述聚亚烷氧基醚单酯有如下结构式:Wherein n 1 is an integer in 0 or 1-3, n 2 is an integer in 1-3, and R 1 is in C 4 H 9 -, C 5 H 11 , C 6 H 13 -, and C 7 H 15 - In one case, the R 2 is one of C 11 H 23 -, C 6 H 13 -, C 7 H 15 -, C 8 H 17 -, C 9 H 19 - and C 10 H 21 -, Preferably, the above polyalkoxy ether monoester has the following structural formula:
Figure PCTCN2015092167-appb-000002
Figure PCTCN2015092167-appb-000002
优选地,上述聚亚烷氧基醚双酯为具有如下结构式的聚亚烷氧基二醇双 酯,Preferably, the above polyalkoxy ether diester is a polyalkyleneoxy glycol double having the following structural formula ester,
其中m为1-3中的整数,R3和R4分别独立地选自C6H13-、C7H15-、C8H17-、C19H19-和C10H21-中的一种。在更优选的情况下,上述聚亚烷氧基醚双酯有如下结构式:Wherein m is an integer in 1-3, and R 3 and R 4 are each independently selected from the group consisting of C 6 H 13 -, C 7 H 15 -, C 8 H 17 -, C 19 H 19 - and C 10 H 21 - One kind. In a more preferred case, the above polyalkoxy ether diester has the following structural formula:
Figure PCTCN2015092167-appb-000004
Figure PCTCN2015092167-appb-000004
虽然满足上述条件的基础油均能达到本发明的目的,但是本发明的发明人发现,当上述烷基苯油的40℃运动粘度为2-15mm2/s时,使用由含有该烷基苯油的基础油得到的冷冻机油的粘度性能更好的符合应用需求。因此,本发明优选上述烷基苯油的粘度范围为2-15mm2/s,优选为3-7mm2/s。Although the base oil satisfying the above conditions can attain the object of the present invention, the inventors of the present invention have found that when the above-mentioned alkylbenzene oil has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, the use of the alkylbenzene is contained. The viscosity of the refrigerating machine oil obtained from the base oil of the oil is better in accordance with the application requirements. Accordingly, in the present invention, it is preferred that the above alkylbenzene oil has a viscosity in the range of 2 to 15 mm 2 /s, preferably 3 to 7 mm 2 /s.
根据本发明,本领域技术人员可以选择任意符合上述要求的烷基苯油以得到本发明的基础油。在本发明的一种优选实施方式中,在上述基础油中可以使用的烷基苯油包括但不限于烷基的碳原子数为8-18的烷基苯油,在优选的情况下,上述烷基苯油为单链烷基苯油,其包括但不限于癸基苯、十一烷基苯、十二烷基苯、十三烷基苯、十五烷基苯、十六烷基苯中的一种或者两种及两种以上的混合物。例如包括但不限于商购自Pt.Unggul Indah Cahaya Tbk.(印尼公司),商购自天津佰特化工公司或商购自韩国其优势公司的烷基苯油。According to the present invention, those skilled in the art can select any alkyl benzene oil meeting the above requirements to obtain the base oil of the present invention. In a preferred embodiment of the present invention, the alkylbenzene oil usable in the above base oil includes, but is not limited to, an alkylbenzene oil having an alkyl group having 8 to 18 carbon atoms, and preferably, the above The alkyl benzene oil is a single chain alkyl benzene oil including, but not limited to, mercaptobenzene, undecylbenzene, dodecylbenzene, tridecylbenzene, pentadecylbenzene, hexadecylbenzene One or two or a mixture of two or more. For example, including but not limited to, commercially available from Pt. Unggul Indah Cahaya Tbk. (Indonesian company), commercially available from Tianjin Haote Chemical Co., Ltd. or commercially available from South Korea, its dominant company, alkyl benzene oil.
虽然满足上述条件的基础油均能达到本发明的目的,但是本发明的发明人发现,当在上述基础油中进一步添加一种不同于烷基苯油的另一种烃类油时,能够进一步降低基础油的粘度,而且其与烃类制冷剂具有较好的相容性,有利于促使所得到的冷冻机油具有更为优良的低温流动性和润滑性及较低的摩擦系数,进而更好地实现节能减排,保护环境的效果。 Although the base oil satisfying the above conditions can attain the object of the present invention, the inventors of the present invention have found that when another hydrocarbon oil different from alkylbenzene oil is further added to the above base oil, further The viscosity of the base oil is lowered, and the compatibility with the hydrocarbon refrigerant is better, which is favorable for promoting the obtained refrigerator oil to have better low-temperature fluidity and lubricity and a lower friction coefficient, thereby being better. The realization of energy saving and emission reduction and environmental protection.
根据本发明,对于添加到基础油中的不同于烷基苯油的另一种烃类油及其用量并没有特殊要求,只要在加入该不同于烷基苯油的另一种烃类油后,依然能够满足基础油120℃运动粘度与40℃运动粘度的比值在0.23-0.30范围内即可。优选情况下,上述不同于烷基苯油的另一种烃类油的40℃运动粘度在4mm2/s以下,倾点小于-30℃,沸点小于280℃。通过调整烃类油的上述性能,有利于更好地调整所制备的基础油,以及冷冻机油组合物的最终性能。进而有利于更好地实现节能减排,进而保护环境的目的。According to the present invention, there is no particular requirement for another hydrocarbon oil other than alkyl benzene oil to be added to the base oil and the amount thereof, as long as the addition of the other hydrocarbon oil different from the alkyl benzene oil , can still meet the ratio of the base oil 120 ° C kinematic viscosity and 40 ° C kinematic viscosity in the range of 0.23-0.30. Preferably, the other hydrocarbon oil different from the alkyl benzene oil has a 40 ° C kinematic viscosity of 4 mm 2 /s or less, a pour point of less than -30 ° C, and a boiling point of less than 280 ° C. By adjusting the above properties of the hydrocarbon oil, it is advantageous to better adjust the base oil prepared, as well as the final properties of the refrigerating machine oil composition. In turn, it is conducive to better achieving energy conservation and emission reduction, thereby protecting the environment.
更为优选地,以上述基础油的总量为基准,不同于烷基苯油的另一种烃类油的含量为0.1-20wt.%。优选情况下,以上述基础油的总量为基准,烷基苯油的含量为40-74.9wt.%、酯类油的含量为25-60wt.%、不同于烷基苯油的另一种烃类油的含量为0.1-20wt.%。更为优选地,以上述基础油的总量为基准,不同于烷基苯油的另一种烃类油的含量为5-10wt.%。More preferably, the content of another hydrocarbon oil different from the alkylbenzene oil is from 0.1 to 20% by weight based on the total amount of the above base oil. Preferably, the content of the alkylbenzene oil is 40-74.9 wt.%, the content of the ester oil is 25-60 wt.%, and the other is different from the alkylbenzene oil based on the total amount of the above base oil. The hydrocarbon oil is present in an amount of from 0.1 to 20% by weight. More preferably, the content of another hydrocarbon oil different from the alkylbenzene oil is from 5 to 10% by weight based on the total amount of the above base oil.
