WO2008062595A1 - Procédé de fabrication d'un combustible liquide - Google Patents

Procédé de fabrication d'un combustible liquide Download PDF

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Publication number
WO2008062595A1
WO2008062595A1 PCT/JP2007/066877 JP2007066877W WO2008062595A1 WO 2008062595 A1 WO2008062595 A1 WO 2008062595A1 JP 2007066877 W JP2007066877 W JP 2007066877W WO 2008062595 A1 WO2008062595 A1 WO 2008062595A1
Authority
WO
WIPO (PCT)
Prior art keywords
catalyst
mass
liquid fuel
producing
phosphorus
Prior art date
Application number
PCT/JP2007/066877
Other languages
English (en)
Japanese (ja)
Inventor
Hiroyuki Seki
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
Application filed by Nippon Oil Corporation filed Critical Nippon Oil Corporation
Priority to AU2007322907A priority Critical patent/AU2007322907B2/en
Priority to JP2007551014A priority patent/JP5408879B2/ja
Publication of WO2008062595A1 publication Critical patent/WO2008062595A1/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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/185—Phosphorus; Compounds thereof with iron group metals or platinum group metals
    • B01J27/1856—Phosphorus; Compounds thereof with iron group metals or platinum group metals with platinum group metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084—Y-type faujasite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/10—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing iron group metals, noble metals or copper
    • B01J29/12—Noble metals
    • B01J29/126—Y-type faujasite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation

Definitions

  • the present invention relates to a method for producing a liquid fuel from paraffinic hydrocarbons in the presence of hydrogen.
  • Patent Document 2 describes a research example in which paraffinic hydrocarbons were hydrocracked using a catalyst in which platinum was supported on a support in which crystalline aluminosilicate (zeolite) and silica alumina which is an amorphous solid acid were combined. It is disclosed.
  • zeolite crystalline aluminosilicate
  • silica alumina silica alumina which is an amorphous solid acid
  • Patent Document 2 Pamphlet of International Publication No. 2004/028688
  • the "middle distillate” referred to in the present invention is a hydrocracked product having a boiling range of 145 to 145. Means petroleum or synthetic fractions at 360 ° C.
  • a typical example of the middle distillate is a middle distillate produced by Fisher's Tropsch (FT ) synthesis.
  • the light oil fraction means a fraction having a boiling point of 260 to 360 ° C, which is a part of the middle fraction.
  • the paraffinic hydrocarbon preferably contains 70% by mass or more normal paraffin.
  • the content of normal paraffin is determined by gas chromatography method!
  • the average particle size of the crystalline aluminosilicate is not particularly limited, but preferably 1.
  • examples of the amorphous solid acid include silica alumina, silica zirconia, silica titania, silica magnesia, alumina zirconia, and alumina polyaer.
  • alumina polya is preferably used.
  • catalyst A phosphorus content: 1.8% by mass, platinum loading: 0.5% by mass.
  • catalyst D phosphorus content: 1.8% by mass, platinum loading: 0.5% by mass.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

L'invention concerne un procédé de fabrication d'un combustible liquide par hydrocraquage d'un hydrocarbure paraffinique. Le procédé est caractérisé par la mise en contact, en présence d'hydrogène, entre un hydrocarbure paraffinique et un catalyseur comprenant un support comportant un aluminosilicate cristallin et un acide solide amorphe et, déposé sur le support, au moins un métal choisi parmi les métaux du groupe VIII du tableau périodique et contenant au moins un élément choisi parmi le phosphore et le bore.
PCT/JP2007/066877 2006-11-21 2007-08-30 Procédé de fabrication d'un combustible liquide WO2008062595A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AU2007322907A AU2007322907B2 (en) 2006-11-21 2007-08-30 Process for producing liquid fuel
JP2007551014A JP5408879B2 (ja) 2006-11-21 2007-08-30 液体燃料の製造方法

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2006-314638 2006-11-21
JP2006314638 2006-11-21

Publications (1)

Publication Number Publication Date
WO2008062595A1 true WO2008062595A1 (fr) 2008-05-29

Family

ID=39429536

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2007/066877 WO2008062595A1 (fr) 2006-11-21 2007-08-30 Procédé de fabrication d'un combustible liquide

Country Status (6)

Country Link
JP (2) JP5408879B2 (fr)
CN (1) CN101547996A (fr)
AU (1) AU2007322907B2 (fr)
MY (1) MY149444A (fr)
RU (1) RU2437716C2 (fr)
WO (1) WO2008062595A1 (fr)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02214544A (ja) * 1989-02-16 1990-08-27 Nippon Oil Co Ltd 重質石油類の水素化分解触媒
JP2000024510A (ja) * 1998-06-25 2000-01-25 Inst Fr Petrole 全体的非脱アルミニウムゼオライトｙと、第ｖｂ族の元素と、ホウ素、リンおよびケイ素からなる群から選ばれる助触媒元素とを含む水素化クラッキング触媒
JP2002523231A (ja) * 1998-09-01 2002-07-30 株式会社ジャパンエナジー 水素化分解触媒及びその製造方法並びに水素化分解方法
WO2004028688A1 (fr) * 2002-09-24 2004-04-08 Nippon Oil Corporation Catalyseur d'hydrocraquage et procede de fabrication d'hydrocarbures liquides
JP2006505671A (ja) * 2002-11-08 2006-02-16 シェブロン ユー．エス．エー． インコーポレイテッド 極低酸度超安定ｙ型ゼオライト及び均質無定形シリカ−アルミナを含む水素化分解触媒並びに水素化分解方法

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4431527A (en) * 1981-11-13 1984-02-14 Standard Oil Company (Indiana) Process for hydrogen treating high nitrogen content hydrocarbon feeds
JP2992971B2 (ja) * 1994-09-01 1999-12-20 株式会社ジャパンエナジー 水素化処理用触媒
US6387246B1 (en) * 1999-05-19 2002-05-14 Institut Francais Du Petrole Catalyst that comprises a partially amorphous Y zeolite and its use in hydroconversion of hydrocarbon petroleum feedstocks
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
JPH02214544A (ja) * 1989-02-16 1990-08-27 Nippon Oil Co Ltd 重質石油類の水素化分解触媒
JP2000024510A (ja) * 1998-06-25 2000-01-25 Inst Fr Petrole 全体的非脱アルミニウムゼオライトｙと、第ｖｂ族の元素と、ホウ素、リンおよびケイ素からなる群から選ばれる助触媒元素とを含む水素化クラッキング触媒
JP2002523231A (ja) * 1998-09-01 2002-07-30 株式会社ジャパンエナジー 水素化分解触媒及びその製造方法並びに水素化分解方法
WO2004028688A1 (fr) * 2002-09-24 2004-04-08 Nippon Oil Corporation Catalyseur d'hydrocraquage et procede de fabrication d'hydrocarbures liquides
JP2006505671A (ja) * 2002-11-08 2006-02-16 シェブロン ユー．エス．エー． インコーポレイテッド 極低酸度超安定ｙ型ゼオライト及び均質無定形シリカ−アルミナを含む水素化分解触媒並びに水素化分解方法

Also Published As

Publication number Publication date
JP5408879B2 (ja) 2014-02-05
MY149444A (en) 2013-08-30
RU2009123492A (ru) 2010-12-27
JP2013079402A (ja) 2013-05-02
CN101547996A (zh) 2009-09-30
RU2437716C2 (ru) 2011-12-27
JPWO2008062595A1 (ja) 2010-03-04
AU2007322907B2 (en) 2011-11-24
AU2007322907A1 (en) 2008-05-29

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