[go: up one dir, main page]

RU2010109387A - LUBRICANT OIL MIX AND ITS PRODUCTION METHOD - Google Patents

LUBRICANT OIL MIX AND ITS PRODUCTION METHOD Download PDF

Info

Publication number
RU2010109387A
RU2010109387A RU2010109387/04A RU2010109387A RU2010109387A RU 2010109387 A RU2010109387 A RU 2010109387A RU 2010109387/04 A RU2010109387/04 A RU 2010109387/04A RU 2010109387 A RU2010109387 A RU 2010109387A RU 2010109387 A RU2010109387 A RU 2010109387A
Authority
RU
Russia
Prior art keywords
base oil
component
carbon atoms
mixture according
oil mixture
Prior art date
Application number
RU2010109387/04A
Other languages
Russian (ru)
Other versions
RU2494140C2 (en
Inventor
Жильбер Робер Бернар ЖЕРМЕН (FR)
Жильбер Робер Бернар Жермен
Дейвид Джон УЭДЛОК (GB)
Дейвид Джон УЭДЛОК
Original Assignee
Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL)
Шелл Интернэшнл Рисерч Маатсхаппий Б.В.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL), Шелл Интернэшнл Рисерч Маатсхаппий Б.В. filed Critical Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL)
Publication of RU2010109387A publication Critical patent/RU2010109387A/en
Application granted granted Critical
Publication of RU2494140C2 publication Critical patent/RU2494140C2/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M111/00—Lubrication 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
    • C10M111/04—Lubrication 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 macromolecular organic compound
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M177/00—Special methods of preparation of lubricating compositions; Chemical modification by after-treatment of components or of the whole of a lubricating composition, not covered by other classes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1022—Fischer-Tropsch products
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/301—Boiling range
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/302—Viscosity
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/304—Pour point, cloud point, cold flow properties
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/308—Gravity, density, e.g. API
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/10—Lubricating oil
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10—Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/1006—Petroleum or coal fractions, e.g. tars, solvents, bitumen used as base material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/17—Fisher Tropsch reaction products
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/17—Fisher Tropsch reaction products
    • C10M2205/173—Fisher Tropsch reaction products used as base material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01—Physico-chemical properties
    • C10N2020/011—Cloud point
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01—Physico-chemical properties
    • C10N2020/02—Viscosity; Viscosity index
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01—Physico-chemical properties
    • C10N2020/071—Branched chain compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/02—Pour-point; Viscosity index
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/70—Soluble oils
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2070/00—Specific manufacturing methods for lubricant compositions

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

1. Смесь смазочного базового масла, содержащая ! (a) произведенное из минеральной нефти базовое масло, имеющее содержание насыщенных соединений больше, чем 90 мас.%, содержание серы меньше, чем 0,03 мас.%, и индекс вязкости между 80 и 150, и ! (b) компонент парафинового базового масла, имеющий вязкость при 100°С от 7 до 30 сСт (от 7 до 30 мм2/с), где компонент (b) представляет собой изомеризованный остаточный продукт, полученный в синтезе Фишера-Тропша и имеющий отношение процентной доли вторичных метиленовых атомов углерода, которые удалены на четыре или более атомов углерода от концевой группы, и ответвление к процентной доле изопропильных атомов углерода, найденное с использованием метода 13С-ЯМР, меньше 8,2. ! 2. Смесь базового масла по п.1, в которой компонент (а) базового масла минерального происхождения присутствует в количестве от 40 мас.% до 95 мас.% в расчете на суммарную массу масляной смеси. ! 3. Смесь базового масла по п.1 или 2, которая имеет кинематическую вязкость при 100°С больше, чем 12,0 сСт, и индекс вязкости больше, чем 95. ! 4. Смесь базового масла по п.1 или 2, в которой индекс вязкости компонента (а) составляет между 100 и 110. ! 5. Смесь базового масла по п.1 или 2, в которой температура помутнения смеси имеет значение ниже 0°С. ! 6. Смесь базового масла по п.1 или 2, в которой компонент (а) базового масла представляет собой базовые масла API групп II и/или API группы III, которые определены в публикации API 1509. ! 7. Смесь базового масла по п.1 или 2, в которой компонент (b) имеет температуру потери текучести ниже -28°С. ! 8. Способ получения смеси смазочного базового масла, который включает смешивание ! (a) произведенного из минеральной нефти базового масла, им 1. A lubricating base oil mixture containing! (a) a mineral oil base oil having a saturated content of more than 90 wt.%, a sulfur content of less than 0.03 wt.%, and a viscosity index between 80 and 150, and! (b) a paraffin base oil component having a viscosity at 100 ° C. of 7 to 30 cSt (7 to 30 mm2 / s), where component (b) is a Fischer-Tropsch derived isomerized residual product and having a percentage ratio the fraction of secondary methylene carbon atoms that are four or more carbon atoms away from the end group and the branch to the percentage of isopropyl carbon atoms found using the 13C-NMR method is less than 8.2. ! 2. The base oil mixture according to claim 1, in which component (a) of the base oil of mineral origin is present in an amount of from 40 wt.% To 95 wt.% Based on the total weight of the oil mixture. ! 3. The base oil mixture according to claim 1 or 2, which has a kinematic viscosity at 100 ° C. of greater than 12.0 cSt, and a viscosity index greater than 95.! 4. The base oil mixture according to claim 1 or 2, in which the viscosity index of component (a) is between 100 and 110.! 5. The base oil mixture according to claim 1 or 2, in which the cloud point of the mixture has a value below 0 ° C. ! 6. The base oil mixture according to claim 1 or 2, wherein the base oil component (a) is an API group II base oil and / or group III API as defined in API publication 1509.! 7. The base oil mixture according to claim 1 or 2, in which component (b) has a pour point below -28 ° C. ! 8. A method of obtaining a mixture of lubricating base oil, which includes mixing! (a) a base oil derived from mineral oil;