根据本发明,本领域技术人员可以选择任意符合上述要求的不同于烷基苯油的另一种烃类油以得到本发明基础油。在本发明的一种优选实施方式中,在上述基础油中可以使用的不同于烷基苯油的另一种烃类油,包括但不限于费托合成异构烷烃、加氢异构烷烃、加氢裂化异构烷烃、聚α烯烃、烯烃叠合油、多烷基环戊烷、多烷基环己烷中的一种或多种。In accordance with the present invention, one skilled in the art can select any other hydrocarbon oil other than the alkyl benzene oil that meets the above requirements to obtain the base oil of the present invention. In a preferred embodiment of the present invention, another hydrocarbon oil different from alkyl benzene oil which may be used in the above base oil includes, but is not limited to, Fischer-Tropsch synthesized isoparaffins, hydroisomerized alkanes, One or more of hydrocracking isoparaffins, polyalphaolefins, olefin stacking oils, polyalkylcyclopentanes, polyalkylcyclohexanes.
这些可选的烃类油可以是任意市售产品,或者是任意石油化工、煤化工等化工流程的合成品或副产品,只要经过检测或经过处理,使其满足40℃运动粘度在4mm2/s以下,倾点小于-30℃,沸点小于280℃的要求,即可作为本发明冷冻机油组合物用的基础油的有效成分使用。These optional hydrocarbon oils may be any commercially available products or synthetic or by-products of any petrochemical, coal chemical and other chemical processes, as long as they are tested or treated to meet a 40 ° C kinematic viscosity of 4 mm 2 /s. Hereinafter, the pour point is less than -30 ° C, and the boiling point is less than 280 ° C, which can be used as an active ingredient of the base oil for the refrigerating machine oil composition of the present invention.
本发明还提供了一种冷冻机油组合物,该组合物含有基础油和添加剂,其中,所述基础油为上述冷冻机油组合物用基础油。根据本发明提供的冷冻机油组合物,在冷冻机油组合物通过在基础油中加入添加剂会使得基础油的120℃运动粘度与40℃运动粘度的比值发生小幅度的变化,在本发明中的一 种优选情况下,上述冷冻机油组合物120℃运动粘度与40℃运动粘度的比值为0.23-0.30,更优选为0.24~0.29。将冷冻机油组合物120℃运动粘度与40℃运动粘度的比值控制在该范围内,有利于在保证油品低温粘度较低的情况下(低粘度趋势下),通过提高其粘温特性,以增加高温下油膜的厚度,提高边界润滑性和密封性,进而提高压缩机制冷效率COP值,最终达到节能减排,保护环境的目的。The present invention also provides a refrigerating machine oil composition comprising a base oil and an additive, wherein the base oil is a base oil for the above refrigerating machine oil composition. According to the refrigerating machine oil composition provided by the present invention, in the refrigerating machine oil composition, by adding an additive to the base oil, the ratio of the 120 ° C kinematic viscosity of the base oil to the 40 ° C kinematic viscosity is slightly changed, in the present invention. Preferably, the ratio of the 120 ° C kinematic viscosity of the refrigerator oil composition to the 40 ° C kinematic viscosity is from 0.23 to 0.30, more preferably from 0.24 to 0.29. The ratio of the 120 ° C kinematic viscosity of the refrigerating machine oil composition to the 40 ° C kinematic viscosity is controlled within this range, which is advantageous in improving the viscosity-temperature characteristics of the oil by lowering the low-temperature viscosity of the oil (low viscosity tendency). Increase the thickness of the oil film at high temperature, improve the boundary lubrication and sealing, and thus improve the COP value of the refrigeration efficiency of the compressor, and finally achieve the purpose of energy saving and environmental protection.
根据本发明提供的冷冻机油组合物,在一种优选情况下,上述机油组合物40℃运动粘度在2~15mm2/s,优选3~7mm2/s,闪点大于140℃,燃点大于150℃,倾点小于-50℃;在另一种优选情况下,上述冷冻机油组合物以组合物的总量为基准,所述基础油的含量为94-98wt.%,所述添加剂的含量为2-6wt.%。According to the refrigerator oil composition provided by the present invention, in a preferred case, the oil composition has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, preferably 3 to 7 mm 2 /s, a flash point of more than 140 ° C, and a flash point of more than 150. °C, the pour point is less than -50 ° C; in another preferred case, the above-mentioned refrigerator oil composition is based on the total amount of the composition, the base oil content is 94-98 wt.%, and the content of the additive is 2-6wt.%.
本发明的冷冻机油组合物的制备没有特别要求,只要将本发明上述冷冻机油组合物用基础油与添加剂混合即可,可以先获得冷冻机油组合物用基础油,再与添加剂混合,也可以直接将组成冷冻机油组合物用基础油的组分与添加剂直接混合以获得冷冻机油组合物,本发明没有特别要求。The preparation of the refrigerating machine oil composition of the present invention is not particularly required, and if the refrigerating machine oil composition of the present invention is mixed with a base oil and an additive, the base oil for the refrigerating machine oil composition may be obtained first, and then mixed with the additive, or directly The components constituting the refrigerator oil composition with the base oil are directly mixed with the additive to obtain a refrigerating machine oil composition, which is not particularly required in the present invention.
优选地,上述添加剂选自润滑剂、减摩剂、抗氧剂、抗腐蚀剂和抗泡剂中的一种或多种。Preferably, the above additive is selected from one or more of a lubricant, an antifriction agent, an antioxidant, an anticorrosive agent, and an antifoaming agent.
根据本发明提供的冷冻机油组合物,上述添加剂及其含量可以是用于冷冻机油组合物的各种常规添加剂及其常规含量。例如,上述添加剂可以是为了改善冷冻机油润滑性能的润滑剂、提高减摩性能的减摩剂和改善热氧化安定性的抗氧剂、抗腐蚀剂、抗泡剂等。According to the refrigerating machine oil composition provided by the present invention, the above additives and their contents may be various conventional additives for refrigerating machine oil compositions and their conventional contents. For example, the above additives may be a lubricant for improving the lubricating properties of the refrigerating machine oil, an antifriction agent for improving the antifriction property, and an antioxidant, an anticorrosive agent, an antifoaming agent and the like for improving the thermal oxidation stability.
上述润滑剂可以是本领域通用的磷酸酯类润滑剂,如三甲苯基磷酸酯、三苯基磷酸酯、辛基二苯基磷酸酯、苄基二苯基磷酸酯、苯基硫代磷酸酯中的一种或多种。以组合物的总量为基准,润滑剂的含量可以为0-6.0重量%,优选为1.0-3.5重量%。 The above lubricant may be a phosphate ester lubricant commonly used in the art, such as tricresyl phosphate, triphenyl phosphate, octyl diphenyl phosphate, benzyl diphenyl phosphate, phenyl phosphorothioate. One or more of them. The lubricant may be included in an amount of from 0 to 6.0% by weight, based on the total amount of the composition, preferably from 1.0 to 3.5% by weight.
上述减摩剂可以是本领域通用的长链脂肪酸、长链脂肪醇、长链脂肪酯、酰胺、膦酸酯和市售的节能减摩剂中的一种或几种,具体地可以是油酸、二聚亚油酸、十二醇、硬脂酸丁酯、油酸乙二醇酯、油酸酰胺、苯三唑十二胺盐等、二异辛基膦酸酯和共晶滚球中的一种或多种。以组合物的总量为基准,减摩剂的含量可以为0-0.8重量%,优选为0.02-0.6重量%。The antifriction agent may be one or more of long-chain fatty acids, long-chain fatty alcohols, long-chain fatty esters, amides, phosphonates and commercially available energy-saving antifriction agents which are generally used in the art, and may specifically be oils. Acid, dimerized linoleic acid, dodecyl alcohol, butyl stearate, ethylene glycol oleate, oleic acid amide, benzotriazole dodecylamine, etc., diisooctylphosphonate and eutectic ball One or more of them. The antifriction agent may be included in an amount of from 0 to 0.8% by weight, preferably from 0.02 to 0.6% by weight, based on the total amount of the composition.
