BRPI0606527A2 - reator catalìtico compacto para sìntese fischer-tropsch, planta para converter gás natural em hidrocarbonetos de cadeia mais longa, e reator fischer-tropsch - Google Patents

reator catalìtico compacto para sìntese fischer-tropsch, planta para converter gás natural em hidrocarbonetos de cadeia mais longa, e reator fischer-tropsch

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Publication number
BRPI0606527A2
BRPI0606527A2 BRPI0606527-9A BRPI0606527A BRPI0606527A2 BR PI0606527 A2 BRPI0606527 A2 BR PI0606527A2 BR PI0606527 A BRPI0606527 A BR PI0606527A BR PI0606527 A2 BRPI0606527 A2 BR PI0606527A2
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BR
Brazil
Prior art keywords
fischer
reactor
tropsch
pressure
plant
Prior art date
Application number
BRPI0606527-9A
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English (en)
Inventor
John Vitucci
Michael Joseph Bowe
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Compactgtl Plc
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Publication date
Application filed by Compactgtl Plc filed Critical Compactgtl Plc
Publication of BRPI0606527A2 publication Critical patent/BRPI0606527A2/pt
Publication of BRPI0606527B1 publication Critical patent/BRPI0606527B1/pt

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    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
    • C01B3/34—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts with external heating of the catalyst
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    • C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
    • C01B3/34—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/382—Processes with two or more reaction steps, of which at least one is catalytic, e.g. steam reforming and partial oxidation
    • 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
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Abstract

REATOR CATALìTICO COMPACTO PARA SìNTESE FISCHER-TROPSCH, PLANTA PARA CONVERTER GáS NATURAL EM HIDROCARBONETOS DE CADEIA MAIS LONGA, E REATOR FISCHER-TROPSCH. Um reator catalítico compacto para síntese Fischer-Tropsch (50) compreende um módulo reator (70) defmindo uma multiplicidade de primeiro e segundo canais de fluxo dispostos alternadamente, para transportar uma mistura de gás e um fluido refrigerante, respectivamente. Uma estrutura de catalisador (82) permeável a gás, removível, com um substrato, por exemplo, de folha de metal, é provida em cada canal de fluxo em que deve ocorrer a reação de síntese. O módulo reator (70) é encerrado dentro de um vaso de pressão (90), sendo a pressão dentro do vaso de pressão estabelecida para estar a uma pressão substancialmente igual à da mistura de gás de reação em alta pressão. ConseqUentemente, todos os canais de fluxo, dentro do módulo, estão ou na pressão de seu ambiente, ou estão sob compressão; nenhuma parte se encontra sob tensão. Isto simplifica o projeto do módulo, e aumenta a proporção do volume do reator que pode ser ocupada pelo catalisador.
BRPI0606527A 2005-01-15 2006-01-11 reator catalítico compacto para síntese fischer-tropsch, planta para converter gás natural em hidrocarbonetos de cadeia mais longa, e reator fischer-tropsch BRPI0606527B1 (pt)

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GBGB0500837.0A GB0500837D0 (en) 2005-01-15 2005-01-15 Catalytic reactor
PCT/GB2006/050008 WO2006075193A1 (en) 2005-01-15 2006-01-11 Catalytic reactor

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BRPI0606527A2 true BRPI0606527A2 (pt) 2009-06-30
BRPI0606527B1 BRPI0606527B1 (pt) 2016-01-19

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WO2006075193A1 (en) 2006-07-20
EA200701516A1 (ru) 2008-02-28
GB0500837D0 (en) 2005-02-23
US20080193346A1 (en) 2008-08-14
MX2007008365A (es) 2007-09-21
EP1835991B1 (en) 2008-12-10
EP1835991A1 (en) 2007-09-26
KR101258222B1 (ko) 2013-04-25
CN100574866C (zh) 2009-12-30
EA012058B1 (ru) 2009-08-28
KR20070113204A (ko) 2007-11-28
CA2593609C (en) 2014-08-19
US7749466B2 (en) 2010-07-06
ATE416840T1 (de) 2008-12-15
AU2006205679A1 (en) 2006-07-20
JP5142199B2 (ja) 2013-02-13
JP2008526943A (ja) 2008-07-24
CN101142017A (zh) 2008-03-12
BRPI0606527B1 (pt) 2016-01-19
DE602006004163D1 (de) 2009-01-22
MY140555A (en) 2009-12-31
DK1835991T3 (da) 2009-03-30
AU2006205679B2 (en) 2010-05-06
CA2593609A1 (en) 2006-07-20
NO20073624L (no) 2007-10-12
TW200630159A (en) 2006-09-01

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