MY148376A - Method for treatment of synthetic oil, process for production of hydrocarbon oil, hydrocarbon oil for hydrogen production, hydrocarbon oil for the smoke point improver for kerosene, and hydrocarbon oil for diesel fuel base - Google Patents

Method for treatment of synthetic oil, process for production of hydrocarbon oil, hydrocarbon oil for hydrogen production, hydrocarbon oil for the smoke point improver for kerosene, and hydrocarbon oil for diesel fuel base

Info

Publication number
MY148376A
MY148376A MYPI20083768A MY148376A MY 148376 A MY148376 A MY 148376A MY PI20083768 A MYPI20083768 A MY PI20083768A MY 148376 A MY148376 A MY 148376A
Authority
MY
Malaysia
Prior art keywords
hydrocarbon oil
fraction
fractional
oil
distillation
Prior art date
Application number
Inventor
Tanaka Yuichi
Takahashi Shinya
Chiba Yoshifumi
Sadakane Osamu
Original Assignee
Nippon Oil Corp
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
Priority claimed from JP2006095201A external-priority patent/JP4908037B2/en
Priority claimed from JP2006095228A external-priority patent/JP4908038B2/en
Application filed by Nippon Oil Corp filed Critical Nippon Oil Corp
Publication of MY148376A publication Critical patent/MY148376A/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

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

THE METHOD FOR PROCESSING SYNTHETIC OIL OF THE PRESENT INVENTION IS CHARACTERIZED IN THAT IT INCLUDES: A FIRST FRACTIONAL-DISTILLATION STEP OF SUBJECTING A MATERIAL TO BE PROCESSED, WHICH COMPRISES SYNTHETIC OIL OBTAINED BY FISCHER TROPSCH SYNTHESIS, TO FRACTIONAL DISTILLATION TO OBTAIN A MIDDLE DISTILLATE, WHICH CONTAINS A FRACTION HAVING A BOILING POINT OF 150 TO 360oC AT 90% BY MASS OR MORE, AND A WAX DISTILLATE WHICH IS HEAVIER THAN THE MIDDLE DISTILLATE; A HYDROTREATING STEP OF SUBJECTING THE MIDDLE DISTILLATE OBTAINED IN THE FIRST FRACTIONAL-DISTILLATION STEP TO HYDROTREATING BY BRINGING THE SAME INTO CONTACT WITH HYDROTREATING CATALYST IN THE PRESENCE OF HYDROGEN SO THAT A FRACTION HAVING A BOILING POINT OF 150�C OR LOWER OF THE MIDDLE DISTILLATE HAS A CONTENT (% BY MASS) WITH AN INCREASE RATE OF 9% BY MASS OR LESS AFTER THE CONTACT WITH THE CATALYST; A SECOND FRACTIONAL-DISTILLATION STEP OF SUBJECTING THE MIDDLE DISTILLATE HAVING PASSED THROUGH THE HYDROTREATING STEP TO FRACTIONAL DISTILLATION TO OBTAIN A FIRST FRACTION, WHICH CONTAINS A FRACTION HAVING A BOILING POINT OF 150 TO 250�C AT 90% BY MASS OR MORE, AND A SECOND FRACTION, WHICH IS HEAVIER THAN THE FIRST FRACTION; A HYDROCRACKING STEP OF SUBJECTING THE WAX DISTILLATE OBTAINED IN THE FIRST FRACTIONAL-DISTILLATION STEP TO HYDROCRACKING BY BRINGING THE SAME INTO CONTACT WITH HYDROCRACKING CATALYST IN THE PRESENCE OF HYDROGEN; A THIRD FRACTIONAL-DISTILLATION STEP OF SUBJECTING THE WAX DISTILLATE HAVING PASSED THROUGH THE HYDROCRACKING STEP TO FRACTIONAL DISTILLATION TO OBTAIN A THIRD FRACTION, WHICH CONTAINS A FRACTION HAVING A BOILING POINT OF 150 TO 360�C AT 90% BY MASS OR MORE; AND A MIXING STEP OF MIXING THE SECOND FRACTION AND THE THIRD FRACTION.
MYPI20083768 2006-03-30 2007-03-05 Method for treatment of synthetic oil, process for production of hydrocarbon oil, hydrocarbon oil for hydrogen production, hydrocarbon oil for the smoke point improver for kerosene, and hydrocarbon oil for diesel fuel base MY148376A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2006095201A JP4908037B2 (en) 2006-03-30 2006-03-30 Method for treating synthetic oil, hydrocarbon oil for kerosene smoke point improver and hydrocarbon oil for diesel fuel base material
JP2006095228A JP4908038B2 (en) 2006-03-30 2006-03-30 Method for treating synthetic oil, hydrocarbon oil for hydrogen production and hydrocarbon oil for diesel fuel base material

Publications (1)

Publication Number Publication Date
MY148376A true MY148376A (en) 2013-04-15

Family

ID=38563239

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI20083768 MY148376A (en) 2006-03-30 2007-03-05 Method for treatment of synthetic oil, process for production of hydrocarbon oil, hydrocarbon oil for hydrogen production, hydrocarbon oil for the smoke point improver for kerosene, and hydrocarbon oil for diesel fuel base

Country Status (4)

Country Link
AU (1) AU2007232015B2 (en)
MY (1) MY148376A (en)
RU (1) RU2429279C2 (en)
WO (1) WO2007113967A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2008304882B2 (en) * 2007-09-28 2011-10-27 Cosmo Oil Co., Ltd. Method of manufacturing diesel fuel base stock and diesel fuel base stock thereof
EA016118B1 (en) * 2007-09-28 2012-02-28 Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн Process for producing diesel fuel
JP5752870B2 (en) * 2008-03-14 2015-07-22 独立行政法人石油天然ガス・金属鉱物資源機構 Operation method of hydrotreating equipment
CN102730637B (en) * 2012-07-17 2014-12-10 武汉凯迪工程技术研究总院有限公司 Comprehensive utilization process for low-carbon-emission Fischer-Tropsch synthesis tail gas
WO2014135966A1 (en) * 2013-03-07 2014-09-12 Verolube, Inc. Method and apparatus for recovering synthetic oils from composite oil streams

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6296757B1 (en) * 1995-10-17 2001-10-02 Exxon Research And Engineering Company Synthetic diesel fuel and process for its production
MY129748A (en) * 2001-03-05 2007-04-30 Shell Int Research Process for the preparation of middle distillates
US6846402B2 (en) * 2001-10-19 2005-01-25 Chevron U.S.A. Inc. Thermally stable jet prepared from highly paraffinic distillate fuel component and conventional distillate fuel component
US6860986B2 (en) * 2002-11-08 2005-03-01 Chevron U.S.A. Inc. Extremely low acidity ultrastable Y zeolite catalyst composition and process
JP4575646B2 (en) * 2003-03-07 2010-11-04 Ｊｘ日鉱日石エネルギー株式会社 Light oil composition
US20070021636A1 (en) * 2003-05-22 2007-01-25 Willem Bosch Process to upgrade kerosenes and a gasoils from naphthenic and aromatic crude petroleum sources

Also Published As

Publication number Publication date
RU2429279C2 (en) 2011-09-20
AU2007232015B2 (en) 2011-11-24
WO2007113967A1 (en) 2007-10-11
AU2007232015A1 (en) 2007-10-11
RU2008142984A (en) 2010-05-10

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