RU2008140146A - OIL OIL AND METHOD FOR PRODUCING OIL OIL - Google Patents

OIL OIL AND METHOD FOR PRODUCING OIL OIL Download PDF

Info

Publication number
RU2008140146A
RU2008140146A RU2008140146/04A RU2008140146A RU2008140146A RU 2008140146 A RU2008140146 A RU 2008140146A RU 2008140146/04 A RU2008140146/04 A RU 2008140146/04A RU 2008140146 A RU2008140146 A RU 2008140146A RU 2008140146 A RU2008140146 A RU 2008140146A
Authority
RU
Russia
Prior art keywords
fraction
specified
boiling point
petroleum oil
paraffin component
Prior art date
Application number
RU2008140146/04A
Other languages
Russian (ru)
Other versions
RU2425859C2 (en
Inventor
Юити ТАНАКА (JP)
Юити Танака
Синя ТАКАХАСИ (JP)
Синя Такахаси
Йосифуми ТИБА (JP)
Йосифуми ТИБА
Original Assignee
Ниппон Ойл Корпорейшн (Jp)
Ниппон Ойл Корпорейшн
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 Ниппон Ойл Корпорейшн (Jp), Ниппон Ойл Корпорейшн filed Critical Ниппон Ойл Корпорейшн (Jp)
Publication of RU2008140146A publication Critical patent/RU2008140146A/en
Application granted granted Critical
Publication of RU2425859C2 publication Critical patent/RU2425859C2/en

Links

Classifications

    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/14—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/12—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • 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
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/301—Boiling range

Abstract

1. Способ получения нефтяного масла, включающий стадии фракционирования синтетической нефти, полученной синтезом Фишера Тропша, таким образом, что полученная промежуточная фракция, обладающая содержанием фракции с точкой кипения от 150 до 360°С, не менее 90 мас.%, и содержанием фракции с точкой кипения не менее 350°С не более 5 мас.%, и парафинового компонента, который является более тяжелым, чем промежуточная фракция, и приведения во взаимодействие каждого из указанных промежуточной фракции и парафинового компонента с катализатором гидрообработки в присутствии водорода, их смешивания, и фракционирования, так чтобы получить нефтяное масло, обладающее содержанием фракции с точкой кипения от 150 до 360°С не менее 86 мас.% и содержанием фракции с точкой кипения не менее 350°С не менее 5 мас.%. ! 2. Способ получения нефтяного масла по п.1, в котором указанная промежуточная фракция подвергается гидрообработке таким образом, что содержание углеводородов с точкой кипения не более 150°С в указанной промежуточной фракции на 3-9% больше после взаимодействия с указанным катализатором гидрообработки, чем перед взаимодействием. ! 3. Способ получения нефтяного масла по п.1 или 2, где указанный парафиновый компонент подвергают гидрообработке таким образом, что содержание фракции с точкой кипения не более 360°С в указанном парафиновом компоненте после взаимодействия с указанным катализатором гидрообработки составляет от 45 до 85 мас.%. ! 4. Способ получения нефтяного масла по по п.1 или 2, в котором каждый из указанных катализаторов гидрообработки приводят в контакт с указанной промежуточной фракцией, и указанный катализатор гидрообработки прив� 1. A method of producing petroleum oil, comprising the stages of fractionation of synthetic oil obtained by Fischer Tropsch synthesis, so that the obtained intermediate fraction having a fraction with a boiling point of from 150 to 360 ° C, not less than 90 wt.%, And a fraction with a boiling point of not less than 350 ° C, not more than 5 wt.%, and a paraffin component, which is heavier than the intermediate fraction, and bringing into contact each of these intermediate fractions and the paraffin component with a hydrotreating catalyst webs in the presence of hydrogen, their mixing, and fractionation, so as to obtain petroleum oil having a fraction with a boiling point of 150 to 360 ° C of at least 86 wt.% and a fraction with a boiling point of at least 350 ° C of at least 5 wt. .%. ! 2. The method of producing petroleum oil according to claim 1, wherein said intermediate fraction is hydrotreated in such a way that the content of hydrocarbons with a boiling point of not more than 150 ° C in said intermediate fraction is 3-9% higher after interaction with said hydrotreatment catalyst than before the interaction. ! 3. The method of producing petroleum oil according to claim 1 or 2, where the specified paraffin component is subjected to hydroprocessing so that the content of the fraction with a boiling point of not more than 360 ° C in the specified paraffin component after interaction with the specified hydroprocessing catalyst is from 45 to 85 wt. % ! 4. The method of producing petroleum oil according to claim 1 or 2, in which each of these hydrotreatment catalysts is brought into contact with the specified intermediate fraction, and the specified hydrotreatment catalyst