上述抗氧剂可以是本领域通用的各种酚型抗氧剂,如2,6-二叔丁基对甲酚、2,3-二叔丁基-4-甲酚、2,6-二叔丁基酚、4,4’-四甲基二(2,6-二叔丁基酚)、对苯二酚、β-萘酚中的一种或多种。以组合物的总量为基准,抗氧剂的含量可以为0-3重量%,优选为0.2-0.8重量%。The above antioxidants may be various phenolic antioxidants commonly used in the art, such as 2,6-di-tert-butyl-p-cresol, 2,3-di-tert-butyl-4-cresol, 2,6-di One or more of tert-butylphenol, 4,4'-tetramethylbis(2,6-di-tert-butylphenol), hydroquinone, and β-naphthol. The antioxidant may be included in an amount of from 0 to 3% by weight, preferably from 0.2 to 0.8% by weight, based on the total amount of the composition.
上述抗腐蚀剂可以为本领域通用的苯三唑衍生物和噻二唑衍生物类抗腐蚀剂,如N,N-二烷基氨基亚甲基苯三唑、2,5-二巯基-1,3,4-噻二唑衍生物、二巯基-苯并噻二唑、二巯基噻二唑钠中的一种或多种。以组合物的总量为基准,所述抗腐蚀剂的含量可以为0-0.1重量%,优选为0.02-0.05重量%。The above anticorrosive agent may be a benzotriazole derivative and a thiadiazole derivative anticorrosive agent commonly used in the art, such as N,N-dialkylaminomethylene benzotriazole, 2,5-dimercapto-1,3 One or more of a 4-thiadiazole derivative, a dimercapto-benzothiadiazole, and a sodium dimercaptothiadiazole. The anticorrosive agent may be included in an amount of from 0 to 0.1% by weight, preferably from 0.02 to 0.05% by weight, based on the total amount of the composition.
上述抗泡剂可以为本领域通用的抗泡剂,如二甲基硅油、丙烯酸酯的均聚物或共聚物中的一种或多种。以组合物的总量为基准,所述抗泡剂的含量可以是0-0.01重量%,优选为0.001-0.005重量%。The antifoaming agent may be an antifoaming agent generally used in the art, such as one or more of a dimethicone, a homopolymer or a copolymer of an acrylate. The antifoaming agent may be included in an amount of from 0 to 0.01% by weight, preferably from 0.001 to 0.005% by weight, based on the total amount of the composition.
本发明还提供了一种用于制冷的组合物,该组合物包括冷冻机油组合物和制冷剂,其中,所述冷冻机油组合物为上述冷冻机油组合物。The present invention also provides a composition for refrigeration, the composition comprising a refrigerating machine oil composition and a refrigerant, wherein the refrigerating machine oil composition is the above refrigerating machine oil composition.
根据本发明,所述制冷剂可以为本领域技术人员已知的任意一种制冷剂。优选情况下,所述制冷剂为烃类制冷剂,例如R600A或R290或R134A。According to the invention, the refrigerant may be any refrigerant known to those skilled in the art. Preferably, the refrigerant is a hydrocarbon refrigerant such as R600A or R290 or R134A.
根据本发明,优选情况下,该组合物中,所述冷冻机油组合物的含量为70-90wt.%,更优选为75-90wt.%,制冷剂的含量为10-30wt.%,更优选为10-25wt.%。According to the present invention, preferably, the composition of the refrigerator oil composition is 70-90 wt.%, more preferably 75-90 wt.%, and the content of the refrigerant is 10-30 wt.%, more preferably in the composition. It is 10-25wt.%.
本发明还提供了一种制冷的方法,该方法包括将冷冻机油组合物和制冷剂混合或不经混合后送入制冷装置的压缩机中进行压缩,其中,所述冷冻机 油组合物为上述冷冻机油组合物;以所述冷冻机油组合物和制冷剂的总量为基准,所述冷冻机油组合物的加入量为70-90wt.%,更优选为75-90wt.%,制冷剂的加入量为10-30wt.%,更优选为10-25wt.%。The present invention also provides a method of refrigeration, comprising: mixing or recombining a refrigerating machine oil composition and a refrigerant into a compressor of a refrigerating device for compression, wherein the refrigerating machine The oil composition is the above-described refrigerating machine oil composition; the refrigerating machine oil composition is added in an amount of 70-90 wt.%, more preferably 75-90 wt.%, based on the total amount of the refrigerating machine oil composition and the refrigerant. The amount of the refrigerant to be added is 10 to 30 wt.%, more preferably 10 to 25 wt.%.
在本发明的制冷的方法中,冷冻机油组合物可以混合好之后再加入,也可以将组成冷冻机油组合物的各个组分直接加入,本发明没有特别要求。In the refrigerating method of the present invention, the refrigerating machine oil composition may be added after being mixed, and the components constituting the refrigerating machine oil composition may be directly added, which is not particularly required in the present invention.
根据本发明,优选情况下,相对于3.5kW的制冷量,所述冷冻机油组合物的用量为0.2-0.5kg。According to the present invention, it is preferred that the refrigerator oil composition is used in an amount of 0.2 to 0.5 kg with respect to a cooling capacity of 3.5 kW.
除非特别说明,本发明所述原料和试剂均为市售商品。Unless otherwise stated, the starting materials and reagents of the present invention are all commercially available.
下面通过实施例对本发明作进一步说明。如下实施例1-10用于说明本发明提供的冷冻机油组合物用基础油、冷冻机油组合物及其制备方法。The invention is further illustrated by the following examples. The following Examples 1-10 are used to illustrate the base oil, the refrigerator oil composition for a refrigerating machine oil composition provided by the present invention, and a preparation method thereof.
实施例1Example 1
(1)冷冻机油组合物用基础油的原料与用量:(1) Raw materials and dosage of base oil for refrigerating machine oil composition:
烷基苯油:商购自Pt.Unggul Indah Cahaya Tbk.(印尼公司)生产的烷基苯油(其包括10wt%的癸烷基苯、25wt%的十一烷基苯、35wt%的十二烷基苯和30%的十三烷基苯,40℃的运动粘度为4.2mm2/s),用量为35重量份;Alkyl benzene oil: commercially available from Pt. Unggul Indah Cahaya Tbk. (Indonesian company) alkyl benzene oil (which includes 10% by weight of decyl benzene, 25% by weight of undecyl benzene, and 35% by weight of twelve An alkylbenzene and 30% tridecylbenzene having a kinematic viscosity at 40 ° C of 4.2 mm 2 /s) in an amount of 35 parts by weight;
酯类油:3-甲基己二酸二正辛酯(40℃的运动粘度为8.38mm2/s,粘度指数为170),用量为45重量份;Ester oil: di-n-octyl 3-methyladipate (kinematic viscosity at 40 ° C is 8.38 mm 2 / s, viscosity index is 170), the amount is 45 parts by weight;
不同于烷基苯油的另一种烃类油:荷兰SHELL公司(煤间接液化)F-T工序生产的费托合成异构烷烃(其主要成分为异构烷烃,40℃运动粘度为2.8mm2/s,倾点为-32℃,沸点为270~280℃),用量为5重量份。Another hydrocarbon oil different from alkyl benzene oil: Fischer-Tropsch synthesized isoparaffin produced by the SHELL company (indirect coal liquefaction) in the Netherlands (the main component of which is isoparaffin, 40 ° C kinematic viscosity is 2.8 mm 2 / s, pour point is -32 ° C, boiling point is 270 ~ 280 ° C), and the amount is 5 parts by weight.
