NO20052822L - Fischer-Tropsch-katalysatorer - Google Patents

Fischer-Tropsch-katalysatorer

Info

Publication number
NO20052822L
NO20052822L NO20052822A NO20052822A NO20052822L NO 20052822 L NO20052822 L NO 20052822L NO 20052822 A NO20052822 A NO 20052822A NO 20052822 A NO20052822 A NO 20052822A NO 20052822 L NO20052822 L NO 20052822L
Authority
NO
Norway
Prior art keywords
fischer
catalyst
impregnated
tropsch catalysts
calcined catalyst
Prior art date
Application number
NO20052822A
Other languages
English (en)
Other versions
NO333752B1 (no
Inventor
Sigrid Eri
Erling Rytter
Dag Schanke
Original Assignee
Statoil Asa
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 Statoil Asa filed Critical Statoil Asa
Publication of NO20052822L publication Critical patent/NO20052822L/no
Publication of NO333752B1 publication Critical patent/NO333752B1/no

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
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/33—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used
    • C10G2/331—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals
    • C10G2/332—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals of the iron-group
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/75—Cobalt
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/889—Manganese, technetium or rhenium
    • B01J23/8896—Rhenium
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/615—100-500 m2/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63—Pore volume
    • B01J35/635—0.5-1.0 ml/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • C10G2300/70—Catalyst aspects
    • C10G2300/703—Activation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)

Abstract

Katalysator for anvendelse i en Fischer-Tropsch syntesereaksjon hvor det benyttes kobolt båret på aluminiumoksid, og hvor katalysatorens midlere partikkelstørre er i området 20-100 ^m, det spesiflkke overflateareal av de impregnerte og kalsinerte katalysatorpartikler er større erm 80 mVg, den midlere porestørrelse av den impregnerte og kalsinerte katalysator er minst 90Å (9 rmi), og den impregnerte og kalsinerte katalysators porevolum er større erm 0,35 cm^/g.
NO20052822A 2002-11-13 2005-06-10 Fischer-Tropsch-katalysatorer og anvendelse av katalysatoren, samt fremgangsmate for fremstilling av hydrokarboner. NO333752B1 (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0226514.8A GB0226514D0 (en) 2002-11-13 2002-11-13 Fischer-tropsch catalysts
PCT/GB2003/004873 WO2004043596A2 (en) 2002-11-13 2003-11-10 Fischer-tropsch catalysts

Publications (2)

Publication Number Publication Date
NO20052822L true NO20052822L (no) 2005-06-10
NO333752B1 NO333752B1 (no) 2013-09-09

Family

ID=9947775

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20052822A NO333752B1 (no) 2002-11-13 2005-06-10 Fischer-Tropsch-katalysatorer og anvendelse av katalysatoren, samt fremgangsmate for fremstilling av hydrokarboner.

Country Status (11)

Country Link
US (1) US8324128B2 (no)
EP (1) EP1562706A2 (no)
CN (1) CN1723087A (no)
AU (1) AU2003301952B2 (no)
BR (1) BR0316210A (no)
CA (1) CA2506534C (no)
EA (1) EA009572B1 (no)
GB (1) GB0226514D0 (no)
NO (1) NO333752B1 (no)
WO (1) WO2004043596A2 (no)
ZA (1) ZA200503842B (no)

