MY148585A - Process for production of hydrocarbon oil and hydrocarbon oil - Google Patents
Process for production of hydrocarbon oil and hydrocarbon oilInfo
- Publication number
- MY148585A MY148585A MYPI20083399A MY148585A MY 148585 A MY148585 A MY 148585A MY PI20083399 A MYPI20083399 A MY PI20083399A MY 148585 A MY148585 A MY 148585A
- Authority
- MY
- Malaysia
- Prior art keywords
- fraction
- hydrocarbon oil
- less
- mass
- content
- Prior art date
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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A HYDROCARBON OIL MANUFACTURING METHOD COMPRISES FRACTIONATING A SYNTHETIC OIL OBTAINED THROUGH FISCHER-TROPSCH SYNTHESIS, SO AS TO OBTAIN A MIDDLE FRACTION HAVING A CONTENT OF A FRACTION OF BOILING POINT 150 TO 360�C OF NOT LESS THAN 90 MASS% AND A CONTENT OF A FRACTION OF BOILING POINT NOT LESS THAN 350�C OF NOT MORE THAN 5 MASS%, AND A WAX COMPONENT THAT IS HEAVIER THAN THE MIDDLE FRACTION, AND BRINGING EACH OF THE MIDDLE FRACTION AND THE WAX COMPONENT INTO CONTACT WITH A HYDROTREATING CATALYST IN THE PRESENCE OF HYDROGEN, AND THEN MIXING TOGETHER, AND FRACTIONATING, SO AS TO OBTAIN A HYDROCARBON OIL HAVING A CONTENT OF A FRACTION OF BOILING POINT 150 TO 360�C OF NOT LESS THAN 86 MASS% AND A CONTENT OF A FRACTION OF BOILING POINT NOT LESS THAN 350�C OF NOT LESS THAN 5 MASS%.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006066465A JP4908022B2 (en) | 2006-03-10 | 2006-03-10 | Method for producing hydrocarbon oil and hydrocarbon oil |
Publications (1)
Publication Number | Publication Date |
---|---|
MY148585A true MY148585A (en) | 2013-04-30 |
Family
ID=38509238
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MYPI20083399 MY148585A (en) | 2006-03-10 | 2007-02-14 | Process for production of hydrocarbon oil and hydrocarbon oil |
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)
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 |
JP5090457B2 (en) * | 2007-09-28 | 2012-12-05 | 独立行政法人石油天然ガス・金属鉱物資源機構 | Method for producing diesel fuel |
BRPI0817737B1 (en) * | 2007-09-28 | 2017-09-12 | Japan Oil, Gas And Metals National Corporation | Diesel fuel base stock production method |
US8163168B2 (en) * | 2008-07-25 | 2012-04-24 | Exxonmobil Research And Engineering Company | Process for flexible vacuum gas oil conversion |
CN105593352A (en) * | 2013-09-30 | 2016-05-18 | 国际壳牌研究有限公司 | 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 |
JP2016535117A (en) * | 2013-09-30 | 2016-11-10 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイShell Internationale Research Maatschappij Besloten Vennootshap | Fischer-Tropsch derived light oil |
WO2015044281A1 (en) * | 2013-09-30 | 2015-04-02 | Shell Internationale Research Maatschappij B.V. | Fischer-tropsch derived gas oil fraction |
US20160208185A1 (en) * | 2013-09-30 | 2016-07-21 | Shell Oil Company | Fischer-tropsch derived gas oil fraction |
JP2016538353A (en) * | 2013-09-30 | 2016-12-08 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイShell Internationale Research Maatschappij Besloten Vennootshap | Fischer-Tropsch derived diesel oil fraction |
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 method of low-temperature Fischer-Tropsch full distillate oil and high production of middle distillate 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)
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 |
EP1835011A1 (en) * | 1998-10-05 | 2007-09-19 | 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 |
EP1547683B1 (en) * | 2002-09-24 | 2017-01-11 | 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 |
EP1664247A1 (en) * | 2003-09-03 | 2006-06-07 | Shell Internationale Researchmaatschappij B.V. | 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 |
-
2006
- 2006-03-10 JP JP2006066465A patent/JP4908022B2/en not_active Expired - Fee Related
-
2007
- 2007-02-14 WO PCT/JP2007/052618 patent/WO2007105400A1/en active Application Filing
- 2007-02-14 RU RU2008140146/04A patent/RU2425859C2/en not_active IP Right Cessation
- 2007-02-14 MY MYPI20083399 patent/MY148585A/en unknown
- 2007-02-14 CN CN200780008543.6A patent/CN101400768B/en not_active Expired - Fee Related
- 2007-02-14 AU AU2007226057A patent/AU2007226057B2/en not_active Ceased
Also Published As
Publication number | Publication date |
---|---|
JP2007238870A (en) | 2007-09-20 |
JP4908022B2 (en) | 2012-04-04 |
RU2008140146A (en) | 2010-04-20 |
CN101400768B (en) | 2012-08-22 |
AU2007226057B2 (en) | 2011-12-01 |
RU2425859C2 (en) | 2011-08-10 |
CN101400768A (en) | 2009-04-01 |
AU2007226057A1 (en) | 2007-09-20 |
WO2007105400A1 (en) | 2007-09-20 |
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