(2)冷冻机油组合物用基础油的混料方法:将上述原料按比例混合,调配成冷冻机油组合物用基础油。(2) Mixing method of base oil for refrigerating machine oil composition: The above raw materials are mixed in proportion and formulated into a base oil for a refrigerating machine oil composition.
(3)冷冻机油组合物及其制备方法:(3) Refrigerator oil composition and preparation method thereof:
将前述冷冻机油组合物用基础油与0.1重量份2,6-二叔丁基对甲酚、3 重量份三甲苯基磷酸酯、0.2重量份油酸乙二醇酯和0.03重量份N,N-二烷基氨基亚甲基苯三唑混合均匀,调配成冷冻机油组合物,记为S1。The above-mentioned refrigerator oil composition is used with a base oil and 0.1 part by weight of 2,6-di-tert-butyl-p-cresol, 3 Parts by weight of tricresyl phosphate, 0.2 parts by weight of ethylene oleate and 0.03 parts by weight of N,N-dialkylaminomethylene benzenetriazole were uniformly mixed and formulated into a refrigerating machine oil composition, which was designated as S1.
实施例2Example 2
(1)冷冻机油组合物用基础油的原料与用量:(1) Raw materials and dosage of base oil for refrigerating machine oil composition:
烷基苯油:商购自天津佰特化工公司,主要原料为十二烷基苯的烷基苯油(40℃的运动粘度为4.2mm2/s),用量为60重量份;Alkyl benzene oil: commercially available from Tianjin Haote Chemical Co., Ltd., the main raw material is alkyl benzene oil of dodecyl benzene (the kinematic viscosity at 40 ° C is 4.2 mm 2 / s), the amount is 60 parts by weight;
酯类油:1,10-癸二醇二(2-乙基己基)酯(40℃的运动粘度为12.1mm2/s,粘度指数为133),用量为30重量份;Ester oil: 1,10-nonanediol di(2-ethylhexyl) ester (kinetic viscosity at 40 ° C of 12.1 mm 2 / s, viscosity index of 133), the amount is 30 parts by weight;
不同于烷基苯油的另一种烃类油:YOUGONG(韩国)公司加氢异构工序生产的加氢异构烷烃(其主要成分为异构烷烃,40℃运动粘度为3.2mm2/s,倾点为-38℃,沸点为270~280℃),用量为10重量份。Another hydrocarbon oil different from alkyl benzene oil: Hydroisomerized alkane produced by the hydroisomerization process of YOUGONG (Korea) Co., Ltd. (the main component of which is isoparaffin, 40 ° C kinematic viscosity is 3.2 mm 2 /s The pour point is -38 ° C, the boiling point is 270 to 280 ° C), and the amount is 10 parts by weight.
(2)冷冻机油组合物用基础油的混料方法:将上述原料混合,调配成冷冻机油组合物用基础油。(2) Mixing method of base oil for refrigerating machine oil composition: The above raw materials are mixed and formulated into a base oil for a refrigerating machine oil composition.
(3)冷冻机油组合物及其制备方法:(3) Refrigerator oil composition and preparation method thereof:
将前述冷冻机油组合物用基础油与0.2重量份2,6-二叔丁基对甲酚、3.5重量份三甲苯基磷酸酯、0.18重量份油酸乙二醇酯和0.04重量份N,N-二烷基氨基亚甲基苯三唑混合均匀,调配成冷冻机油组合物,记为S2。The foregoing refrigerator oil composition is used with a base oil and 0.2 parts by weight of 2,6-di-tert-butyl-p-cresol, 3.5 parts by weight of tricresyl phosphate, 0.18 parts by weight of ethylene oleate, and 0.04 parts by weight of N,N. - Dialkylaminomethylene benzotriazole was uniformly mixed and formulated into a refrigerating machine oil composition, which was designated as S2.
实施例3Example 3
(1)冷冻机油组合物用基础油的原料与用量:(1) Raw materials and dosage of base oil for refrigerating machine oil composition:
烷基苯油:商购自韩国其优势公司,主要原料为十二烷基苯的烷基苯油(40℃的运动粘度为3.8mm2/s),用量为50重量份;Alkyl benzene oil: commercially available from Korea's dominant company, the main raw material is dodecylbenzene alkyl benzene oil (40 ° C kinematic viscosity of 3.8 mm 2 / s), the amount of 50 parts by weight;
酯类油:丙三醇三己酸酯(40℃的运动粘度为8.93mm2/s,粘度指数为170),用量为40重量份;Ester oil: glycerol trihexanoate (kinematic viscosity at 40 ° C is 8.93 mm 2 / s, viscosity index is 170), the amount is 40 parts by weight;
不同于烷基苯油的另一种烃类油:Mobil(美国)生产的聚α烯烃(其 主要成分为异构烷烃,40℃运动粘度为3.2mm2/s,倾点为-60℃,沸点为270~280℃),用量为10重量份。Another hydrocarbon oil different from alkyl benzene oil: polyalphaolefin produced by Mobil (USA) (the main component of which is isoparaffin, having a kinematic viscosity at 40 ° C of 3.2 mm 2 /s and a pour point of -60 ° C, The boiling point is 270 to 280 ° C), and the amount is 10 parts by weight.
(2)冷冻机油组合物用基础油的混料方法:将上述原料混合,调配成冷冻机油组合物用基础油。(2) Mixing method of base oil for refrigerating machine oil composition: The above raw materials are mixed and formulated into a base oil for a refrigerating machine oil composition.
(3)冷冻机油组合物及其制备方法:(3) Refrigerator oil composition and preparation method thereof:
将前述冷冻机油组合物用基础油与0.5重量份2,6-二叔丁基对甲酚、5重量份三甲苯基磷酸酯、0.2重量份油酸乙二醇酯和0.05重量份N,N-二烷基氨基亚甲基苯三唑混合均匀,调配成冷冻机油组合物,记为S3。The foregoing refrigerator oil composition is used with a base oil and 0.5 parts by weight of 2,6-di-tert-butyl-p-cresol, 5 parts by weight of tricresyl phosphate, 0.2 parts by weight of ethylene oleate, and 0.05 parts by weight of N,N. - Dialkylaminomethylene benzotriazole was uniformly mixed and formulated into a refrigerating machine oil composition, designated as S3.
实施例4Example 4
(1)冷冻机油组合物用基础油的原料与用量:(1) Raw materials and dosage of base oil for refrigerating machine oil composition:
烷基苯油:同实施例1,用量为60重量份;Alkyl benzene oil: same as in Example 1, the amount is 60 parts by weight;
酯类油:同实施例1,用量为40重量份;Ester oil: same as in Example 1, the amount is 40 parts by weight;
(2)冷冻机油组合物用基础油的混料方法:将上述原料按比例混合,调配成冷冻机油组合物用基础油。(2) Mixing method of base oil for refrigerating machine oil composition: The above raw materials are mixed in proportion and formulated into a base oil for a refrigerating machine oil composition.
(3)冷冻机油组合物及其制备方法:(3) Refrigerator oil composition and preparation method thereof:
参照实施例1,将实施例6中步骤(2)制备的冷冻机油组合物用基础油代替实施例1中步骤(2)制备的冷冻机油组合物用基础油,所调配成冷冻机油组合物记为S4。Referring to Example 1, the refrigerating machine oil composition prepared in the step (2) of the embodiment 6 was replaced with a base oil in the base oil of the refrigerating machine oil composition prepared in the step (2) of the first embodiment, and was formulated into a refrigerating machine oil composition. For S4.
