ATE337385T1 - Katalytischer reaktor und verfahren - Google Patents

Katalytischer reaktor und verfahren

Info

Publication number
ATE337385T1
ATE337385T1 AT03778556T AT03778556T ATE337385T1 AT E337385 T1 ATE337385 T1 AT E337385T1 AT 03778556 T AT03778556 T AT 03778556T AT 03778556 T AT03778556 T AT 03778556T AT E337385 T1 ATE337385 T1 AT E337385T1
Authority
AT
Austria
Prior art keywords
channels
fischer
header
stages
channel
Prior art date
Application number
AT03778556T
Other languages
English (en)
Inventor
Michael Joseph Bowe
Clive Derek Lee-Tuffnell
Original Assignee
Gtl Microsystems Ag
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=32472134&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ATE337385(T1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority claimed from PCT/GB2002/005443 external-priority patent/WO2003048035A1/en
Priority claimed from GBGB0314790.7A external-priority patent/GB0314790D0/en
Application filed by Gtl Microsystems Ag filed Critical Gtl Microsystems Ag
Application granted granted Critical
Publication of ATE337385T1 publication Critical patent/ATE337385T1/de

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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • 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
    • C10G2/34—Apparatus, reactors
    • C10G2/341—Apparatus, reactors with stationary catalyst bed
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/249—Plate-type reactors
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/2495—Net-type reactors
    • 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
    • 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
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2465—Two reactions in indirect heat exchange with each other
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2469—Feeding means
    • B01J2219/247—Feeding means for the reactants
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
AT03778556T 2002-12-02 2003-11-27 Katalytischer reaktor und verfahren ATE337385T1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
PCT/GB2002/005443 WO2003048035A1 (en) 2001-12-05 2002-12-02 Process and apparatus for steam-methane reforming
GBGB0314790.7A GB0314790D0 (en) 2003-06-25 2003-06-25 Catalytic reactor and process

Publications (1)

Publication Number Publication Date
ATE337385T1 true ATE337385T1 (de) 2006-09-15

Family

ID=32472134

Family Applications (1)

Application Number Title Priority Date Filing Date
AT03778556T ATE337385T1 (de) 2002-12-02 2003-11-27 Katalytischer reaktor und verfahren

Country Status (8)

Country Link
EP (1) EP1567616B2 (de)
JP (1) JP4446388B2 (de)
AT (1) ATE337385T1 (de)
AU (1) AU2003285558B2 (de)
DE (1) DE60307885T3 (de)
MX (1) MXPA05005870A (de)
RU (1) RU2310677C2 (de)
WO (1) WO2004050799A1 (de)

