WO2008087897A1 - Processes for production of liquid fuel - Google Patents

Processes for production of liquid fuel Download PDF

Info

Publication number
WO2008087897A1
WO2008087897A1 PCT/JP2008/050244 JP2008050244W WO2008087897A1 WO 2008087897 A1 WO2008087897 A1 WO 2008087897A1 JP 2008050244 W JP2008050244 W JP 2008050244W WO 2008087897 A1 WO2008087897 A1 WO 2008087897A1
Authority
WO
WIPO (PCT)
Prior art keywords
oil
catalyst
carrier
fraction
solid acid
Prior art date
Application number
PCT/JP2008/050244
Other languages
French (fr)
Japanese (ja)
Inventor
Hiroyuki Seki
Masahiro Higashi
Original Assignee
Nippon Oil Corporation
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 JP2007006210A external-priority patent/JP4861838B2/en
Priority claimed from JP2007006215A external-priority patent/JP2008169356A/en
Application filed by Nippon Oil Corporation filed Critical Nippon Oil Corporation
Priority to AU2008206002A priority Critical patent/AU2008206002B2/en
Publication of WO2008087897A1 publication Critical patent/WO2008087897A1/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
    • 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
    • C10G47/18—Crystalline alumino-silicate carriers the catalyst containing platinum group metals or compounds thereof
    • 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
    • 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
    • C10G65/16—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only including only refining steps
    • 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)
  • Catalysts (AREA)

Abstract

A first process which comprises fractionating a stock oil which contains normal paraffins, oxygen-containing compounds and olefins and exhibits distillation properties involving a final point of 360°C or below into a first fraction and a second fraction with the boundary point falling within the range of 130 to 160°C and hydrorefining the first and second fractions respectively with a first catalyst and a second catalyst which each comprise both a carrier containing a solid acid and a Group VIII metal of the periodic table supported on the carrier. A second process which comprises bringing a stock oil containing paraffin-base hydrocarbons into contact with a supported platinum catalyst prepared from a carrier containing both crystalline aluminosilicate and an amorphous solid acid and a platinum compound free from constituent chlorine element to conduct hydrocracking of the oil and thus obtain a cracked oil.
PCT/JP2008/050244 2007-01-15 2008-01-11 Processes for production of liquid fuel WO2008087897A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2008206002A AU2008206002B2 (en) 2007-01-15 2008-01-11 Processes for production of liquid fuel

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP2007006210A JP4861838B2 (en) 2007-01-15 2007-01-15 Method for producing liquid fuel
JP2007-006215 2007-01-15
JP2007006215A JP2008169356A (en) 2007-01-15 2007-01-15 Method for producing liquid fuel
JP2007-006210 2007-01-15

Publications (1)

Publication Number Publication Date
WO2008087897A1 true WO2008087897A1 (en) 2008-07-24

Family

ID=39635901

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2008/050244 WO2008087897A1 (en) 2007-01-15 2008-01-11 Processes for production of liquid fuel

Country Status (5)

Country Link
CN (1) CN105038844A (en)
AU (1) AU2008206002B2 (en)
MY (1) MY150403A (en)
RU (1) RU2443756C2 (en)
WO (1) WO2008087897A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012211287A (en) * 2011-03-31 2012-11-01 Jx Nippon Oil & Energy Corp Process for producing kerosene

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2536585C1 (en) * 2013-09-27 2014-12-27 Федеральное государственное бюджетное учреждение науки Институт катализа им. Г.К. Борескова Сибирского отделения Российской академии наук Catalyst, method of manufacturing thereof and process of diesel fuel hydroisomerisation

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5378348A (en) * 1993-07-22 1995-01-03 Exxon Research And Engineering Company Distillate fuel production from Fischer-Tropsch wax
JPH11509137A (en) * 1995-07-14 1999-08-17 エクソン リサーチ アンド エンジニアリング カンパニー Supported nickel-copper hydroconversion catalyst
US5994607A (en) * 1996-02-05 1999-11-30 Institut Francais Du Petrole Paraffin isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones
US20030057134A1 (en) * 2001-07-06 2003-03-27 Institut Francais Du Petrole Process for the production of middle distillates by hydroisomerisation and hydrocracking feeds from the fischer-tropsch process
US20040254415A1 (en) * 2001-08-06 2004-12-16 Christophe Bouchy Method for the isomerisation of a c5-c8 fraction involving two parallel reactors

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL178305B1 (en) * 1993-10-08 2000-04-28 Akzo Nobel Nv Hydrocracking and hydrodeparaffining method
US5865988A (en) * 1995-07-07 1999-02-02 Mobil Oil Corporation Hydrocarbon upgrading process
US6569315B2 (en) * 2000-04-17 2003-05-27 Exxonmobil Research And Engineering Company Cycle oil conversion process
ITMI20011441A1 (en) * 2001-07-06 2003-01-06 Agip Petroli PROCESS FOR THE PRODUCTION OF MEDIUM PARAFFINIC DISTILLATES
US7122494B2 (en) * 2003-02-05 2006-10-17 Exxonmobil Chemical Patents Inc. Combined cracking and selective hydrogen combustion for catalytic cracking
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

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5378348A (en) * 1993-07-22 1995-01-03 Exxon Research And Engineering Company Distillate fuel production from Fischer-Tropsch wax
JPH11509137A (en) * 1995-07-14 1999-08-17 エクソン リサーチ アンド エンジニアリング カンパニー Supported nickel-copper hydroconversion catalyst
US5994607A (en) * 1996-02-05 1999-11-30 Institut Francais Du Petrole Paraffin isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones
US20030057134A1 (en) * 2001-07-06 2003-03-27 Institut Francais Du Petrole Process for the production of middle distillates by hydroisomerisation and hydrocracking feeds from the fischer-tropsch process
US20040254415A1 (en) * 2001-08-06 2004-12-16 Christophe Bouchy Method for the isomerisation of a c5-c8 fraction involving two parallel reactors

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012211287A (en) * 2011-03-31 2012-11-01 Jx Nippon Oil & Energy Corp Process for producing kerosene

Also Published As

Publication number Publication date
AU2008206002A1 (en) 2008-07-24
RU2009131081A (en) 2011-02-27
MY150403A (en) 2014-01-15
RU2443756C2 (en) 2012-02-27
AU2008206002B2 (en) 2011-11-17
CN105038844A (en) 2015-11-11

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