Claims (6)

1. Способ получения нефтяного масла, включающий стадии фракционирования синтетической нефти, полученной синтезом Фишера Тропша, таким образом, что полученная промежуточная фракция, обладающая содержанием фракции с точкой кипения от 150 до 360°С, не менее 90 мас.%, и содержанием фракции с точкой кипения не менее 350°С не более 5 мас.%, и парафинового компонента, который является более тяжелым, чем промежуточная фракция, и приведения во взаимодействие каждого из указанных промежуточной фракции и парафинового компонента с катализатором гидрообработки в присутствии водорода, их смешивания, и фракционирования, так чтобы получить нефтяное масло, обладающее содержанием фракции с точкой кипения от 150 до 360°С не менее 86 мас.% и содержанием фракции с точкой кипения не менее 350°С не менее 5 мас.%.1. A method of producing petroleum oil, comprising the stages of fractionation of synthetic oil obtained by Fischer Tropsch synthesis, so that the obtained intermediate fraction having a fraction with a boiling point of from 150 to 360 ° C, not less than 90 wt.%, And a fraction with a boiling point of not less than 350 ° C, not more than 5 wt.%, and a paraffin component, which is heavier than the intermediate fraction, and bringing into contact each of these intermediate fractions and the paraffin component with a hydrotreating catalyst webs in the presence of hydrogen, their mixing, and fractionation, so as to obtain petroleum oil having a fraction with a boiling point of 150 to 360 ° C of at least 86 wt.% and a fraction with a boiling point of at least 350 ° C of at least 5 wt. .%. 2. Способ получения нефтяного масла по п.1, в котором указанная промежуточная фракция подвергается гидрообработке таким образом, что содержание углеводородов с точкой кипения не более 150°С в указанной промежуточной фракции на 3-9% больше после взаимодействия с указанным катализатором гидрообработки, чем перед взаимодействием.2. The method of producing petroleum oil according to claim 1, wherein said intermediate fraction is hydrotreated in such a way that the content of hydrocarbons with a boiling point of not more than 150 ° C in said intermediate fraction is 3-9% higher after interaction with said hydrotreatment catalyst than before the interaction. 3. Способ получения нефтяного масла по п.1 или 2, где указанный парафиновый компонент подвергают гидрообработке таким образом, что содержание фракции с точкой кипения не более 360°С в указанном парафиновом компоненте после взаимодействия с указанным катализатором гидрообработки составляет от 45 до 85 мас.%.3. The method of producing petroleum oil according to claim 1 or 2, where the specified paraffin component is subjected to hydroprocessing so that the content of the fraction with a boiling point of not more than 360 ° C in the specified paraffin component after interaction with the specified hydroprocessing catalyst is from 45 to 85 wt. % 4. Способ получения нефтяного масла по по п.1 или 2, в котором каждый из указанных катализаторов гидрообработки приводят в контакт с указанной промежуточной фракцией, и указанный катализатор гидрообработки приводят в контакт с указанным парафиновым компонентом, включает носитель, содержащий от 0,1 до 80,0 мас.% кристаллического цеолита и от 0,1 до 60,0 мас.% жаростойкого аморфного оксида металла, и, по меньшей мере, один металл, выбранный из группы металлов, принадлежащих к VIII группе периодической таблицы, нанесенный на носитель.4. The method of producing petroleum oil according to claim 1 or 2, in which each of these hydrotreatment catalysts is brought into contact with the specified intermediate fraction, and said hydrotreatment catalyst is brought into contact with the specified paraffin component, includes a carrier containing from 0.1 to 80.0 wt.% Crystalline zeolite and from 0.1 to 60.0 wt.% Heat-resistant amorphous metal oxide, and at least one metal selected from the group of metals belonging to group VIII of the periodic table, deposited on a carrier. 5. Способ получения нефтяного масла по по п.1 или 2, где указанную промежуточную фракцию приводят в контакт с указанным катализатором гидрообработки при температуре реакции от 200 до 370°С, парциальном давлении водорода от 1,0 до 5,0 МПа и часовой объемной скорости жидкости от 0,3 до 3,5 ч-1, и указанный парафиновый компонент приводят в контакт с указанным катализатором гидрообработки при температуре реакции от 200 до 370°С, парциальном давлении водорода от 1,0 до 5,0 МПа и часовой объемной скорости жидкости от 0,3 до 3,5 ч-1.5. The method of producing petroleum oil according to claim 1 or 2, where the specified intermediate fraction is brought into contact with the specified hydrotreatment catalyst at a reaction temperature of from 200 to 370 ° C, a partial pressure of hydrogen from 1.0 to 5.0 MPa and hourly volumetric a fluid velocity of from 0.3 to 3.5 h −1 , and said paraffin component is brought into contact with said hydrotreatment catalyst at a reaction temperature of 200 to 370 ° C., a partial pressure of hydrogen of 1.0 to 5.0 MPa, and an hourly volumetric fluid speeds from 0.3 to 3.5 h -1 . 6. Нефтяное масло, полученное способом получения по любому из пп.1-5, обладающее температурой потери текучести не более -7,5°С и кинематической вязкостью при 30°С не менее 2,5 мм2/с. 6. Petroleum oil obtained by the production method according to any one of claims 1 to 5, having a pour point of not more than -7.5 ° C and a kinematic viscosity at 30 ° C of not less than 2.5 mm 2 / s.
RU2008140146/04A 2006-03-10 2007-02-14 Petroleum oil and petroleum oil obtaining method RU2425859C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2006-066465 2006-03-10
JP2006066465A JP4908022B2 (en) 2006-03-10 2006-03-10 Method for producing hydrocarbon oil and hydrocarbon oil