Claims (10)

1. Смесь смазочного базового масла, содержащая1. A lubricating base oil mixture containing (a) произведенное из минеральной нефти базовое масло, имеющее содержание насыщенных соединений больше, чем 90 мас.%, содержание серы меньше, чем 0,03 мас.%, и индекс вязкости между 80 и 150, и(a) a mineral oil derived base oil having a saturated content of more than 90 wt.%, a sulfur content of less than 0.03 wt.%, and a viscosity index between 80 and 150, and (b) компонент парафинового базового масла, имеющий вязкость при 100°С от 7 до 30 сСт (от 7 до 30 мм2/с), где компонент (b) представляет собой изомеризованный остаточный продукт, полученный в синтезе Фишера-Тропша и имеющий отношение процентной доли вторичных метиленовых атомов углерода, которые удалены на четыре или более атомов углерода от концевой группы, и ответвление к процентной доле изопропильных атомов углерода, найденное с использованием метода 13С-ЯМР, меньше 8,2.(b) a paraffin base oil component having a viscosity at 100 ° C. of 7 to 30 cSt (7 to 30 mm 2 / s), where component (b) is an isomerized residual product obtained in a Fischer-Tropsch synthesis and having a ratio the percentage of secondary methylene carbon atoms that are four or more carbon atoms away from the end group and the branch to the percentage of isopropyl carbon atoms found using 13 C-NMR is less than 8.2. 2. Смесь базового масла по п.1, в которой компонент (а) базового масла минерального происхождения присутствует в количестве от 40 мас.% до 95 мас.% в расчете на суммарную массу масляной смеси.2. The base oil mixture according to claim 1, in which component (a) of the base oil of mineral origin is present in an amount of from 40 wt.% To 95 wt.% Based on the total weight of the oil mixture. 3. Смесь базового масла по п.1 или 2, которая имеет кинематическую вязкость при 100°С больше, чем 12,0 сСт, и индекс вязкости больше, чем 95.3. The base oil mixture according to claim 1 or 2, which has a kinematic viscosity at 100 ° C. of greater than 12.0 cSt, and a viscosity index of greater than 95. 4. Смесь базового масла по п.1 или 2, в которой индекс вязкости компонента (а) составляет между 100 и 110.4. The base oil mixture according to claim 1 or 2, in which the viscosity index of component (a) is between 100 and 110. 5. Смесь базового масла по п.1 или 2, в которой температура помутнения смеси имеет значение ниже 0°С.5. The base oil mixture according to claim 1 or 2, in which the cloud point of the mixture has a value below 0 ° C. 6. Смесь базового масла по п.1 или 2, в которой компонент (а) базового масла представляет собой базовые масла API групп II и/или API группы III, которые определены в публикации API 1509.6. The base oil mixture according to claim 1 or 2, wherein the base oil component (a) is an API group II base oil and / or group III API as defined in API publication 1509. 7. Смесь базового масла по п.1 или 2, в которой компонент (b) имеет температуру потери текучести ниже -28°С.7. The base oil mixture according to claim 1 or 2, in which component (b) has a pour point below -28 ° C. 8. Способ получения смеси смазочного базового масла, который включает смешивание8. A method of obtaining a mixture of lubricating base oil, which includes mixing (a) произведенного из минеральной нефти базового масла, имеющего содержание насыщенных соединений больше, чем 90 мас.%, содержание серы меньше чем 0,03 мас.%, и индекс вязкости между 80 и 150, и(a) a mineral oil-derived base oil having a saturated content of more than 90 wt.%, a sulfur content of less than 0.03 wt.