RU2012141026A - Способ получения активированного катализатора синтеза фишера-тропша и способ получения углеводородов - Google Patents
Способ получения активированного катализатора синтеза фишера-тропша и способ получения углеводородов Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract 22
- 238000003786 synthesis reaction Methods 0.000 title claims abstract 17
- 230000015572 biosynthetic process Effects 0.000 title claims abstract 16
- 238000004519 manufacturing process Methods 0.000 title claims abstract 13
- 229930195733 hydrocarbon Natural products 0.000 title claims 2
- 150000002430 hydrocarbons Chemical class 0.000 title claims 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract 11
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract 6
- 239000001257 hydrogen Substances 0.000 claims abstract 6
- 229910052809 inorganic oxide Inorganic materials 0.000 claims abstract 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract 4
- 239000007789 gas Substances 0.000 claims abstract 4
- 229910052751 metal Inorganic materials 0.000 claims abstract 4
- 239000002184 metal Substances 0.000 claims abstract 4
- 230000006641 stabilisation Effects 0.000 claims abstract 4
- 238000011105 stabilization Methods 0.000 claims abstract 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract 3
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract 3
- 238000000034 method Methods 0.000 claims abstract 3
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical group [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical group [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims abstract 2
- 150000001869 cobalt compounds Chemical class 0.000 claims abstract 2
- 150000003304 ruthenium compounds Chemical class 0.000 claims abstract 2
- 239000000377 silicon dioxide Substances 0.000 claims abstract 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 1
- 235000012239 silicon dioxide Nutrition 0.000 claims 1
- 229910052726 zirconium Inorganic materials 0.000 claims 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- 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
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/066—Zirconium or hafnium; Oxides or hydroxides thereof
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/08—Silica
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
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- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/009—Preparation by separation, e.g. by filtration, decantation, screening
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
- B01J37/0207—Pretreatment of the support
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
- B01J37/082—Decomposition and pyrolysis
- B01J37/088—Decomposition of a metal salt
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/12—Oxidising
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/16—Reducing
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/34—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
- B01J37/341—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation
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- 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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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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- C10G2300/4006—Temperature
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/70—Catalyst aspects
- C10G2300/703—Activation
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Abstract
1. Способ получения активированного катализатора синтеза Фишера-Тропша, включающий:стадию восстановления водородом катализатора, содержащего в качестве атома металла соединения кобальта и/или соединения рутения в количестве от 3 до 50 мас.ч. относительно 100 мас.ч. носителя, содержащего пористый неорганический оксид, где металл нанесен на носитель, путем восстановления в газе, содержащем молекулярный водород при температуре от 300°С до 600°С; истадию восстановления СО, включающую восстановление катализатора в газе, содержащем монооксид углерода и не содержащем молекулярного водорода при температуре от 200°С до 400°С.2. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1, в котором стадия восстановления СО предусмотрена после стадии восстановления водородом.3. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, в котором пористый неорганический оксид является диоксидом кремния и/или оксидом алюминия.4. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, дополнительно включающий:стадию стабилизационной обработки активированного катализатора, где стабилизационная стадия проводится после завершения как стадии восстановления водородом, так и стадии восстановления СО.5. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, в котором степень восстановления атомов кобальта и/или атомов рутения в активированном катализаторе синтеза Фишера-Тропша составляет от 70 мол.% до 95 мол.%.6. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, в котором носитель, содержащий пористый неорганичес
Claims (7)
1. Способ получения активированного катализатора синтеза Фишера-Тропша, включающий:
стадию восстановления водородом катализатора, содержащего в качестве атома металла соединения кобальта и/или соединения рутения в количестве от 3 до 50 мас.ч. относительно 100 мас.ч. носителя, содержащего пористый неорганический оксид, где металл нанесен на носитель, путем восстановления в газе, содержащем молекулярный водород при температуре от 300°С до 600°С; и
стадию восстановления СО, включающую восстановление катализатора в газе, содержащем монооксид углерода и не содержащем молекулярного водорода при температуре от 200°С до 400°С.
2. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1, в котором стадия восстановления СО предусмотрена после стадии восстановления водородом.
3. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, в котором пористый неорганический оксид является диоксидом кремния и/или оксидом алюминия.
4. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, дополнительно включающий:
стадию стабилизационной обработки активированного катализатора, где стабилизационная стадия проводится после завершения как стадии восстановления водородом, так и стадии восстановления СО.
5. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, в котором степень восстановления атомов кобальта и/или атомов рутения в активированном катализаторе синтеза Фишера-Тропша составляет от 70 мол.% до 95 мол.%.
6. Способ получения активированного катализатора синтеза Фишера-Тропша по п.1 или 2, в котором носитель, содержащий пористый неорганический оксид, дополнительно содержит цирконий.
7. Способ получения углеводородов, в котором исходное сырье, содержащее монооксид углерода и газообразный водород, подвергают реакции синтеза Фишера-Тропша в присутствии активированного катализатора синтеза Фишера-Тропша, полученного способом по любому из пп.1-6.
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Application Number | Priority Date | Filing Date | Title |
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JP2010043003A JP5676120B2 (ja) | 2010-02-26 | 2010-02-26 | 活性化フィッシャー・トロプシュ合成触媒の製造方法及び炭化水素の製造方法 |
JP2010-043003 | 2010-02-26 | ||
PCT/JP2011/050126 WO2011105118A1 (ja) | 2010-02-26 | 2011-01-06 | 活性化フィッシャー・トロプシュ合成触媒の製造方法及び炭化水素の製造方法 |
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RU2012141026A true RU2012141026A (ru) | 2014-04-10 |
RU2556211C2 RU2556211C2 (ru) | 2015-07-10 |
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US (1) | US8557879B2 (ru) |
JP (1) | JP5676120B2 (ru) |
CN (1) | CN102770204B (ru) |
AU (1) | AU2011219264B2 (ru) |
CA (1) | CA2790389C (ru) |
MY (1) | MY156584A (ru) |
RU (1) | RU2556211C2 (ru) |
WO (1) | WO2011105118A1 (ru) |
ZA (1) | ZA201206409B (ru) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
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EP2898947A4 (en) * | 2012-09-21 | 2016-10-05 | Jx Nippon Oil & Energy Corp | FISCHER-TROPSCH SYNTHESIS CATALYST, PROCESS FOR PRODUCING THE SAME, AND PROCESS FOR PRODUCING HYDROCARBONS |
MY169931A (en) * | 2012-10-24 | 2019-06-17 | Sasol Tech Pty Ltd | Process for preparing a fischer-tropsch catalyst |
CN103406137B (zh) * | 2013-08-09 | 2015-06-17 | 南京大学 | 用于费托合成的氮掺杂碳纳米管负载型催化剂 |
JP6007167B2 (ja) * | 2013-11-18 | 2016-10-12 | Jxエネルギー株式会社 | フィッシャー・トロプシュ合成用触媒の製造方法及び炭化水素の製造方法 |
WO2016091694A1 (en) | 2014-12-12 | 2016-06-16 | Bp P.L.C. | Process for producing a supported, partially reductively activated fischer-tropsch synthesis catalyst, and process for producing hydrocarbons using the same |
WO2016091696A1 (en) * | 2014-12-12 | 2016-06-16 | Bp P.L.C. | Process for producing a partially reductively activated fischer-tropsch synthesis catalyst, and process for producing hydrocarbons using the same |
WO2016091692A1 (en) | 2014-12-12 | 2016-06-16 | Bp P.L.C. | Process for producing a supported reductively activated fischer-tropsch synthesis catalyst, and process for producing hydrocarbons using the same |
WO2016091695A1 (en) | 2014-12-12 | 2016-06-16 | Bp P.L.C. | Process for producing a reductively activated fischer-tropsch synthesis catalyst, and process for producing hydrocarbons using the same |
FR3039432B1 (fr) * | 2015-07-31 | 2017-08-04 | Ifp Energies Now | Procede de preparation d'un catalyseur destine a etre mis en œuvre dans une reaction fischer-tropsch. |
CN105772049B (zh) * | 2016-04-06 | 2019-05-07 | 中国科学院上海高等研究院 | 一种用于合成气直接制备烯烃的碳化钴基催化剂及其制备方法和应用 |
CN107029724B (zh) * | 2017-04-13 | 2019-08-02 | 济南大学 | 一种用co还原改性重整制氢钴基催化剂的制备方法 |
CN109675593B (zh) * | 2017-10-18 | 2021-07-09 | 中国石油化工股份有限公司 | 含铁费托合成催化剂及其制备方法和费托合成反应的方法 |