Publications (2)

Publication Number Publication Date
RU2008140146A true RU2008140146A (en) 2010-04-20
RU2425859C2 RU2425859C2 (en) 2011-08-10

Family

ID=38509238

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2008140146/04A RU2425859C2 (en) 2006-03-10 2007-02-14 Petroleum oil and petroleum oil obtaining method

Country Status (6)

Country Link
JP (1) JP4908022B2 (en)
CN (1) CN101400768B (en)
AU (1) AU2007226057B2 (en)
MY (1) MY148585A (en)
RU (1) RU2425859C2 (en)
WO (1) WO2007105400A1 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4908037B2 (en) * 2006-03-30 2012-04-04 Ｊｘ日鉱日石エネルギー株式会社 Method for treating synthetic oil, hydrocarbon oil for kerosene smoke point improver and hydrocarbon oil for diesel fuel base material
US8597502B2 (en) 2007-09-28 2013-12-03 Japan Oil, Gas And Metals National Corporation Method of manufacturing diesel fuel base stock and diesel fuel base stock thereof
WO2009041478A1 (en) 2007-09-28 2009-04-02 Japan Oil, Gas And Metals National Corporation Process for producing diesel fuel
US8163168B2 (en) * 2008-07-25 2012-04-24 Exxonmobil Research And Engineering Company Process for flexible vacuum gas oil conversion
WO2015044279A1 (en) * 2013-09-30 2015-04-02 Shell Internationale Research Maatschappij B.V. Fischer-tropsch derived gas oil fraction
CN105579561A (en) * 2013-09-30 2016-05-11 国际壳牌研究有限公司 Fischer-tropsch derived gas oil fraction
BR112016006763A2 (en) * 2013-09-30 2017-08-01 Shell Int Research fischer-tropsch derived fuel oil fraction, functional fluid formulation, and use of a fischer-tropsch derived fuel oil fraction
US20160230100A1 (en) * 2013-09-30 2016-08-11 Shell Oil Company Fischer-tropsch derived gas oil fraction
EP3052596A1 (en) * 2013-09-30 2016-08-10 Shell Internationale Research Maatschappij B.V. Fischer-tropsch derived gas oil fraction
WO2015044278A1 (en) * 2013-09-30 2015-04-02 Shell Internationale Research Maatschappij B.V. Fischer-tropsch derived gas oil
CN104673384B (en) * 2015-03-02 2016-09-14 武汉凯迪工程技术研究总院有限公司 A kind of hydrofinishing process of Low Temperature Fischer Tropsch full distillate oil fecund intermediate oil
CN104673383B (en) * 2015-03-03 2016-12-07 上海兖矿能源科技研发有限公司 A kind of method being produced high melting-point wax by Fischer-Tropsch synthetic