%, and a viscosity index between 80 and 150, and (b) компонента парафинового базового масла, имеющего вязкость при 100°С от 7 до 30 сСт (от 7 до 30 мм2/с), где компонент (b) представляет собой изомеризованный остаточный продукт, полученный в синтезе Фишера-Тропша и имеющий отношение процентной доли вторичных метиленовых атомов углерода, которые удалены на четыре или более атомов углерода от концевой группы, и ответвление к процентной доле изопропильных атомов углерода, найденное с использованием метода 13С-ЯМР, меньше 8,2.(b) a paraffin base oil component having a viscosity at 100 ° C. of 7 to 30 cSt (7 to 30 mm 2 / s), where component (b) is a Fischer-Tropsch derived isomerized residual product and having a ratio the percentage of secondary methylene carbon atoms that are four or more carbon atoms away from the end group and the branch to the percentage of isopropyl carbon atoms found using 13 C-NMR is less than 8.2. 9. Способ по п.9, в котором компонент (b) имеет среднюю степень разветвления в молекулах свыше 10 алкильных разветвлений на 100 атомов углерода.9. The method according to claim 9, in which component (b) has an average degree of branching in the molecules of more than 10 alkyl branches per 100 carbon atoms. 10. Способ по любому из пп.8 и 9, в котором парафиновый компонент (b) базового масла является тяжелой остаточной фракцией после дистилляции воска, произведенного в синтезе Фишера-Тропша, или парафинового рафинатного сырья, полученного путем:10. The method according to any of paragraphs.8 and 9, in which the paraffin component (b) of the base oil is a heavy residual fraction after distillation of the wax produced in the Fischer-Tropsch synthesis, or paraffin raffinate feedstock obtained by: (а) гидрокрекинга/гидроизомеризации сырья, произведенного в синтезе Фишера-Тропша, в котором весовое отношение соединений, имеющих, по меньшей мере, 60 или больше атомов углерода, и соединений, имеющих, по меньшей мере, 30 атомов углерода в сырье, произведенном в синтезе Фишера-Тропша, составляет, по меньшей мере, 0,2, и в котором, по меньшей мере, 30 мас.% соединений в сырье, произведенном в синтезе Фишера-Тропша, имеет, по меньшей мере, 30 атомов углерода;(a) hydrocracking / hydroisomerization of a Fischer-Tropsch derived feedstock in which the weight ratio of compounds having at least 60 or more carbon atoms and compounds having at least 30 carbon atoms in the feed produced Fischer-Tropsch synthesis, is at least 0.2, and in which at least 30 wt.% of the compounds in the raw materials produced in the Fischer-Tropsch synthesis, has at least 30 carbon atoms; (b) разделения продукта стадии (а) на одну или несколько дистиллятных фракций низкокипящих фракций и широкую фракцию предшественника базового масла, и такую тяжелую фракцию, в которой точка выкипания 90 мас.% фракции - предшественника базового масла находится между 350 и 550°С;(b) separating the product of step (a) into one or more distillate fractions of low boiling fractions and a broad fraction of the base oil precursor, and such a heavy fraction in which the boiling point of 90 wt.% of the base oil precursor fraction is between 350 and 550 ° C; (c) осуществляют обработку полученной на стадии (b) широкой фракции - предшественника базового масла на стадии снижения температуры потери текучести; и(c) carry out the processing obtained in stage (b) a wide fraction of the precursor of the base oil at the stage of lowering the temperature of the fluidity loss; and (d) выделяют тяжелую остаточную фракцию путем дистилляции продукта стадии (с). (d) a heavy residual fraction is isolated by distillation of the product of step (c).
RU2010109387/04A 2007-08-13 2008-08-12 Lubricating oil composition and method for production thereof RU2494140C2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP07114257.4 2007-08-13
EP07114257 2007-08-13
PCT/EP2008/060599 WO2009021958A2 (en) 2007-08-13 2008-08-12 Lubricating base oil blend

Publications (2)