CN109675642B (zh) * | 2017-10-18 | 2021-07-09 | 中国石油化工股份有限公司 | 微通道费托合成催化剂及其制备方法和费托合成反应的方法 |
CN113467387A (zh) * | 2020-03-31 | 2021-10-01 | 国家能源投资集团有限责任公司 | 用于活化费托合成催化剂过程的控制图、监控方法及装置 |
US20230015935A1 (en) * | 2021-07-15 | 2023-01-19 | Emerging Fuels Technology, Inc. | Method for the activation or rejuvenation of a catalyst |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0110449B1 (en) | 1982-11-22 | 1986-08-13 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation of a fischer-tropsch catalyst, a catalyst so prepared and use of this catalyst in the preparation of hydrocarbons |
IN164465B (ru) * | 1984-07-06 | 1989-03-18 | Shell Int Research | |
GB9010075D0 (en) | 1990-05-04 | 1990-06-27 | Shell Int Research | Process for the preparation of alumina based extrudates |
PE31698A1 (es) * | 1995-11-08 | 1998-06-15 | Shell Int Research | Proceso de activacion y rejuvenecimiento de catalizador |
FR2801228B1 (fr) * | 1999-11-22 | 2001-12-28 | Inst Francais Du Petrole | Procede d'activation d'un catalyseur de synthese fischer tropsch |
US6696502B1 (en) * | 2000-06-02 | 2004-02-24 | Exxonmobil Research And Engineering Company | Slurry hydrocarbon synthesis with fresh catalyst activity increase during hydrocarbon production |
GB0227081D0 (en) * | 2002-11-20 | 2002-12-24 | Exxonmobil Res & Eng Co | Methods for preparing catalysts |
JP4227847B2 (ja) | 2003-06-23 | 2009-02-18 | 株式会社リコー | 画像形成装置及び位置ずれ補正方法 |
MY142111A (en) * | 2004-04-16 | 2010-09-15 | Nippon Oil Corp | Catalyst for fischer-tropsch synthesis and process for producing hydrocarbons |
GB0510316D0 (en) * | 2005-05-20 | 2005-06-29 | Johnson Matthey Plc | Catalyst manufacture |
JP4982987B2 (ja) | 2005-09-20 | 2012-07-25 | Dic株式会社 | 被覆用樹脂組成物 |
JP4808688B2 (ja) * | 2006-08-25 | 2011-11-02 | 新日本製鐵株式会社 | 合成ガスから炭化水素を製造する触媒、触媒の製造方法、触媒の再生方法、及び合成ガスから炭化水素を製造する方法 |
WO2008099695A1 (ja) * | 2007-02-14 | 2008-08-21 | Nippon Oil Corporation | 一酸化炭素の還元による炭化水素の製造方法 |
-
2010
- 2010-02-26 JP JP2010043003A patent/JP5676120B2/ja not_active Expired - Fee Related
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2011
- 2011-01-06 CA CA2790389A patent/CA2790389C/en not_active Expired - Fee Related
- 2011-01-06 WO PCT/JP2011/050126 patent/WO2011105118A1/ja active Application Filing
- 2011-01-06 CN CN201180011182.7A patent/CN102770204B/zh not_active Expired - Fee Related
- 2011-01-06 RU RU2012141026/04A patent/RU2556211C2/ru not_active IP Right Cessation
- 2011-01-06 US US13/580,239 patent/US8557879B2/en not_active Expired - Fee Related
- 2011-01-06 AU AU2011219264A patent/AU2011219264B2/en not_active Ceased
- 2011-01-06 MY MYPI2012700572A patent/MY156584A/en unknown
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2012
- 2012-08-24 ZA ZA2012/06409A patent/ZA201206409B/en unknown
Also Published As
Publication number | Publication date |
---|---|
CN102770204B (zh) | 2014-11-12 |
RU2556211C2 (ru) | 2015-07-10 |
CN102770204A (zh) | 2012-11-07 |
US20130041052A1 (en) | 2013-02-14 |
CA2790389A1 (en) | 2011-09-01 |
JP5676120B2 (ja) | 2015-02-25 |
WO2011105118A1 (ja) | 2011-09-01 |
MY156584A (en) | 2016-03-15 |
AU2011219264A1 (en) | 2012-09-06 |
JP2011177626A (ja) | 2011-09-15 |
CA2790389C (en) | 2017-05-23 |
AU2011219264B2 (en) | 2016-07-14 |
US8557879B2 (en) | 2013-10-15 |
ZA201206409B (en) | 2013-03-27 |
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