实施例5-10Example 5-10
(1)冷冻机油组合物用基础油的原料与用量:(1) Raw materials and dosage of base oil for refrigerating machine oil composition:
参见如下表1,其中所选用的烷基苯均为商购自Pt.Unggul Indah Cahaya Tbk.(印尼公司)生产的烷基苯油。 See Table 1 below, in which the selected alkylbenzenes are all alkylbenzene oils commercially available from Pt. Unggul Indah Cahaya Tbk. (Indonesia).
表1.Table 1.
Figure PCTCN2015092167-appb-000005
Figure PCTCN2015092167-appb-000005
(2)冷冻机油组合物用基础油的混料方法:参照实施例1。(2) Mixing method of base oil for refrigerating machine oil composition: Refer to Example 1.
(3)冷冻机油组合物及其制备方法:(3) Refrigerator oil composition and preparation method thereof:
参照实施例1,将实施例5-10中步骤(2)制备的冷冻机油组合物用基础油代替实施例1中步骤(2)制备的冷冻机油组合物用基础油,所调配成冷冻机油组合物记为S5-S10。Referring to Example 1, the refrigerating machine oil composition prepared in the step (2) of the embodiment 5-10 was replaced with a base oil to replace the refrigerating machine oil composition prepared in the step (2) of the first embodiment with a base oil, and was formulated into a refrigerating machine oil combination. The record is S5-S10.
对比例1Comparative example 1
(1)冷冻机油组合物用基础油的原料与用量:(1) Raw materials and dosage of base oil for refrigerating machine oil composition:
烷基苯油:同实施例1,用量为100重量份; Alkyl benzene oil: same as in Example 1, the amount is 100 parts by weight;
(2)冷冻机油组合物及其制备方法:参照实施例1,将对比例1中步骤(1)制备的冷冻机油组合物用基础油代替实施例1中步骤(1)制备的冷冻机油组合物用基础油,所调配成冷冻机油组合物记为D1。(2) Refrigerator oil composition and preparation method thereof: Referring to Example 1, the refrigerator oil composition prepared in the step (1) of Comparative Example 1 was replaced with the base oil to replace the refrigerator oil composition prepared in the step (1) of Example 1. The base oil was used to prepare a refrigerating machine oil composition as D1.
对比例2Comparative example 2
(1)冷冻机油组合物用基础油的原料与用量:(1) Raw materials and dosage of base oil for refrigerating machine oil composition:
烷基苯油:商购自Pt.Unggul Indah Cahaya Tbk.(印尼公司)生产的烷基苯油(成分包括55wt%的十三烷基苯、25wt%的十四烷基苯和20wt%的十五烷基苯,40℃的运动粘度为5.21mm2/s),用量为100重量份。Alkyl benzene oil: commercially available from Pt. Unggul Indah Cahaya Tbk. (Indonesian company) alkyl benzene oil (ingredients including 55 wt% of tridecyl benzene, 25 wt% of tetradecyl benzene and 20 wt% of ten Pentaalkylbenzene has a kinematic viscosity at 40 ° C of 5.21 mm 2 /s) in an amount of 100 parts by weight.
(2)冷冻机油组合物及其制备方法:参照实施例1,将对比例2中步骤(1)制备的冷冻机油组合物用基础油代替实施例1中步骤(1)制备的冷冻机油组合物用基础油,所调配成冷冻机油组合物记为D2。(2) Refrigerating machine oil composition and preparation method thereof: Referring to Example 1, the refrigerating machine oil composition prepared in the step (1) of Comparative Example 2 was replaced with the base oil to replace the refrigerating machine oil composition prepared in the step (1) of Example 1. The base oil was used to prepare a refrigerating machine oil composition as D2.
对比例3Comparative example 3
(1)冷冻机油组合物用基础油的原料与用量:参照对比例1,区别在于,其中不含有烷基苯油、且酯类油的用量为50重量份,不同于烷基苯油的另一种烃类油的用量为50重量份。(1) Raw material and amount of base oil for refrigerating machine oil composition: Refer to Comparative Example 1, except that it does not contain alkyl benzene oil, and the amount of the ester oil is 50 parts by weight, which is different from the alkyl benzene oil. A hydrocarbon oil is used in an amount of 50 parts by weight.
(2)冷冻机油组合物用基础油的混料方法:将上述原料混合,调配成冷冻机油组合物用基础油。(2) Mixing method of base oil for refrigerating machine oil composition: The above raw materials are mixed and formulated into a base oil for a refrigerating machine oil composition.
(3)冷冻机油组合物及其制备方法:参照实施例1,所调配成冷冻机油组合物记为D3。(3) Refrigerator oil composition and preparation method thereof: Referring to Example 1, the composition of the refrigerator oil was designated as D3.
对比例4Comparative example 4
目前市场上使用最广的以R600A为制冷剂的烃基冷冻机油CS1(商品名suniso1GS Aj sun oil Co.生产),记为D4。Currently, the most widely used hydrocarbon-based refrigerating machine oil CS1 (trade name: suniso1GS Aj sun oil Co.) using R600A as a refrigerant is referred to as D4.
对比例5 Comparative example 5
目前市场上曾推广过的以R600A为制冷剂的烃类冷冻机油K7P,记为D5。The hydrocarbon refrigeration oil K7P, which has been promoted on the market with R600A as refrigerant, is recorded as D5.
测试例1:Test Example 1:
实施例1至10和对比例1至5所调配成冷冻机油组合物用基础油的理化性质如表2所示。The physicochemical properties of the base oils formulated for the refrigerator oil compositions of Examples 1 to 10 and Comparative Examples 1 to 5 are shown in Table 2.
表2.Table 2.
Figure PCTCN2015092167-appb-000006
Figure PCTCN2015092167-appb-000006
*R1:基础油120℃运动粘度与40℃运动粘度的比值*R1: ratio of kinematic viscosity at 120 °C of base oil to kinematic viscosity at 40 °C
如表2中数据可知,在40℃条件下,“实施例1”的运动粘度比“对比例2”的低一个等级,“实施例7”的运动粘度比“对比例1”的低一个等级,然而在120℃条件下,“实施例1”的120℃运动粘度与“对比例2的120℃运动粘度相等;“实施例7”的120℃运动粘度高于“对比例1”的120℃运动粘度;由此可见,通过选择适当的烷基苯油和酯类油,并合理的调整两者的比例使得基础油120℃粘度与40℃粘度的比值符合本发明要求,能够提高本发明所要求 保护的基础油的粘温特性。As can be seen from the data in Table 2, the kinematic viscosity of "Example 1" was lower than that of "Comparative Example 2" at 40 ° C, and the kinematic viscosity of "Example 7" was lower than that of "Comparative Example 1". However, at 120 ° C, the 120 ° C kinematic viscosity of "Example 1" is equal to "120 ° C kinematic viscosity of Comparative Example 2; the 120 ° C kinematic viscosity of "Example 7" is higher than the "Comparative Example 1" of 120 ° C Kinematic viscosity; it can be seen that by selecting an appropriate alkyl benzene oil and an ester oil, and reasonably adjusting the ratio of the two, the ratio of the viscosity of the base oil at 120 ° C to the viscosity at 40 ° C meets the requirements of the present invention, and the present invention can be improved. Claim The viscosity-temperature characteristics of the protected base oil.
