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BR9808808A - Processo de sìntese de hidrocarbonetos em suspensão para a produção de hidrocarbonetos - Google Patents

Processo de sìntese de hidrocarbonetos em suspensão para a produção de hidrocarbonetos

Info

Publication number
BR9808808A
BR9808808A BR9808808-4A BR9808808A BR9808808A BR 9808808 A BR9808808 A BR 9808808A BR 9808808 A BR9808808 A BR 9808808A BR 9808808 A BR9808808 A BR 9808808A
Authority
BR
Brazil
Prior art keywords
suspension
reactor
vessel
hydrocarbons
gas
Prior art date
Application number
BR9808808-4A
Other languages
English (en)
Inventor
Charles William Degeorge
Min Chang
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 BR9808808A publication Critical patent/BR9808808A/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
    • 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
    • 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
    • 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
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • B01J2219/00768—Baffles attached to the reactor wall vertical
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • B01J2219/0077—Baffles attached to the reactor wall inclined

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

"PROCESSO DE SìNTESE DE HIDROCARBONETOS EM SUSPENSãO PARA A PRODUçãO DE HIDROCARBONETOS". Um processo de síntese de hidrocarbonetos em suspensão emprega um vaso de filtração de suspensão externo ao reator de suspensão. A suspensão proveniente do reator é passada através de uma ou mais zonas liberadores de gás e sólidos, uma ou mais das quais podem estar presentes no reator e no vaso, para reduzir o teor de gás e sólidos da suspensão antes desta contactar o filtro no vaso. O filtro separa o líquido de hidrocarbonetos da suspensão do gás e dos sólidos como um filtrado, que é enviado para beneficiamento. Válvulas nos condutos de gás e fluido permitem que o vaso de filtração seja isolado do reator para manutenção, para substituir os filtros e para auxiliar no controle do fluxo da suspensão através do vaso. Um gás rico em hidrogênio pode ser injetado no vaso de filtração para evitar a desativação do catalisador. A suspensão é hidraulicamente circulada entre o reator e o vaso devido a diferenças de densidade enquanto o reator está operando.
BR9808808-4A 1997-05-16 1998-05-15 Processo de sìntese de hidrocarbonetos em suspensão para a produção de hidrocarbonetos BR9808808A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/857,604 US5770629A (en) 1997-05-16 1997-05-16 Slurry hydrocarbon synthesis with external product filtration
PCT/US1998/009941 WO1998051407A1 (en) 1997-05-16 1998-05-15 Slurry hydrocarbon synthesis with external product filtration

Publications (1)

Publication Number Publication Date
BR9808808A true BR9808808A (pt) 2000-07-18

Family

ID=25326349

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9808808-4A BR9808808A (pt) 1997-05-16 1998-05-15 Processo de sìntese de hidrocarbonetos em suspensão para a produção de hidrocarbonetos

Country Status (11)

Country Link
US (1) US5770629A (pt)
EP (1) EP0991463B1 (pt)
JP (1) JP2001526587A (pt)
AU (1) AU721272B2 (pt)
BR (1) BR9808808A (pt)
CA (1) CA2288979A1 (pt)
DE (1) DE69807691T2 (pt)
MY (1) MY114816A (pt)
NO (1) NO995569L (pt)
WO (1) WO1998051407A1 (pt)
ZA (1) ZA983962B (pt)

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US6359018B1 (en) 2000-10-27 2002-03-19 Chevron U.S.A. Inc Process for upflow fixed-bed hydroprocessing of fischer-tropsch wax
US6652760B2 (en) 2001-03-12 2003-11-25 Texaco Inc. Internal filter for fischer-tropsch catalyst/wax separation
FR2826295B1 (fr) * 2001-06-25 2003-09-26 Inst Francais Du Petrole Dispositif et procede optimisant la circulation d'une suspension dans une installation comprenant un reacteur triphasique
AR034670A1 (es) * 2001-07-03 2004-03-03 Shell Int Research Procedimiento de preparacion de hidrocarburos liquidos
US7078439B2 (en) * 2001-12-28 2006-07-18 Conocophillips Company Systems and methods for catalyst/hydrocarbon product separation
US6809122B2 (en) * 2001-12-28 2004-10-26 Conocophillips Company Method for reducing the maximum water concentration in a multi-phase column reactor
US6720358B2 (en) 2001-12-28 2004-04-13 Conocophillips Company Water stripping and catalyst/liquid product separation system
US7001927B2 (en) * 2001-12-28 2006-02-21 Conocophillips Company Water removal in Fischer-Tropsch processes
US6956063B2 (en) * 2001-12-28 2005-10-18 Conocophillips Company Method for reducing water concentration in a multi-phase column reactor
ZA200407224B (en) * 2002-04-16 2006-02-22 Conocophillips Co Solid/liquid separation system for multiphase converters.
US6833078B2 (en) * 2002-09-13 2004-12-21 Conocophillips Company Solid-liquid separation system
US6878655B2 (en) * 2002-09-20 2005-04-12 Conocophillips Company Method and apparatus for the regeneration of hydrocarbon synthesis catalysts
DE602005022833D1 (de) * 2004-03-08 2010-09-23 Shell Int Research Filtersystem mit in ein gehäuse zurückziehbaren filtermitteln
US7332073B2 (en) * 2004-03-31 2008-02-19 Chevron U.S.A. Inc. Process for removing contaminants from Fischer-Tropsch feed streams
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) * 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) * 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
KR100989756B1 (ko) 2005-12-14 2010-10-26 신닛떼쯔 엔지니어링 가부시끼가이샤 기포탑형 피셔ㆍ트롭쉬 합성 슬러리상 반응 방법 및 장치
US7378452B2 (en) * 2005-12-28 2008-05-27 Exxonmobil Research And Engineering Company Filtration system for slurry hydrocarbon synthesis process using both small and large pore filter elements
US20070155987A1 (en) * 2006-01-04 2007-07-05 O'meadhra Ruairi S Oxidative digestion with optimized agitation
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of 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
US20070208194A1 (en) * 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US20080260631A1 (en) 2007-04-18 2008-10-23 H2Gen Innovations, Inc. Hydrogen production process
US20080300417A1 (en) * 2007-05-31 2008-12-04 Te Chang Slurry reaction system
CA2700126C (en) * 2007-09-27 2014-02-18 Japan Oil, Gas And Metals National Corporation Synthesis reaction system
US8022109B2 (en) * 2008-12-23 2011-09-20 Exxonmobil Research And Engineering Company Product filtration system for slurry reactors
US8389585B2 (en) * 2009-02-13 2013-03-05 Exxonmobil Research And Engineering Company Slurry reactor fines segregation and removal
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
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Also Published As

Publication number Publication date
DE69807691D1 (de) 2002-10-10
ZA983962B (en) 1998-11-12
US5770629A (en) 1998-06-23
AU721272B2 (en) 2000-06-29
DE69807691T2 (de) 2003-01-30
CA2288979A1 (en) 1998-11-19
AU7489198A (en) 1998-12-08
NO995569D0 (no) 1999-11-12
MY114816A (en) 2003-01-31
EP0991463A1 (en) 2000-04-12
JP2001526587A (ja) 2001-12-18
WO1998051407A1 (en) 1998-11-19
EP0991463B1 (en) 2002-09-04
NO995569L (no) 2000-01-11

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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.