BR0214008A - Processos para a ativação de um catalisador regenerado mas não reativado, e de sìntese de hidrocarbonetos, e, métodos para a produção de um lubrificante e de um combustìvel - Google Patents

Processos para a ativação de um catalisador regenerado mas não reativado, e de sìntese de hidrocarbonetos, e, métodos para a produção de um lubrificante e de um combustìvel

Info

Publication number
BR0214008A
BR0214008A BR0214008-0A BR0214008A BR0214008A BR 0214008 A BR0214008 A BR 0214008A BR 0214008 A BR0214008 A BR 0214008A BR 0214008 A BR0214008 A BR 0214008A
Authority
BR
Brazil
Prior art keywords
catalyst
regenerated
reactivated
hcs
reactor
Prior art date
Application number
BR0214008-0A
Other languages
English (en)
Inventor
Stuart Leon Soled
Joseph Ernest Baumgartner
Gabor Kiss
Original Assignee
Exxonmobil Res & Eng Co
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 Exxonmobil Res & Eng Co filed Critical Exxonmobil Res & Eng Co
Publication of BR0214008A publication Critical patent/BR0214008A/pt

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
    • B01J23/90—Regeneration or reactivation
    • B01J23/94—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper
    • 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
    • B01J23/90—Regeneration or reactivation
    • B01J23/96—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the noble 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
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/10—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using elemental hydrogen
    • 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
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • 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
    • C10G2/333—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 platinum-group

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

"PROCESSOS PARA A ATIVAçãO DE UM CATALISADOR REGENERADO MAS NãO REATIVADO, E DE SìNTESE DE HIDROCARBONETOS, E, MéTODOS PARA A PRODUçãO DE UM LUBRIFICANTE E DE UM COMBUSTìVEL". Um processo in situ para executar a regeneração de catalisador desativado de síntese de hidrocarbonetos. O catalisador regenerado (15), mas não ainda reativado, poderá ser introduzido em um reator em operação HCS (1) que possui meios para rejuvenescer o catalisador (14). Qualquer combinação de um catalisador fresco ativado, um catalisador fresco, apassivado, ou catalisadores desativados a longo prazo ou curto prazo, poderão já estar presentes no reator HCS (1). O catalisador regenerado, mas não ainda reativado é ativado no reator HCS (1) com os meios de rejuvenescimento (14) em condições normais de processo. O reator HCS (1) recebe o gás de síntese através da linha de entrada (3) e libera hidrocarbonetos líquidos através da linha de saída (4) e hidrocarbonetos gasosos e gás de síntese não reagido através da linha de gás de saída de gases (2). O catalisador é removido do reator HCS (1) através da linha de descarga (5) para uma unidade de filtração (6) que é alimentada com um fluido de remoção (7). O catalisador filtrado prossegue para a unidade de regeneração (9) a qual é alimentada por um fluido regenerativo (10). O catalisador regenerado retorna para o reator HCS (1) através da linha de retorno de catalisador (11) onde ele é reativado.
BR0214008-0A 2001-11-13 2002-10-15 Processos para a ativação de um catalisador regenerado mas não reativado, e de sìntese de hidrocarbonetos, e, métodos para a produção de um lubrificante e de um combustìvel BR0214008A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/054,228 US6900151B2 (en) 2001-11-13 2001-11-13 In situ catalyst regeneration/activation process
PCT/US2002/032760 WO2003041860A2 (en) 2001-11-13 2002-10-15 In situ catalyst regeneration/activation process

Publications (1)

Publication Number Publication Date
BR0214008A true BR0214008A (pt) 2004-11-03

Family

ID=21989609

Family Applications (1)

Application Number Title Priority Date Filing Date
BR0214008-0A BR0214008A (pt) 2001-11-13 2002-10-15 Processos para a ativação de um catalisador regenerado mas não reativado, e de sìntese de hidrocarbonetos, e, métodos para a produção de um lubrificante e de um combustìvel

Country Status (10)

Country Link
US (1) US6900151B2 (pt)
EP (1) EP1446226A2 (pt)
JP (2) JP4512365B2 (pt)
CN (1) CN100488634C (pt)
AU (1) AU2002335008B2 (pt)
BR (1) BR0214008A (pt)
CA (1) CA2466441C (pt)
TW (1) TWI231812B (pt)
WO (1) WO2003041860A2 (pt)
ZA (1) ZA200403504B (pt)