Publication Number Publication Date
RU2010109387A true RU2010109387A (en) 2011-09-20
RU2494140C2 RU2494140C2 (en) 2013-09-27

Family

ID=39135175

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2010109387/04A RU2494140C2 (en) 2007-08-13 2008-08-12 Lubricating oil composition and method for production thereof

Country Status (8)

Country Link
US (1) US20110290702A1 (en)
EP (1) EP2176388A2 (en)
JP (1) JP2010535925A (en)
CN (1) CN101796170B (en)
BR (1) BRPI0814956A2 (en)
RU (1) RU2494140C2 (en)
SG (1) SG183713A1 (en)
WO (1) WO2009021958A2 (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150060329A1 (en) * 2012-04-04 2015-03-05 Shell Oil Company Process to prepare residual base oil
US9284500B2 (en) * 2013-03-14 2016-03-15 Exxonmobil Research And Engineering Company Production of base oils from petrolatum
US20150099675A1 (en) * 2013-10-03 2015-04-09 Exxonmobil Research And Engineering Company Compositions with improved varnish control properties
US20170044460A1 (en) * 2014-04-25 2017-02-16 The Lubrizol Corporation Multigrade lubricating compositions
WO2016074985A1 (en) * 2014-11-12 2016-05-19 Shell Internationale Research Maatschappij B.V. Lubricating oil composition
JP6502149B2 (en) * 2015-04-06 2019-04-17 Ｅｍｇルブリカンツ合同会社 Lubricating oil composition
EP3371281B1 (en) 2015-11-04 2021-02-24 Purify Founders, LLC Fuel additive composition and related methods and compositions
BR112018010648B1 (en) * 2015-11-24 2020-11-17 Shell Internationale Research Maatschappij B.V. method to improve the release of air from a lubricating oil into a hydraulic system
CN106908467A (en) * 2015-12-23 2017-06-30 中国石油天然气股份有限公司 Analytical method for determining the sequence distribution and degree of long-chain branching of long-chain branched EPDM rubber
US10590360B2 (en) * 2015-12-28 2020-03-17 Exxonmobil Research And Engineering Company Bright stock production from deasphalted oil
FI128090B (en) 2016-12-22 2019-09-13 Neste Oyj Hydraulic fluid composition
JP2020525614A (en) * 2017-06-30 2020-08-27 エクソンモービル リサーチ アンド エンジニアリング カンパニーＥｘｘｏｎ Ｒｅｓｅａｒｃｈ Ａｎｄ Ｅｎｇｉｎｅｅｒｉｎｇ Ｃｏｍｐａｎｙ 13C-NMR-based compositions of high quality lubricating oil base oils, and methods enabling their design and manufacture, and their performance in finished lubricating oils
CN108441292A (en) * 2018-02-28 2018-08-24 河南道骐汽车科技有限公司 A kind of long-life environment-friendly type steam turbine oil
CN116376622B (en) * 2023-04-06 2024-12-03 国家能源集团宁夏煤业有限责任公司 Coal-based engine oil and its application