测试例2:Test Example 2:
实施例1至10和对比例1至5所调配成冷冻机油组合物的理化性质如表3所示:The physicochemical properties of the refrigerator oil compositions formulated in Examples 1 to 10 and Comparative Examples 1 to 5 are shown in Table 3:
表3.table 3.
Figure PCTCN2015092167-appb-000007
Figure PCTCN2015092167-appb-000007
*R2:冷冻机油组合物120℃运动粘度与40℃运动粘度的比值*R2: ratio of 120 ° C kinematic viscosity to 40 ° C kinematic viscosity of the refrigerating machine oil composition
实施例11-20Example 11-20
实施例11-20用于说明本发明提供的用于制冷的组合物。Examples 11-20 are used to illustrate the compositions for refrigeration provided by the present invention.
将实施例1-10制备的冷冻机油组合物样品S1-S10分别与制冷剂R600A混合,依次获得用于制冷的组合物T1-T10。用于制冷的组合物T1-T10的组成如表4所示。 The refrigerating machine oil composition samples S1-S10 prepared in Examples 1-10 were separately mixed with the refrigerant R600A, and the compositions T1-T10 for refrigeration were sequentially obtained. The composition of the compositions T1-T10 for refrigeration is shown in Table 4.
对比例6-10Comparative example 6-10
将对比例1-5制备的冷冻机油组合物样品D1-D5与制冷剂R600A混合,获得用于制冷的组合物E1-E5。用于制冷的组合物E1-E5的组成如表4所示。The refrigerating machine oil composition samples D1-D5 prepared in Comparative Examples 1-5 were mixed with a refrigerant R600A to obtain compositions E1-E5 for refrigeration. The composition of the compositions E1-E5 used for refrigeration is shown in Table 4.
表4Table 4
样品编号Sample serial number T1T1 T2T2 T3T3 T4T4 T5T5 T6T6 T7T7 T8T8
冷冻机油组合物/重量%Refrigerator oil composition / weight% 9090 9090 9090 9090 9090 9090 9090 9090
R600A/重量%R600A/% by weight 1010 1010 1010 1010 1010 1010 1010 1010
样品编号Sample serial number T9T9 T10T10 E1E1 E2E2 E3E3 E4E4 E5E5  
冷冻机油组合物/重量%Refrigerator oil composition / weight% 9090 9090 9090 9090 9090 9090 9090  
R600A/重量%R600A/% by weight 1010 1010 1010 1010 1010 1010 1010  
测试例3:(压缩机性能试验)Test Example 3: (compressor performance test)
测试方法:将实施例1-10和对比例1-5制备的冷冻机油组合物样品各取27克(约300mL)注入冰箱压缩机(PZ89DIY-4DV)中,用30克R600A作制冷剂,在压缩机性能试验台上进行性能试验。Test method: 27 g (about 300 mL) of each sample of the refrigerating machine oil composition prepared in Examples 1-10 and Comparative Examples 1-5 was injected into a refrigerator compressor (PZ89DIY-4DV), and 30 g of R600A was used as a refrigerant. Performance tests were performed on the compressor performance test bench.
测试项目及依据:Test items and basis:
磨斑直径:根据GB/T3142(30kg、30min、1200转、室温);Wear spot diameter: according to GB/T3142 (30kg, 30min, 1200 rpm, room temperature);
最高油膜强度(PB值):根据GB/T3142(1200转、室温);Maximum oil film strength (PB value): according to GB/T3142 (1200 rpm, room temperature);
Falex极压负荷(磅):根据ASTM D323Falex extreme pressure load (lbs): according to ASTM D323
COP值(制冷效率):热泵系统所能实现的制冷量(制热量)和输入功率的比值;并通过COP值推算出它们的节能效果(节能率)。COP value (refrigeration efficiency): The ratio of the amount of cooling (heat) to the input power that can be achieved by the heat pump system; and the energy saving effect (energy saving rate) is derived from the COP value.
测试结果:参见表5。Test results: See Table 5.
表5.table 5.
样品编号Sample serial number S1S1 S2S2 S3S3 S4S4 S5S5 S6S6 S7S7 S8S8
磨斑直径(mm)Wear spot diameter (mm) 0.390.39 0.380.38 0.370.37 0.370.37 0.370.37 0.380.38 0.400.40 0.370.37
PB(KG)PB (KG) 4646 5050 5252 5252 5353 5252 4545 5353
Falex极压负荷(磅)Falex extreme pressure load (lbs) 10501050 11001100 11001100 11501150 11501150 11001100 10001000 11001100
COP值COP value 1.921.92 1.881.88 1.881.88 1.911.91 1.861.86 1.901.90 1.891.89 1.901.90
节能率(%)Energy saving rate (%) 12.312.3 9.99.9 9.99.9 11.711.7 8.88.8 11.111.1 10.510.5 11.111.1
样品编号Sample serial number S9S9 S10S10 D1D1 D2D2 D3D3 D4D4 D5D5  
磨斑直径(mm)Wear spot diameter (mm) 0.370.37 0.380.38 0.520.52 0.500.50 0.440.44 0.460.46 0.500.50  
PB(KG)PB (KG) 5252 5252 3838 3838 4545 4040 3838  
Falex极压负荷(磅)Falex extreme pressure load (lbs) 11001100 11501150 800800 900900 900900 600600 550550  
COP值COP value 1.881.88 1.881.88 1.871.87 1.871.87 1.841.84 1.711.71 1.781.78  
节能率(%)Energy saving rate (%) 9.99.9 9.99.9 9.49.4 9.49.4 7.67.6 00 4.14.1  
注:节能率以太阳油SUNISO 1GSAJ的值为基准的COP增加百分率。Note: The energy saving rate is the percentage increase of COP based on the value of solar oil SUNISO 1GSAJ.
从上表2至表5的结果可以看出,本发明提供的冷冻机油组合物具有优良的与R600A制冷剂的相溶性和热化学稳定性,并具有优良的粘度温度特性、较高闪点、优良的低温流动性和良好的润滑性及较低的摩擦系数,显示了较明显的节能效果。It can be seen from the results of the above Table 2 to Table 5 that the refrigerator oil composition provided by the present invention has excellent compatibility with the R600A refrigerant and thermochemical stability, and has excellent viscosity temperature characteristics, a high flash point, Excellent low temperature fluidity, good lubricity and low coefficient of friction show significant energy savings.
而且,本发明上述冷冻机油组合物用基础油,通过使用烷基苯油有利于获得粘度较低的基础油,同时通过将烷基苯油与低粘度、高粘度指数的酯类油协同使用,并通过调整所得到的基础油120℃粘度与40℃粘度的比值,有利于形成随着温度的升高,粘度不会过分降低的基础油。通过提高其粘温特性,以增加高温下油膜的厚度,提高边界润滑性和密封性能,进而提高压缩机制冷效率,最终达到进一步节能减排,保护环境的目的。Moreover, the base oil for the above-mentioned refrigerator oil composition of the present invention is advantageous in obtaining a base oil having a lower viscosity by using an alkylbenzene oil, and at the same time, by using an alkylbenzene oil in combination with a low viscosity, high viscosity index ester oil, By adjusting the ratio of the viscosity of the base oil at 120 ° C to the viscosity at 40 ° C, it is advantageous to form a base oil whose viscosity does not excessively decrease as the temperature increases. By increasing its viscosity-temperature characteristics, it increases the thickness of the oil film at high temperatures, improves the boundary lubricity and sealing performance, and further improves the refrigeration efficiency of the compressor, ultimately achieving the goal of further energy saving and environmental protection.
