WO2008087897A1 - Procédés de fabrication d'un combustible liquide - Google Patents

Procédés de fabrication d'un combustible liquide Download PDF

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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
English (en)
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/ja
Priority claimed from JP2007006215A external-priority patent/JP2008169356A/ja
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/fr

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

L'invention porte sur un premier procédé qui comprend le fractionnement d'une huile de base qui contient des paraffines normales, des composés à teneur en oxygène et des oléfines et qui présente des propriétés de distillation mettant en jeu un point final de 360 °C ou moins dans une première fraction et une seconde fraction avec le point limite tombant dans la plage de 130 à 160 °C et l'hydroraffinage des première et seconde fractions respectivement avec un premier catalyseur et un second catalyseur qui comprennent chacun à la fois un support contenant un acide solide et un métal du Groupe VIII de la classification périodique supporté sur le support. L'invention porte sur un second procédé qui comprend l'opération consistant à amener une huile de base contenant des hydrocarbures à base de paraffine en contact avec un catalyseur au platine supporté préparé à partir d'un support contenant à la fois de l'aluminosilicate cristallin et un acide solide amorphe et un composé du platine exempt d'élément chlore constitutif pour conduire un hydrocraquage de l'huile et obtenir ainsi une huile craquée.
PCT/JP2008/050244 2007-01-15 2008-01-11 Procédés de fabrication d'un combustible liquide WO2008087897A1 (fr)

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 (ja) 2007-01-15 2007-01-15 液体燃料の製造方法
JP2007-006215 2007-01-15
JP2007006215A JP2008169356A (ja) 2007-01-15 2007-01-15 液体燃料の製造方法
JP2007-006210 2007-01-15

Publications (1)

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

Family

ID=39635901

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2008/050244 WO2008087897A1 (fr) 2007-01-15 2008-01-11 Procédés de fabrication d'un combustible liquide

Country Status (5)

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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012211287A (ja) * 2011-03-31 2012-11-01 Jx Nippon Oil & Energy Corp 灯油の製造方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2536585C1 (ru) * 2013-09-27 2014-12-27 Федеральное государственное бюджетное учреждение науки Институт катализа им. Г.К. Борескова Сибирского отделения Российской академии наук Катализатор, способ его приготовления и процесс гидроизомеризации дизельного топлива

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 (ja) * 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 担持ニッケル−銅水素化転化触媒
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 (pl) * 1993-10-08 2000-04-28 Akzo Nobel Nv Sposób hydrokrakowania i hydroodparafinowania
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 (it) * 2001-07-06 2003-01-06 Agip Petroli Processo per la produzione di distillati medi paraffinici
US7122494B2 (en) * 2003-02-05 2006-10-17 Exxonmobil Chemical Patents Inc. Combined cracking and selective hydrogen combustion for catalytic cracking
JP4313237B2 (ja) * 2004-03-29 2009-08-12 新日本石油株式会社 水素化分解触媒および液状炭化水素の製造方法

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 (ja) * 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 担持ニッケル−銅水素化転化触媒
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 (ja) * 2011-03-31 2012-11-01 Jx Nippon Oil & Energy Corp 灯油の製造方法

Also Published As

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

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