NO20052822L - Fischer-Tropsch-katalysatorer - Google Patents
Fischer-Tropsch-katalysatorerInfo
- 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
Links
- 239000003054 catalyst Substances 0.000 title abstract 6
- 239000002245 particle Substances 0.000 abstract 2
- 239000011148 porous material Substances 0.000 abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 229910017052 cobalt Inorganic materials 0.000 abstract 1
- 239000010941 cobalt Substances 0.000 abstract 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 abstract 1
- 238000003786 synthesis reaction Methods 0.000 abstract 1
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.
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) |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
GB0112792D0 (en) * | 2001-05-25 | 2001-07-18 | Bp Exploration Operating | Process |
-
2002
- 2002-11-13 GB GBGB0226514.8A patent/GB0226514D0/en not_active Ceased
-
2003
- 2003-11-10 US US10/535,066 patent/US8324128B2/en not_active Expired - Fee Related
- 2003-11-10 EP EP03811022A patent/EP1562706A2/en not_active Withdrawn
- 2003-11-10 WO PCT/GB2003/004873 patent/WO2004043596A2/en not_active Application Discontinuation
- 2003-11-10 AU AU2003301952A patent/AU2003301952B2/en not_active Ceased
- 2003-11-10 CN CN200380105506.9A patent/CN1723087A/zh active Pending
- 2003-11-10 CA CA2506534A patent/CA2506534C/en not_active Expired - Fee Related
- 2003-11-10 BR BR0316210-9A patent/BR0316210A/pt not_active Application Discontinuation
- 2003-11-10 EA EA200500805A patent/EA009572B1/ru not_active IP Right Cessation
-
2005
- 2005-05-12 ZA ZA200503842A patent/ZA200503842B/en unknown
- 2005-06-10 NO NO20052822A patent/NO333752B1/no not_active IP Right Cessation
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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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM1K | Lapsed by not paying the annual fees |