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NZ204088A (en) * 1982-05-18 1986-03-14 Mobil Oil Corp Catalytic isomerisation of long chain n-paraffins
US4919786A (en) * 1987-12-18 1990-04-24 Exxon Research And Engineering Company Process for the hydroisomerization of was to produce middle distillate products (OP-3403)
US5689031A (en) * 1995-10-17 1997-11-18 Exxon Research & Engineering Company Synthetic diesel fuel and process for its production
US5866748A (en) * 1996-04-23 1999-02-02 Exxon Research And Engineering Company Hydroisomerization of a predominantly N-paraffin feed to produce high purity solvent compositions
US5814109A (en) * 1997-02-07 1998-09-29 Exxon Research And Engineering Company Diesel additive for improving cetane, lubricity, and stability
WO2000020534A1 (en) * 1998-10-05 2000-04-13 Sasol Technology (Pty.) Ltd. Biodegradable middle distillates and production thereof
US6458265B1 (en) * 1999-12-29 2002-10-01 Chevrontexaco Corporation Diesel fuel having a very high iso-paraffin to normal paraffin mole ratio
JP3963311B2 (en) * 2002-06-14 2007-08-22 株式会社ジャパンエナジー Refrigerator oil composition
AU2003266527A1 (en) * 2002-09-24 2004-04-19 Nippon Oil Corporation Hydrocracking catalyst and process for production of liquid hydrocarbons
FR2850393B1 (en) * 2003-01-27 2005-03-04 Inst Francais Du Petrole PROCESS FOR THE PRODUCTION OF MEDIUM DISTILLATES BY HYDROISOMERIZATION AND HYDROCRACKING OF FISCHER-TROPSCH PROCESS
CN100413946C (en) * 2003-09-03 2008-08-27 国际壳牌研究有限公司 Fuel compositions comprising fischer-tropsch derived fuel
JP4313237B2 (en) * 2004-03-29 2009-08-12 新日本石油株式会社 Hydrocracking catalyst and method for producing liquid hydrocarbon
JP5180427B2 (en) * 2004-06-01 2013-04-10 出光興産株式会社 Hydrocracking catalyst for waxy feedstock

Also Published As

Publication number Publication date
AU2007226057B2 (en) 2011-12-01
JP2007238870A (en) 2007-09-20
JP4908022B2 (en) 2012-04-04
RU2425859C2 (en) 2011-08-10
AU2007226057A1 (en) 2007-09-20
CN101400768A (en) 2009-04-01
MY148585A (en) 2013-04-30
WO2007105400A1 (en) 2007-09-20
CN101400768B (en) 2012-08-22

Similar Documents

Publication Publication Date Title
RU2008140146A (en) OIL OIL AND METHOD FOR PRODUCING OIL OIL
JP4416742B2 (en) Production of biodegradable middle distillates
TW523545B (en) Production of synthetic lubricant and lubricant base stock without dewaxing
KR101090939B1 (en) Base oil
EP2847302B1 (en) Process for making high vi lubricating oils
JP5290912B2 (en) Method for producing lubricating base oil
JP2002527530A (en) Isoparaffinic base oil produced by dewaxing Fischer-Tropsch wax hydroisomerized oil with Pt / H-mordenite
EP0876446A1 (en) Biodegradable high performance hydrocarbon base oils
RU2009117176A (en) METHODS FOR PRODUCING RAW PRODUCT AND ITS COMPOSITIONS
KR102359499B1 (en) Process for the production of hydrocarbon fluids having a low aromatic and sulfur content
RU2010150300A (en) CATALYTIC SYSTEM AND METHOD FOR HYDROPROCESSING HEAVY OILS
CN101760236B (en) Method for producing lube base oil
CN105316036A (en) Method of producing ultrahigh-viscosity-index lubricant base oil
RU2011143807A (en) METHOD FOR PRODUCING BASIC OIL FOR LUBRICANTS
CN110003947B (en) Process for producing low slack wax and high viscosity index base oil
RU2011132002A (en) METHODS FOR HYDROCRACKING WITH PRODUCTION OF A HYDROISOMERIZED PRODUCT FOR BASIC COMPONENTS OF LUBRICANTS
CN109321273B (en) Method and device for producing naphthenic base refrigerator oil base oil
WO2007143435A3 (en) Process for producing light neutral base oil having a high viscosity index
RU2008136837A (en) METHOD FOR HYDROGENING SYNTHETIC OIL AND METHOD FOR PRODUCING BASIC FUEL
CN106999914B (en) Alternate preparation of distillate fuel and lube base stocks
JP2002317190A (en) Mineral oil based lubricating oil base oil
CN111378494A (en) Processing method of Fischer-Tropsch synthetic oil
CN110540873A (en) Method for processing naphthenic oil
CN105219427A (en) A kind of working method of lubricant base
WO2008087897A1 (en) Processes for production of liquid fuel

Legal Events

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

Effective date: 20180215