BR9809363A - Processos para rejuvenescimento de um catalisador de sìntese de hidrocarboneto particulado e para sìntese de hidrocarbonetos em lama - Google Patents

Processos para rejuvenescimento de um catalisador de sìntese de hidrocarboneto particulado e para sìntese de hidrocarbonetos em lama

Info

Publication number
BR9809363A
BR9809363A BR9809363-0A BR9809363A BR9809363A BR 9809363 A BR9809363 A BR 9809363A BR 9809363 A BR9809363 A BR 9809363A BR 9809363 A BR9809363 A BR 9809363A
Authority
BR
Brazil
Prior art keywords
gas
rejuvenation
catalyst
sludge
hydrocarbon synthesis
Prior art date
Application number
BR9809363-0A
Other languages
English (en)
Inventor
Min Chang
Constantine A Coulaloglou
Stephen J Hsia
Charles John Mart
Original Assignee
Exxon Research Engineering 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 Exxon Research Engineering Co filed Critical Exxon Research Engineering Co
Publication of BR9809363A publication Critical patent/BR9809363A/pt

Links

Classifications

    • 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
    • B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
    • B01J38/50—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using organic liquids
    • B01J38/58—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using organic liquids and gas addition thereto
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005—Separating solid material from the gas/liquid stream
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005—Separating solid material from the gas/liquid stream
    • B01J8/006—Separating solid material from the gas/liquid stream by filtration
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/224—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
    • B01J8/228—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • 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
    • C07C1/06—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen in the presence of organic compounds, e.g. hydrocarbons
    • C07C1/063—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen in the presence of organic compounds, e.g. hydrocarbons the organic compound being the catalyst or a part of the catalyst system
    • C07C1/066—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen in the presence of organic compounds, e.g. hydrocarbons the organic compound being the catalyst or a part of the catalyst system used for dissolving, suspending or transporting the catalyst
    • 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
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/584—Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

"PROCESSOS PARA REJUVENESCIMENTO DE UM CATALISADOR DE SìNTESE DE HIDROCARBONETO PARTICULADO E PARA SìNTESE DE HIDROCARBONETOS EM LAMA". Um catalisador de síntese de hidrocarboneto reversivelmente desativado em uma lama de síntese de hidrocarboneto é rejuvenescido por passagens sucessivas da lama através de pelo menos dois estágios de rejuvenescimento externos ao reator de lama, cada um dos quais compreende uma zona de rejuvenescimento seguida por uma zona de remoção de gás de topo. Isto é realizado usando-se um tubo de elevação fora do reator pelo qual a lama do reator passa e contata um gás rejuvenescedor de catalisador para parcialmente rejuvenescer as partículas de catalisador e formar um gás de topo do rejuvenescimento. A mistura de gás e lama passa para um vaso no qual o gás é removido da lama. O gás de rejuvenescimento é borbulhado na lama do vaso para rejuvenescer adicionalmente o catalisador. Um tubo de descida removedor de gás remove gás da lama no vaso antes que ela volte para o reator. O gás de rejuvenescimento também age como um gás de elevação no tubo ascendente.
BR9809363-0A 1997-05-02 1998-04-29 Processos para rejuvenescimento de um catalisador de sìntese de hidrocarboneto particulado e para sìntese de hidrocarbonetos em lama BR9809363A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/850,356 US5821270A (en) 1997-05-02 1997-05-02 Slurry hydrocarbon synthesis process with multistage catalyst rejuvenation
PCT/US1998/008690 WO1998050489A1 (en) 1997-05-02 1998-04-29 Slurry hydrocarbon synthesis process with multistage catalyst rejuvenation

Publications (1)

Publication Number Publication Date
BR9809363A true BR9809363A (pt) 2000-07-04

Family

ID=25307907

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9809363-0A BR9809363A (pt) 1997-05-02 1998-04-29 Processos para rejuvenescimento de um catalisador de sìntese de hidrocarboneto particulado e para sìntese de hidrocarbonetos em lama

Country Status (11)

Country Link
US (1) US5821270A (pt)
EP (1) EP0979259B1 (pt)
JP (1) JP3979475B2 (pt)
AU (1) AU727986B2 (pt)
BR (1) BR9809363A (pt)
CA (1) CA2286289C (pt)
DE (1) DE69801321T2 (pt)
MY (1) MY115262A (pt)
NO (1) NO995332L (pt)
WO (1) WO1998050489A1 (pt)
ZA (1) ZA983679B (pt)

