JP2002512556A - 高活性触媒の調製方法ならびに該触媒およびその使用 - Google Patents
高活性触媒の調製方法ならびに該触媒およびその使用Info
- Publication number
- JP2002512556A JP2002512556A JP54622298A JP54622298A JP2002512556A JP 2002512556 A JP2002512556 A JP 2002512556A JP 54622298 A JP54622298 A JP 54622298A JP 54622298 A JP54622298 A JP 54622298A JP 2002512556 A JP2002512556 A JP 2002512556A
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- JP
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- Prior art keywords
- catalyst
- rhenium
- acid
- metals
- cobalt
- Prior art date
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- 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
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- 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
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- 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
- B01J37/0203—Impregnation the impregnation liquid containing organic compounds
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
- C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
- C07C1/0425—Catalysts; their physical properties
- C07C1/0445—Preparation; Activation
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
- C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
- C07C1/0485—Set-up of reactors or accessories; Multi-step processes
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- 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
-
- 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
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/32—Manganese, technetium or rhenium
- C07C2523/36—Rhenium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
- C07C2523/75—Cobalt
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
- C07C2523/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/889—Manganese, technetium or rhenium
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S502/00—Catalyst, solid sorbent, or support therefor: product or process of making
- Y10S502/506—Method of making inorganic composition utilizing organic compound, except formic, acetic, or oxalic acid or salt thereof
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S502/00—Catalyst, solid sorbent, or support therefor: product or process of making
- Y10S502/514—Process applicable either to preparing or to regenerating or to rehabilitating catalyst or sorbent
Abstract
Description
Claims (1)
- 【特許請求の範囲】 1.一酸化炭素の水素化に有用な触媒を調製するための方法であって、該方法は 、耐火性無機酸化物担体を、下記成分(a)〜(c)を含む溶液と接触させるこ とによって含浸させ、次いで乾燥し、多官能性カルボン酸を除去し、触媒組成物 上に金属酸化物を形成することを特徴とする触媒の調製方法。 (a)1種もしくは複数種の触媒金属の化合物または塩 (b)式HOOC-(CRR1)n-COOHを有する多官能性カルボン酸 ここで、nは1〜約4の整数であり、置換基RおよびR1は水素、ハイ ドロカルビル、ヒドロキシル、カルボキシル、アミノおよびアルコキシからなる 群れから選ばれる同一または異なる基であって、担体上に1種もしくは複数種の 触媒金属の化合物または塩を分散させるのに十分な基である。 (c)レニウムの化合物または塩 2.該含浸は、初期湿潤を経由することを特徴とする請求の範囲1記載の触媒の 調製方法。 3.該1種もしくは複数種の触媒金属、該レニウム、および該酸は、単一の含浸 溶液から担体上に共析出されることを特徴とする請求の範囲1記載の触媒の調製 方法。 4.担体上に含浸された該1種もしくは複数種の触媒金属は、銅または鉄族金属 を含み、該式HOOC-(CRR1)n-COOHのnは、約2〜3であることを特徴 とする請求の範囲1記載の触媒の調製方法。 5.該1種もしくは複数種の触媒金属、該レニウム、および該酸は、初期湿潤を 経由して担体上に単一の含浸溶液から共析出され、該1種もしくは複数種の触媒 金属は、コバルトを含み、さらに該式HOOC-(CRR1)n-COOHのnは、約 2〜約3であることを特徴とする請求の範囲1記載の触媒の調製方法。 6.該レニウムは、元素レニウム:銅または鉄族金属の重量比が約0.005: 1〜約0.2:1の範囲になるのに十分な濃度で担体に加えられることを特徴と する請求の範囲1記載の触媒の調製方法。 7.該多官能性カルボン酸は、カルボン酸:金属のモル比が約0.1:1〜約0 .6:1の範囲になるのに十分な濃度で含浸溶液に加えられることを特徴とする 請求の範囲1記載の触媒の調製方法。 8.担体上に含浸された該1種もしくは複数種の触媒金属は、銅または鉄族金属 を含み、該レニウムは、元素レニウム:元素銅または鉄族金属の重量比が約0. 005:1〜約0.2:1の範囲で担体に加えられることを特徴とする請求の範 囲1記載の触媒の調製方法。 9.請求の範囲1〜8のいずれかに記載されるステップによって調製されること を特徴とする触媒。 10.水素と一酸化炭素からなる合成ガスを反応条件の下で触媒と接触させるこ とによりC5+液体炭化水素を製造する方法において、該触媒は、請求の範囲1〜 8のいずれかに記載されるステップによって調 製されることを特徴とする触媒の調製方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/847,958 US5863856A (en) | 1997-04-22 | 1997-04-22 | Preparation of high activity catalysts the catalysts and their use |