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US20050096211A1 (en) * 2003-10-31 2005-05-05 Hiroshi Takeda Catalyst for the conversion of carbon monoxide
GB2410449B (en) * 2004-01-28 2008-05-21 Statoil Asa Fischer-Tropsch catalysts
GB2416715A (en) * 2004-07-30 2006-02-08 Statoil Asa Fischer-Tropsch catalyst
US8080224B2 (en) * 2006-05-05 2011-12-20 Sud-Chemie Inc. Catalyst for the conversion of carbon monoxide
CN101195553B (zh) * 2006-12-07 2011-08-10 中国石油化工股份有限公司 一种烃合成方法
GB2446127A (en) * 2007-01-30 2008-08-06 Gtl F1 Ag Preparation of Fischer-Tropsch Catalysts
WO2010071989A1 (en) * 2008-12-22 2010-07-01 Canada Chemical Corporation Low-pressure fischer-tropsch process
GB2473071B (en) 2009-09-01 2013-09-11 Gtl F1 Ag Fischer-tropsch catalysts
GB2475492B (en) 2009-11-18 2014-12-31 Gtl F1 Ag Fischer-Tropsch synthesis
GB201000993D0 (en) * 2010-01-22 2010-03-10 Johnson Matthey Plc Catalyst support
JP5759447B2 (ja) * 2010-03-05 2015-08-05 Ｊｘ日鉱日石エネルギー株式会社 フィッシャー・トロプシュ合成触媒の製造方法、並びに炭化水素の製造方法
WO2011119638A2 (en) 2010-03-22 2011-09-29 Brigham Young University Method for making highly porous, stable metal oxide with a controlled pore structure
GB2482171B (en) * 2010-07-22 2018-04-11 Gtl F1 Ag Catalyst treatment
EP2603316B1 (en) 2010-08-09 2017-04-19 Gtl. F1 Ag Fischer-tropsch catalysts
US20120115967A1 (en) 2010-11-08 2012-05-10 Shell Oil Company Fischer-tropsch catalysts
US9114378B2 (en) 2012-03-26 2015-08-25 Brigham Young University Iron and cobalt based fischer-tropsch pre-catalysts and catalysts
RU2629940C2 (ru) * 2012-10-24 2017-09-05 Сасол Тэкнолоджи (Проприэтэри) Лимитед Способ получения катализатора синтеза фишера-тропша
US9289750B2 (en) 2013-03-09 2016-03-22 Brigham Young University Method of making highly porous, stable aluminum oxides doped with silicon
US9180436B1 (en) 2013-11-19 2015-11-10 Emerging Fuels Technology, Inc. Optimized fischer-tropsch catalyst
US9358526B2 (en) 2013-11-19 2016-06-07 Emerging Fuels Technology, Inc. Optimized fischer-tropsch catalyst
CN103933996B (zh) * 2014-04-22 2016-05-25 华东理工大学 阳极氧化与电镀结合制备Co/Al2O3/不锈钢整体式催化剂的方法
FR3044565B1 (fr) * 2015-12-08 2017-12-01 Ifp Energies Now Chargement d'un catalyseur dans une colonne a bulles pour la synthese fischer-tropsch
CN109718773B (zh) * 2017-10-27 2022-03-11 中国石油化工股份有限公司 一种ft合成催化剂及其制备方法和应用及费托合成方法
CN110252358B (zh) * 2018-03-12 2022-03-22 国家能源投资集团有限责任公司 费托合成钴催化剂及其制备方法以及费托合成的方法
CN108435200B (zh) * 2018-04-24 2021-04-30 西安元创化工科技股份有限公司 一种钴基费托合成重质烃催化剂及其制备方法和应用
GB201903502D0 (en) * 2019-03-14 2019-05-01 Johnson Matthey Plc Cobalt catalysts and precursors therefor

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US3988263A (en) * 1974-10-02 1976-10-26 Union Oil Company Of California Thermally stable coprecipitated catalysts useful for methanation and other reactions
US3933883A (en) * 1975-04-14 1976-01-20 W. R. Grace & Co. Methanation catalyst and process of use
US4102822A (en) * 1976-07-26 1978-07-25 Chevron Research Company Hydrocarbon hydroconversion catalyst and the method for its preparation
US4613624A (en) * 1981-10-13 1986-09-23 Chevron Research Company Conversion of synthesis gas to diesel fuel and catalyst therefor
US4888316A (en) * 1988-11-21 1989-12-19 Phillips Petroleum Company Preparation of hydrotreating catalyst from spent catalyst
US5639798A (en) * 1994-12-15 1997-06-17 Wexford P.A. Syncrude Limited Partnership Process and catalyst for production of hydrocarbons
DZ2013A1 (fr) * 1995-04-07 2002-10-23 Sastech Ltd Catalyseurs.
IT1292462B1 (it) * 1997-07-03 1999-02-08 Agip Petroli Composizione catalitica utile nel processo di fischer-tropsch
FR2784096B1 (fr) * 1998-09-18 2000-12-01 Inst Francais Du Petrole Procede de conversion du gaz de synthese en presence d'un catalyseur a base de metal du groupe viii, les particules du metal etant reparties sous forme d'agregats
KR20010080035A (ko) * 1998-10-05 2001-08-22 마샤 마그달레나 밴 더 메르베 촉매 함침법
EP0998976A1 (en) * 1998-11-04 2000-05-10 Engelhard Corporation Star shaped alumina extrudates and catalyst based thereon
GB0003961D0 (en) * 2000-02-21 2000-04-12 Ici Plc Catalysts
IT1317868B1 (it) 2000-03-02 2003-07-15 Eni Spa Catalizzatore a base di cobalto supportato, particolarmente utilenella reazione di fischer-tropsch.
US6255358B1 (en) * 2000-03-17 2001-07-03 Energy International Corporation Highly active Fischer-Tropsch synthesis using doped, thermally stable catalyst support
US7452844B2 (en) * 2001-05-08 2008-11-18 Süd-Chemie Inc High surface area, small crystallite size catalyst for Fischer-Tropsch synthesis
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Also Published As

Publication number Publication date
US20080064770A1 (en) 2008-03-13
WO2004043596A2 (en) 2004-05-27
US8324128B2 (en) 2012-12-04
WO2004043596A3 (en) 2004-08-12
AU2003301952B2 (en) 2009-01-15
CA2506534C (en) 2013-05-07
ZA200503842B (en) 2006-09-27
EP1562706A2 (en) 2005-08-17
EA009572B1 (ru) 2008-02-28
AU2003301952A1 (en) 2004-06-03
EA200500805A1 (ru) 2005-12-29
CN1723087A (zh) 2006-01-18
GB0226514D0 (en) 2002-12-18
BR0316210A (pt) 2005-09-27
CA2506534A1 (en) 2004-05-27
NO333752B1 (no) 2013-09-09

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