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US7638039B2 (en) * 2004-06-15 2009-12-29 Cormetech, Inc. In-situ catalyst replacement
US20060111232A1 (en) * 2004-11-22 2006-05-25 Conocophillips Company Multi-staged wax displacement process for catalyst recovery from a slurry
UA98644C2 (ru) * 2007-05-11 2012-06-11 Сасол Текнолоджи (Проприетари) Лимитед Процесс регенерации отработанного катализатора на основе кобальта для синтеза фишера-тропша
US20090023822A1 (en) * 2007-07-19 2009-01-22 Tijm Peter J Method for activating and regenerating catalyst for a fischer-tropsch synthesis reaction
US8614158B2 (en) * 2008-02-29 2013-12-24 Schlumberger Technology Corporation Fischer-trospch and oxygenate synthesis catalyst activation/regeneration in a micro scale process
JP2009214013A (ja) * 2008-03-11 2009-09-24 Ihi Corp フィッシャー・トロプシュ合成触媒の連続再生方法及び装置
US8293805B2 (en) * 2008-05-29 2012-10-23 Schlumberger Technology Corporation Tracking feedstock production with micro scale gas-to-liquid units
EP2408559B1 (en) 2009-03-16 2016-09-28 Saudi Basic Industries Corporation (Sabic) Nickel/lanthana catalyst for producing syngas
WO2011031579A1 (en) 2009-09-08 2011-03-17 Exxonmobil Chemical Patents Inc. Aromatic hydrocarbon purification method
BR112012014717B1 (pt) 2009-12-16 2019-11-12 Shell Int Research processo para regenerar uma ou mais partículas de catalisador de fischer-tropsch que compreendem cobalto
US9062569B2 (en) 2010-10-29 2015-06-23 General Electric Company Systems, methods, and apparatus for regenerating a catalytic material
US9416067B2 (en) 2010-12-22 2016-08-16 Saudi Basic Industries Corporation Catalyst useful in fisher-tropsch synthesis
EP2699344A1 (en) 2011-04-19 2014-02-26 Saudi Basic Industries Corporation Carbon supported cobalt and molybdenum catalyst
EP2729247A1 (en) 2011-07-08 2014-05-14 Saudi Basic Industries Corporation Improved carbon supported cobalt and molybdenum catalyst and use thereof for producing lower alcohols
EP2679568A1 (en) 2012-06-25 2014-01-01 Saudi Basic Industries Corporation Process for production ethylene and propylene from syngas
WO2014001354A1 (en) 2012-06-27 2014-01-03 Saudi Basic Industries Corporation Catalyst and process for the selective production of lower hydrocarbons c1-c5 from syngass with low methane and co2 production
US9827555B2 (en) 2013-07-31 2017-11-28 Saudi Basic Industries Corporation Catalyst for conversion of synthesis gas
BR112017010259B1 (pt) 2014-11-20 2020-12-01 Sasol Technology Proprietary Limited síntese de fischer-tropsch
KR101890044B1 (ko) * 2016-12-26 2018-08-20 한서대학교 산학협력단 중질유 또는 잔사유 수소화 처리 공정용 재생 촉매 및 이의 제조방법
CN108722426B (zh) * 2017-04-19 2021-06-11 中国石油化工股份有限公司 催化剂及制备方法和应用以及催化剂前体还原活化方法以及低碳烯烃的制备方法
CN109331824A (zh) * 2018-10-08 2019-02-15 德清原素高科生物技术有限公司 一种葡萄糖酸钠生产过程中的钯铋炭催化剂的再生工艺
CN109999729B (zh) * 2019-04-26 2022-08-02 上海华畅环保设备发展有限公司 沸腾床加氢反应器中催化剂原位在线旋流活性恢复方法和装置
CN110052226B (zh) * 2019-04-26 2022-08-02 上海华畅环保设备发展有限公司 沸腾床加氢反应器中催化剂原位在线旋流活性恢复方法和装置
CN110124753B (zh) * 2019-06-10 2022-05-24 新疆中泰化学阜康能源有限公司 低汞触媒在线活化再生方法及装置
CN113731023A (zh) * 2020-05-27 2021-12-03 国家能源投资集团有限责任公司 一种费托合成过滤元件的再生方法

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Also Published As

Publication number Publication date
TWI231812B (en) 2005-05-01
EP1446226A2 (en) 2004-08-18
ZA200403504B (en) 2005-05-19
AU2002335008B2 (en) 2007-07-19
JP2005508739A (ja) 2005-04-07
CA2466441C (en) 2010-09-28
JP2010174248A (ja) 2010-08-12
WO2003041860A3 (en) 2003-12-31
CN100488634C (zh) 2009-05-20
CA2466441A1 (en) 2003-05-22
WO2003041860A2 (en) 2003-05-22
CN1610582A (zh) 2005-04-27
JP4512365B2 (ja) 2010-07-28
US20030092781A1 (en) 2003-05-15
US6900151B2 (en) 2005-05-31

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Legal Events

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B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE A 7A E 8A ANUIDADE(S).

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 2108 DE 31/05/2011.