以上详细描述了本发明的优选实施方式,但是,本发明并不限于上述实施方式中的具体细节,在本发明的技术构思范围内,可以对本发明的技术方案进行多种简单变型,这些简单变型均属于本发明的保护范围。The preferred embodiments of the present invention have been described in detail above, but the present invention is not limited to the specific details of the above embodiments, and various simple modifications can be made to the technical solutions of the present invention within the scope of the technical idea of the present invention. These simple variants All fall within the scope of protection of the present invention.
另外需要说明的是,在上述具体实施方式中所描述的各个具体技术特征,在不矛盾的情况下,可以通过任何合适的方式进行组合。为了避免不必要的重复,本发明对各种可能的组合方式不再另行说明。It should be further noted that the specific technical features described in the above specific embodiments may be combined in any suitable manner without contradiction. In order to avoid unnecessary repetition, the present invention will not be further described in various possible combinations.
此外,本发明的各种不同的实施方式之间也可以进行任意组合,只要其不违背本发明的思想,其同样应当视为本发明所公开的内容。 In addition, any combination of various embodiments of the invention may be made as long as it does not deviate from the idea of the invention, and it should be regarded as the disclosure of the invention.

Claims (16)

  1. 一种冷冻机油组合物用基础油,其特征在于,所述基础油含有烷基苯油和酯类油,且所述基础油120℃运动粘度与40℃运动粘度的比值为0.23-0.30。A base oil for a refrigerating machine oil composition, characterized in that the base oil contains an alkylbenzene oil and an ester oil, and the ratio of the kinematic viscosity at 120 ° C of the base oil to the kinematic viscosity at 40 ° C is 0.23 - 0.30.
  2. 根据权利要求1所述的基础油,其中,所述基础油的40℃运动粘度为2-15mm2/s,所述基础油120℃运动粘度与40℃运动粘度的比值为0.24-0.29。The base oil according to claim 1, wherein the base oil has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, and a ratio of a kinematic viscosity at 120 ° C of the base oil to a kinematic viscosity at 40 ° C is 0.24 to 0.29.
  3. 根据权利要求2所述的基础油,其中,所述基础油的40℃运动粘度为3~7mm2/s,且当所述基础油40℃运动粘度为3~5mm2/s时,其120℃运动粘度与40℃运动粘度的比值为0.24~0.29;当所述基础油40℃运动粘度为大于5mm2/s至小于或等于7mm2/s时,其120℃运动粘度与40℃运动粘度的比值为0.23~0.28。The base oil according to claim 2, wherein the base oil has a kinematic viscosity at 40 ° C of 3 to 7 mm 2 /s, and when the base oil has a kinematic viscosity at 40 ° C of 3 to 5 mm 2 /s, The ratio of °C kinematic viscosity to 40°C kinematic viscosity is 0.24~0.29; when the base oil 40°C kinematic viscosity is more than 5mm 2 /s to less than or equal to 7mm 2 /s, its 120°C kinematic viscosity and 40°C kinematic viscosity The ratio is 0.23 to 0.28.
  4. 根据权利要求1所述的基础油,其中,以所述基础油的总量为基准,所述烷基苯油的含量为40-80wt.%,所述酯类油的含量为20-60wt.%。The base oil according to claim 1, wherein the alkylbenzene oil is contained in an amount of 40 to 80% by weight based on the total amount of the base oil, and the ester oil is contained in an amount of 20 to 60% by weight. %.
  5. 根据权利要求1至4中任意一项所述的基础油,其中,所述酯类油的40℃运动粘度为2-15mm2/s,优选为8-15mm2/s,且所述酯类油的粘度指数大于90,优选大于120。The base oil according to any one of claims 1 to 4, wherein the ester oil has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, preferably 8 to 15 mm 2 /s, and the esters The viscosity index of the oil is greater than 90, preferably greater than 120.
  6. 根据权利要求5所述的基础油,其中,所述酯类油选自如下酯类油中的一种或多种:The base oil according to claim 5, wherein the ester oil is selected from one or more of the following ester oils:
    C6-C14一元醇酯,优选为一元醇选自异十三醇、异癸醇或异壬醇的C1-C6酸酯; a C 6 -C 14 monohydric alcohol ester, preferably a monohydric alcohol selected from the group consisting of C 13 -C 6 esters of isotridecyl alcohol, isodecyl alcohol or isodecyl alcohol;
    C8-C18一元酸酯,优选为一元酸选自癸酸、十二酸、十四酸、十六酸或十八酸的C1-C8正构或异构醇酯;a C 8 -C 18 monobasic acid ester, preferably a C 1 -C 8 normal or isomeric alcohol ester of a monobasic acid selected from the group consisting of citric acid, dodecanoic acid, tetradecanoic acid, palmitic acid or octadecanoic acid;
    C4-C12二元醇酯,优选为二元醇选自己二醇、甲基己二醇、新戊基乙二醇或1,10-癸二醇的C5-C10正构或异构酸酯;a C 4 -C 12 glycol ester, preferably a C 5 -C 10 normal or different diol selected from its own diol, methyl hexane diol, neopentyl glycol or 1,10- decanediol Acid ester
    C4-C12二元酸酯,优选为二元酸选自丁二酸、己二酸、庚二酸、壬二酸、癸二酸或邻苯二甲酸的C4-C10正构或异构醇酯;a C 4 -C 12 dibasic acid ester, preferably a dibasic acid selected from the group consisting of C 4 -C 10 normal structures of succinic acid, adipic acid, pimelic acid, sebacic acid, sebacic acid or phthalic acid Isomerized alcohol ester;
    C3-C6多元醇酯,优选为多元醇选自丙三醇、三羟甲基丙烷或季戊四醇的C4-C10正构或异构酸酯;a C 3 -C 6 polyol ester, preferably a C 4 -C 10 normal or isomeric acid ester of a polyol selected from the group consisting of glycerol, trimethylolpropane or pentaerythritol;
    C3-C20多元酸酯,优选为多元酸选自偏苯三酸或均苯四甲酸的C4-C10正构或异构醇酯;a C 3 -C 20 polybasic acid ester, preferably a C 4 -C 10 normal or isomeric alcohol ester of a polybasic acid selected from the group consisting of trimellitic acid or pyromellitic acid;
    具有如下结构式的聚亚烷氧基醚单酯:Polyalkoxy ether monoester having the following structural formula:
    Figure PCTCN2015092167-appb-100001
    Figure PCTCN2015092167-appb-100001
    其中n1为0或1-3中的整数,n2为1-3中的整数,R1为C4H9-、C5H11-、C6H13-或C7H15-中的一种,所述R2为C11H23-、C6H13-、C8H17-、C10H21-或C12H25-中的一种;Wherein n 1 is an integer of 0 or 1-3, n 2 is an integer of 1-3, and R 1 is C 4 H 9 -, C 5 H 11 -, C 6 H 13 - or C 7 H 15 - And R 2 is one of C 11 H 23 -, C 6 H 13 -, C 8 H 17 -, C 10 H 21 - or C 12 H 25 -;
    具有如下结构式的聚亚烷氧基醚双酯:Polyalkyleneoxyether diester having the following structural formula:
    Figure PCTCN2015092167-appb-100002
    Figure PCTCN2015092167-appb-100002
    其中m为1-3中的整数,R3和R4分别独立地选自C6H13-、C7H15-、C8H17-、C9H19-或C10H21-中的一种。Wherein m is an integer in 1-3, and R 3 and R 4 are each independently selected from C 6 H 13 -, C 7 H 15 -, C 8 H 17 -, C 9 H 19 - or C 10 H 21 - One kind.