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US5958986A (en) * 1997-05-02 1999-09-28 Exxon Research And Engineering Co. Slurry hydrocarbon synthesis process with catalyst rejuvenation in external lift pipe (law544)
US6103773A (en) * 1998-01-27 2000-08-15 Exxon Research And Engineering Co Gas conversion using hydrogen produced from syngas for removing sulfur from gas well hydrocarbon liquids
JP2001081050A (ja) * 1999-09-10 2001-03-27 Nippon Shokubai Co Ltd 易重合性化合物の取り扱い装置および取り扱い方法
US6201030B1 (en) 1999-09-22 2001-03-13 Syntroleum Corporation Process and apparatus for regenerating a particulate catalyst
US6869978B2 (en) 1999-11-17 2005-03-22 Conocophillips Company Pressure swing catalyst regeneration procedure for Fischer-Tropsch catalyst
US6486220B1 (en) 1999-11-17 2002-11-26 Conoco Inc. Regeneration procedure for Fischer-Tropsch catalyst
US6726850B1 (en) * 2000-01-14 2004-04-27 Sebastian C. Reyes Catalytic partial oxidation using staged oxygen addition
AU5719501A (en) * 2000-04-25 2001-11-07 Lexicon Genetics Inc Novel human kinase proteins and polynucleotides encoding the same
US6323248B1 (en) 2000-06-02 2001-11-27 Exxonmobil Research And Engineering Company Slurry hydrocarbon synthesis with fresh catalyst activity increase during hydrocarbon production
US6696502B1 (en) 2000-06-02 2004-02-24 Exxonmobil Research And Engineering Company Slurry hydrocarbon synthesis with fresh catalyst activity increase during hydrocarbon production
US6812179B2 (en) 2001-04-25 2004-11-02 Syntroleum Corporation Process for regenerating a slurry fischer-tropsch catalyst
AU2002303759B2 (en) * 2001-05-17 2006-10-19 Conocophillips Company Pressure swing catalyst regeneration procedure for fischer-tropsch catalyst
CA2451705A1 (en) * 2001-07-13 2003-01-23 Exxonmobil Research And Engineering Company Direct production of high purity fischer-tropsch wax
US6649803B2 (en) 2001-11-06 2003-11-18 Exxonmobil Research And Engineering Company Slurry hydrocarbon synthesis with isomerization zone in external lift reactor loop
US6717024B2 (en) * 2001-11-06 2004-04-06 Exxonmobil Research And Engineering Company Slurry hydrocarbon synthesis with liquid hydroisomerization in the synthesis reactor
US6753286B2 (en) * 2002-01-29 2004-06-22 Exxonmobil Research And Engineering Company Supported catalyst regeneration
US7045554B2 (en) * 2003-09-03 2006-05-16 Conocophillips Company Method for improved Fischer-Tropsch catalyst stability and higher stable syngas conversion
US6838487B1 (en) * 2003-12-04 2005-01-04 Rentech, Inc. Method and apparatus for regenerating an iron-based Fischer-Tropsch catalyst
JP4437436B2 (ja) * 2003-12-22 2010-03-24 株式会社日本触媒 分離装置、それを備えた分離システム及び分離装置の使用方法
US20050154069A1 (en) * 2004-01-13 2005-07-14 Syntroleum Corporation Fischer-Tropsch process in the presence of nitrogen contaminants
US20070208194A1 (en) * 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7420082B2 (en) * 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7393973B2 (en) 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
US7326807B2 (en) * 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system with enhanced heating for oxidative digestion
US7501537B2 (en) * 2006-03-01 2009-03-10 Eastman Chemical Company Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange
US7326808B2 (en) * 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
JP5409370B2 (ja) * 2007-09-27 2014-02-05 新日鉄住金エンジニアリング株式会社 合成反応システム
JP5223073B2 (ja) * 2008-03-14 2013-06-26 独立行政法人石油天然ガス・金属鉱物資源機構 Ｆｔ合成油中の磁性粒子の除去方法
EA018022B1 (ru) * 2008-03-14 2013-04-30 Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн Способ получения синтетической сырой нефти фишера-тропша
JP5841874B2 (ja) 2012-03-28 2016-01-13 独立行政法人石油天然ガス・金属鉱物資源機構 気泡塔型スラリー床反応器の触媒充填装置及び気泡塔型スラリー床反応器の触媒充填方法
WO2014152070A1 (en) * 2013-03-14 2014-09-25 Synthesis Energy Systems, Inc. Method and apparatus for recycling ash fines
US9802971B2 (en) 2014-03-04 2017-10-31 Chevron U.S.A. Inc. Alkane dehydrogenation process
US10017430B2 (en) 2016-08-12 2018-07-10 Chevron U.S.A. Inc. Alkane-alkene coupling via tandem alkane-dehydrogenation/alkene-dimerization catalyzed by pincer iridium catalyst heterogenized on solid supports
CN117643836B (zh) * 2024-01-26 2024-04-09 山东昊瑞环保科技有限公司 一种加氢催化剂再生装置及再生方法

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Also Published As

Publication number Publication date
WO1998050489A1 (en) 1998-11-12
NO995332L (no) 1999-12-20
ZA983679B (en) 1998-11-06
EP0979259A1 (en) 2000-02-16
MY115262A (en) 2003-04-30
JP3979475B2 (ja) 2007-09-19
DE69801321T2 (de) 2002-05-08
CA2286289A1 (en) 1998-11-12
EP0979259B1 (en) 2001-08-08
AU727986B2 (en) 2001-01-04
US5821270A (en) 1998-10-13
DE69801321D1 (de) 2001-09-13
JP2002500687A (ja) 2002-01-08
CA2286289C (en) 2005-11-01
AU7268198A (en) 1998-11-27
NO995332D0 (no) 1999-11-01

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Legal Events

Date Code Title Description
B07A Technical examination (opinion): publication of technical examination (opinion) [chapter 7.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted

Free format text: PRAZO DE VALIDADE: 10 (DEZ) ANOS CONTADOS A PARTIR DE 04/11/2008, OBSERVADAS AS CONDICOES LEGAIS.

B24H Lapse because of non-payment of annual fees (definitively: art 78 iv lpi)
B24F Patent annual fee: publication cancelled

Free format text: ANULADA A PUBLICACAO CODIGO 24.8 NA RPI NO 2258 DE 15/04/2014 POR TER SIDO INDEVIDA.

B21F Lapse acc. art. 78, item iv - on non-payment of the annual fees in time

Free format text: REFERENTE AS 15A, 16A, 17A, 18A, 19A, 20A E 21A ANUIDADES.

B24J Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12)

Free format text: EM VIRTUDE DA EXTINCAO PUBLICADA NA RPI 2606 DE 15-12-2020 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDA A EXTINCAO DA PATENTE E SEUS CERTIFICADOS, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013.