US08/847,958 | 1997-04-22 | ||
PCT/US1998/007888 WO1998047618A1 (en) | 1997-04-22 | 1998-04-17 | Preparation of high activity catalysts, the catalysts and their use |
Publications (2)
Publication Number | Publication Date |
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JP2002512556A true JP2002512556A (ja) | 2002-04-23 |
JP4210337B2 JP4210337B2 (ja) | 2009-01-14 |
Family
ID=25301952
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP54622298A Expired - Fee Related JP4210337B2 (ja) | 1997-04-22 | 1998-04-17 | 高活性触媒の調製方法ならびに該触媒およびその使用 |
Country Status (9)
Country | Link |
---|---|
US (3) | US5863856A (ja) |
EP (1) | EP0977630B1 (ja) |
JP (1) | JP4210337B2 (ja) |
AU (1) | AU731432B2 (ja) |
CA (1) | CA2285062C (ja) |
DE (1) | DE69827617T2 (ja) |
MY (1) | MY133867A (ja) |
NO (1) | NO995135D0 (ja) |
WO (1) | WO1998047618A1 (ja) |
Cited By (6)
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JP2006506224A (ja) * | 2002-11-20 | 2006-02-23 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 触媒の製造方法 |
JP2006506430A (ja) * | 2002-11-20 | 2006-02-23 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 水素化方法 |
JP2007519805A (ja) | 2004-01-28 | 2007-07-19 | ヴェロシス,インク. | マイクロチャネル技術を用いるフィッシャー・トロプシュ合成ならびに新規な触媒およびマイクロチャネル反応器 |
JP2011528984A (ja) * | 2008-07-25 | 2011-12-01 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 高活性コバルト触媒の調製、触媒、およびそれらの使用 |
WO2016136969A1 (ja) * | 2015-02-27 | 2016-09-01 | 国立大学法人九州大学 | 後周期遷移金属微粒子担持体の製造方法 |
CN111036932A (zh) * | 2019-08-02 | 2020-04-21 | 浙江工业大学 | 一种液相还原制备金属铼的方法 |
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FR3050659B1 (fr) | 2016-04-29 | 2021-09-03 | Ifp Energies Now | Catalyseur de cobalt a base d'un support contenant une phase d'oxyde mixte contenant du cobalt et/ou du nickel prepare par l'utilisation d'un compose ester |
FR3050660B1 (fr) | 2016-04-29 | 2021-09-03 | Ifp Energies Now | Catalyseur de cobalt a base d'un support contenant une phase d'oxyde mixte contenant du cobalt et/ou du nickel prepare par l'utilisation d'un compose comportant deux fontions acides carboxyliques et au moins trois atomes de carbone |
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MY197616A (en) | 2016-11-07 | 2023-06-28 | Shell Int Research | Method of producing hydrocarbons |
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FR3119556A1 (fr) | 2021-02-11 | 2022-08-12 | IFP Energies Nouvelles | Procédé de préparation d’un catalyseur de Fischer-Tropsch en présence d’un additif et d’une étape de calcination spécifique |
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- 1998-04-17 WO PCT/US1998/007888 patent/WO1998047618A1/en active IP Right Grant
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- 1998-04-17 CA CA002285062A patent/CA2285062C/en not_active Expired - Fee Related
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JP2006506224A (ja) * | 2002-11-20 | 2006-02-23 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 触媒の製造方法 |
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CN111036932A (zh) * | 2019-08-02 | 2020-04-21 | 浙江工业大学 | 一种液相还原制备金属铼的方法 |
Also Published As
Publication number | Publication date |
---|---|
DE69827617T2 (de) | 2005-10-06 |
AU731432B2 (en) | 2001-03-29 |
DE69827617D1 (de) | 2004-12-23 |
CA2285062C (en) | 2006-11-21 |
AU7136898A (en) | 1998-11-13 |
WO1998047618A1 (en) | 1998-10-29 |
US5863856A (en) | 1999-01-26 |
JP4210337B2 (ja) | 2009-01-14 |
NO995135L (no) | 1999-10-21 |
EP0977630B1 (en) | 2004-11-17 |
US5968991A (en) | 1999-10-19 |
US5945459A (en) | 1999-08-31 |
MY133867A (en) | 2007-11-30 |
EP0977630A1 (en) | 2000-02-09 |
CA2285062A1 (en) | 1998-10-29 |
NO995135D0 (no) | 1999-10-21 |
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