Family Cites Families (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6090989A (en) * 1997-10-20 2000-07-18 Mobil Oil Corporation Isoparaffinic lube basestock compositions
CN1286953C (en) * 2000-07-17 2006-11-29 国际壳牌研究有限公司 Method for preparing water-white lubricating oil base oil
RU2278147C2 (en) * 2001-04-19 2006-06-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Method of production of the base oil with the high content of the saturated hydrocarbons
CA2499405A1 (en) * 2002-10-08 2004-04-22 Exxonmobil Research And Engineering Company Heavy hydrocarbon composition with utility as a heavy lubricant base stock
US7053254B2 (en) * 2003-11-07 2006-05-30 Chevron U.S.A, Inc. Process for improving the lubricating properties of base oils using a Fischer-Tropsch derived bottoms
EP1548088A1 (en) * 2003-12-23 2005-06-29 Shell Internationale Researchmaatschappij B.V. Process to prepare a haze free base oil
US7655132B2 (en) * 2004-05-04 2010-02-02 Chevron U.S.A. Inc. Process for improving the lubricating properties of base oils using isomerized petroleum product
US7473345B2 (en) * 2004-05-19 2009-01-06 Chevron U.S.A. Inc. Processes for making lubricant blends with low Brookfield viscosities
US7273834B2 (en) * 2004-05-19 2007-09-25 Chevron U.S.A. Inc. Lubricant blends with low brookfield viscosities
US7384536B2 (en) * 2004-05-19 2008-06-10 Chevron U.S.A. Inc. Processes for making lubricant blends with low brookfield viscosities
US7572361B2 (en) * 2004-05-19 2009-08-11 Chevron U.S.A. Inc. Lubricant blends with low brookfield viscosities
US20060219597A1 (en) * 2005-04-05 2006-10-05 Bishop Adeana R Paraffinic hydroisomerate as a wax crystal modifier
JP4764070B2 (en) * 2005-05-24 2011-08-31 本田技研工業株式会社 Work station safety system
US20080053868A1 (en) * 2005-06-22 2008-03-06 Chevron U.S.A. Inc. Engine oil compositions and preparation thereof
US7687445B2 (en) * 2005-06-22 2010-03-30 Chevron U.S.A. Inc. Lower ash lubricating oil with low cold cranking simulator viscosity
EP1896556B1 (en) * 2005-06-23 2018-09-26 Shell International Research Maatschappij B.V. Oxidative stable oil formulation
US8318002B2 (en) * 2005-12-15 2012-11-27 Exxonmobil Research And Engineering Company Lubricant composition with improved solvency
US20080128322A1 (en) * 2006-11-30 2008-06-05 Chevron Oronite Company Llc Traction coefficient reducing lubricating oil composition
US20090001330A1 (en) * 2007-06-28 2009-01-01 Chevron U.S.A. Inc. Electrical Insulating Oil Compositions and Preparation Thereof
US20090036337A1 (en) * 2007-07-31 2009-02-05 Chevron U.S.A. Inc. Electrical Insulating Oil Compositions and Preparation Thereof
US20090088352A1 (en) * 2007-09-27 2009-04-02 Chevron U.S.A. Inc. Tractor hydraulic fluid compositions and preparation thereof
US20090163391A1 (en) * 2007-12-20 2009-06-25 Chevron U.S.A. Inc. Power Transmission Fluid Compositions and Preparation Thereof

Also Published As

Publication number Publication date
WO2009021958A3 (en) 2009-04-30
BRPI0814956A2 (en) 2015-02-03
RU2494140C2 (en) 2013-09-27
CN101796170A (en) 2010-08-04
WO2009021958A2 (en) 2009-02-19
CN101796170B (en) 2014-07-02
US20110290702A1 (en) 2011-12-01
JP2010535925A (en) 2010-11-25
SG183713A1 (en) 2012-09-27
EP2176388A2 (en) 2010-04-21

Similar Documents

Publication Publication Date Title
RU2010109387A (en) LUBRICANT OIL MIX AND ITS PRODUCTION METHOD
AU769075B2 (en) Novel hydrocarbon base oil for lubricants with very high viscosity index
WO2021094657A1 (en) Method for producing renewable fuel and base oil
JP2005507014A5 (en)
CN101910378B (en) fuel composition
CN101591584B (en) Water-base lubricant and preparation method thereof
CZ299839B6 (en) Liquid hydrocarbon composition, lubricant basestock composition and lubricating oil composition
MY154529A (en) Lubricant base oils and lubricant compositions and methods for making them
US9115327B2 (en) Base oil upgrading by co-feeding a ketone or beta-keto-ester feedstock
JP2023027759A (en) High quality lubricant oil manufacturing process utilizing waste lubricant oil purification fraction
WO2013181510A2 (en) Process for producing ketones from fattyacids
RU2658914C2 (en) Lubricating oil compositions comprising heavy fischer-tropsch derived and alkylated aromatic base oil
JP2025015401A (en) Lubricating base oil manufacturing process utilizing waste lubricating oil purification fraction, and lubricating base oil manufactured thereby
RU2604070C1 (en) Method of producing high-index components of base oils
RU2019137575A (en) COMBUSTION ENGINE LUBRICATING OIL COMPOSITION
RU2011143807A (en) METHOD FOR PRODUCING BASIC OIL FOR LUBRICANTS
CN119317689A (en) Hydrocarbon components
WO2014157383A1 (en) Lubricating oil composition
US20250026997A1 (en) Method of producing lube base oil and lube base oil produced thereby
CN112940829A (en) Antiwear hydraulic oil and preparation method thereof
JP2011506632A (en) Base oil formulation
JP6279986B2 (en) Light oil composition
JP5342206B2 (en) Method for producing hydrocarbon composition, hydrocarbon composition, lubricating base oil, lubricating oil composition
CA3155328C (en) Method for producing renewable fuel and base oil
JP7690304B2 (en) lubricating oil composition

Legal Events

Date Code Title Description
MM4A The patent is invalid due to non-payment of fees

Effective date: 20170813