  7. 根据权利要求6所述的基础油,其中,所述酯类油选自由十二烷酸二(2-乙基己基)酯、癸酸二(2-乙基己基)酯、硬脂酸甲酯、月桂酸异丁酯、月桂酸异戊酯、3-甲基-1,6-乙二醇二正辛酸酯、1,10-癸二醇二(2-乙基己基)酯、己二醇二异辛酸酯、己二酸二正辛酯、3-甲基己二酸二正辛酯、 己二酸二(2-乙基己基)酯、己二酸间甲基环己基二(2-乙基己基)酯、己二酸对甲基环己基二(2-乙基己基)酯、壬二酸二(2-乙基己基)酯、癸二酸二正丁酯、丙三醇三己酸酯、季戊四醇四己酸酯、三羟甲基丙烷三己酸酯和三羟甲基丙烷三戊酸酯、化学式为
    Figure PCTCN2015092167-appb-100003
    的聚亚烷氧基二醚双酯、以及具有如下化学式的聚亚烷氧基醚单酯组成的组,
    The base oil according to claim 6, wherein the ester oil is selected from the group consisting of di(2-ethylhexyl) dodecanoate, di(2-ethylhexyl) phthalate, and methyl stearate. , isobutyl laurate, isoamyl laurate, 3-methyl-1,6-ethylene glycol di-n-octanoate, 1,10-decanediol di(2-ethylhexyl) ester, hexane Alcohol diisooctanoate, di-n-octyl adipate, di-n-octyl 3-methyladipate, di(2-ethylhexyl) adipate, m-cyclohexyl di adipate 2-ethylhexyl) ester, p-methylcyclohexyl bis(2-ethylhexyl) adipate, di(2-ethylhexyl) sebacate, di-n-butyl sebacate, glycerol Trihexanoate, pentaerythritol tetrahexanoate, trimethylolpropane trihexanoate and trimethylolpropane trivalerate, the chemical formula is
    Figure PCTCN2015092167-appb-100003
    a polyalkyleneoxydiether diester, and a group of polyalkoxy ether monoesters having the following chemical formula,
    Figure PCTCN2015092167-appb-100004
    Figure PCTCN2015092167-appb-100004
  8. 根据权利要求1所述的基础油,其中,所述烷基苯油的40℃运动粘度为2-15mm2/s,优选为3-7mm2/s,The base oil according to claim 1, wherein the alkylbenzene oil has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, preferably 3 to 7 mm 2 /s,
    优选地,所述烷基苯油为癸基苯、十一烷基苯、十二烷基苯、十三烷基苯、十五烷基苯、以及十六烷基苯中的一种或两种及两种以上的混合物。Preferably, the alkyl benzene oil is one or two of mercaptobenzene, undecylbenzene, dodecylbenzene, tridecylbenzene, pentadecylbenzene, and hexadecylbenzene. And a mixture of two or more kinds.
  9. 根据权利要求1所述的基础油,其中,所述基础油还含有不同于烷基苯油的另一种烃类油,The base oil according to claim 1, wherein said base oil further contains another hydrocarbon oil different from alkyl benzene oil,
    优选地,所述不同于烷基苯油的另一种烃类油的40℃运动粘度在4mm2/s以下,倾点小于-30℃,沸点小于280℃;Preferably, the other hydrocarbon oil different from the alkyl benzene oil has a 40 ° C kinematic viscosity of 4 mm 2 /s or less, a pour point of less than -30 ° C, and a boiling point of less than 280 ° C;
    更优选地,以所述基础油的总量为基准,所述不同于烷基苯油的另一种烃类油的含量为0.1wt.%-20wt.%。More preferably, the content of the other hydrocarbon oil different from the alkylbenzene oil is from 0.1 wt.% to 20 wt.%, based on the total amount of the base oil.
  10. 根据权利要求9所述的基础油,其中,所述不同于烷基苯油的另一种烃类油选自费托合成异构烷烃、加氢异构烷烃、加氢裂化异构烷烃、聚α烯烃、烯烃叠合油、多烷基环戊烷、以及多烷基环己烷中的一种或多种。 The base oil according to claim 9, wherein the other hydrocarbon oil different from the alkylbenzene oil is selected from the group consisting of Fischer-Tropsch synthesis isoparaffins, hydroisomerized alkanes, hydrocracking isoparaffins, poly alpha One or more of an olefin, an olefinic superposed oil, a polyalkylcyclopentane, and a polyalkylcyclohexane.
  11. 一种冷冻机油组合物,该组合物含有基础油和添加剂,其特征在于,所述基础油为权利要求1-10中任意一项所述的冷冻机油组合物用基础油。A refrigerating machine oil composition, the composition comprising a base oil and an additive, wherein the base oil is the base oil for a refrigerating machine oil composition according to any one of claims 1 to 10.
  12. 根据权利要求11所述的组合物,其中,所述组合物120℃运动粘度与40℃运动粘度的比值为0.23-0.30,优选为0.24~0.29。The composition according to claim 11, wherein the ratio of the 120 ° C kinematic viscosity to the 40 ° C kinematic viscosity of the composition is from 0.23 to 0.30, preferably from 0.24 to 0.29.
  13. 根据权利要求12所述的组合物,其中,所述组合物40℃运动粘度在2~15mm2/s,优选为3~7mm2/s,闪点大于140℃,燃点大于150℃,倾点小于-50℃。The composition according to claim 12, wherein said composition has a kinematic viscosity at 40 ° C of 2 to 15 mm 2 /s, preferably 3 to 7 mm 2 /s, a flash point of more than 140 ° C, a flash point of more than 150 ° C, and a pour point. Less than -50 ° C.
  14. 根据权利要求11至13中任意一项所述的组合物,其中,以组合物的总量为基准,所述基础油的含量为94-98wt.%,所述添加剂的含量为2-6wt.%,The composition according to any one of claims 11 to 13, wherein the base oil is contained in an amount of from 94 to 98% by weight based on the total amount of the composition, and the additive is contained in an amount of from 2 to 6 % by weight. %,
    优选地,所述添加剂选自润滑剂、减摩剂、抗氧剂、抗腐蚀剂、抗泡剂中的一种或多种。Preferably, the additive is selected from one or more of a lubricant, an antifriction agent, an antioxidant, an anticorrosive agent, and an antifoaming agent.
  15. 一种用于制冷的组合物,该组合物含有冷冻机油组合物和制冷剂,其特征在于,所述冷冻机油组合物为权利要求11至14中任意一项所述的冷冻机油组合物。A composition for refrigeration, the composition comprising a refrigerating machine oil composition and a refrigerant, wherein the refrigerating machine oil composition is the refrigerating machine oil composition according to any one of claims 11 to 14.
  16. 根据权利要求15所述的组合物,其中,以所述组合物的总量为基准,所述冷冻机油组合物的含量为70-90wt.%,制冷剂的含量10-30wt.%,The composition according to claim 15, wherein the refrigerating machine oil composition is 70-90 wt.%, and the refrigerant content is 10-30 wt.%, based on the total amount of the composition.
    优选地,所述制冷剂为R600A、R290或R134A中的任意一种。 Preferably, the refrigerant is any one of R600A, R290 or R134A.
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