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US6622519B1 (en) 2002-08-15 2003-09-23 Velocys, Inc. Process for cooling a product in a heat exchanger employing microchannels for the flow of refrigerant and product
US6969505B2 (en) 2002-08-15 2005-11-29 Velocys, Inc. Process for conducting an equilibrium limited chemical reaction in a single stage process channel
US7014835B2 (en) 2002-08-15 2006-03-21 Velocys, Inc. Multi-stream microchannel device
US7118920B2 (en) * 2002-10-22 2006-10-10 Battelle Memorial Institute Multiphasic microchannel reactions
US7294734B2 (en) 2003-05-02 2007-11-13 Velocys, Inc. Process for converting a hydrocarbon to an oxygenate or a nitrile
US7485671B2 (en) 2003-05-16 2009-02-03 Velocys, Inc. Process for forming an emulsion using microchannel process technology
DE602004009681T2 (de) 2003-05-16 2008-08-14 Velocys, Inc., Plain City Verfahren zur erzeugung einer emulsion durch verwendung einer mikrokanalverfahrentechnologie
US8580211B2 (en) 2003-05-16 2013-11-12 Velocys, Inc. Microchannel with internal fin support for catalyst or sorption medium
US7220390B2 (en) 2003-05-16 2007-05-22 Velocys, Inc. Microchannel with internal fin support for catalyst or sorption medium
CA2535842C (en) 2003-08-29 2012-07-10 Velocys Inc. Process for separating nitrogen from methane using microchannel process technology
US7029647B2 (en) 2004-01-27 2006-04-18 Velocys, Inc. Process for producing hydrogen peroxide using microchannel technology
US7084180B2 (en) 2004-01-28 2006-08-01 Velocys, Inc. Fischer-tropsch synthesis using microchannel technology and novel catalyst and microchannel reactor
US9023900B2 (en) 2004-01-28 2015-05-05 Velocys, Inc. Fischer-Tropsch synthesis using microchannel technology and novel catalyst and microchannel reactor
US8747805B2 (en) 2004-02-11 2014-06-10 Velocys, Inc. Process for conducting an equilibrium limited chemical reaction using microchannel technology
US7304198B2 (en) 2004-05-14 2007-12-04 Battelle Memorial Institute Staged alkylation in microchannels
GB0413400D0 (en) * 2004-06-16 2004-07-21 Accentus Plc Catalytic plant and process
CA2574113C (en) 2004-07-23 2014-02-18 Anna Lee Tonkovich Distillation process using microchannel technology
US7305850B2 (en) 2004-07-23 2007-12-11 Velocys, Inc. Distillation process using microchannel technology
CN101023068B (zh) 2004-08-12 2013-02-13 万罗赛斯公司 使用微通道工艺技术将乙烯转化成环氧乙烷的方法
EP1804964A1 (de) 2004-10-01 2007-07-11 Velocys Inc. Mehrphasiges mischverfahren mit mikrokanalverarbeitungstechnologie
EP1817102A1 (de) 2004-11-12 2007-08-15 Velocys, Inc. Verfahren unter verwendung von mikrokanaltechnologie zur durchführung einer alkylierungs- oder acylierungsreaktion
CA2587546C (en) 2004-11-16 2013-07-09 Velocys Inc. Multiphase reaction process using microchannel technology
GB0501731D0 (en) * 2005-01-31 2005-03-02 Accentus Plc Catalytic reactor
US7507274B2 (en) 2005-03-02 2009-03-24 Velocys, Inc. Separation process using microchannel technology
EP1890802A2 (de) 2005-05-25 2008-02-27 Velocys, Inc. Träger zur verwendung bei der mikrokanalverarbeitung
GB0513484D0 (en) * 2005-07-01 2005-08-10 Accentus Plc Producing liquid hydrocarbons
EP1904223A2 (de) 2005-07-08 2008-04-02 Velocys Inc. Verfahren für eine katalytische reaktion unter verwendung von mikrokanaltechnologie
CA2675816C (en) 2007-01-19 2015-09-01 Velocys, Inc. Process and apparatus for converting natural gas to higher molecular weight hydrocarbons using microchannel process technology
GB0725140D0 (en) * 2007-12-24 2008-01-30 Compactgtl Plc Catalytic Reactor
WO2009126765A2 (en) 2008-04-09 2009-10-15 Velocys Inc. Process for converting a carbonaceous material to methane, methanol and/or dimethyl ether using microchannel process technology
US8100996B2 (en) 2008-04-09 2012-01-24 Velocys, Inc. Process for upgrading a carbonaceous material using microchannel process technology
US8747656B2 (en) 2008-10-10 2014-06-10 Velocys, Inc. Process and apparatus employing microchannel process technology
JP5581028B2 (ja) * 2009-09-16 2014-08-27 住友精密工業株式会社 触媒反応器
GB201007196D0 (en) 2010-04-30 2010-06-16 Compactgtl Plc Gas-to-liquid technology
RU2442819C1 (ru) * 2010-07-05 2012-02-20 Учреждение Российской Академии наук Институт катализа им. Г.К. Борескова Сибирского отделения РАН (ИК СО РАН) Способ работы устройства для переработки попутных нефтяных газов
GB201107070D0 (en) * 2011-04-27 2011-06-08 Davy Process Techn Ltd FT process using can reactor
GB201112028D0 (en) 2011-07-13 2011-08-31 Gas2 Ltd Fixed bed fischer tropsch reactor
GB201120327D0 (en) 2011-11-24 2012-01-04 Compactgtl Plc Oil well product treatment
GB201214122D0 (en) 2012-08-07 2012-09-19 Oxford Catalysts Ltd Treating of catalyst support
US9676623B2 (en) 2013-03-14 2017-06-13 Velocys, Inc. Process and apparatus for conducting simultaneous endothermic and exothermic reactions
WO2016201218A2 (en) 2015-06-12 2016-12-15 Velocys, Inc. Synthesis gas conversion process
RU2610526C2 (ru) * 2015-06-18 2017-02-13 Открытое акционерное общество "Нефтяная компания "Роснефть" Катализатор для осуществления процесса Фишера-Тропша в компактном варианте и способ его получения (варианты)
RU2638217C1 (ru) * 2016-12-15 2017-12-12 Публичное акционерное общество "Нефтяная компания "Роснефть" Компактный реактор для получения синтетических углеводородов в процессе Фишера-Тропша, способ активации катализатора Фишера-Тропша и способ осуществления синтеза Фишера-Тропша в компактном варианте с его использованием
FR3073152B1 (fr) * 2017-11-09 2022-03-11 Aer Unite d'hydrogenation d'oxydes de carbone a taux de conversion accru, dont la performance depend faiblement du vieillissement du catalyseur
DE102021110735A1 (de) 2021-04-27 2022-10-27 Ineratec Gmbh Verfahren zur Herstellung von Kohlenwasserstoffen

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Also Published As

Publication number Publication date
JP2006508234A (ja) 2006-03-09
DE60307885T3 (de) 2010-12-16
EP1567616B2 (de) 2010-08-18
EP1567616A1 (de) 2005-08-31
MXPA05005870A (es) 2005-08-26
RU2005120773A (ru) 2006-01-20
DE60307885T2 (de) 2007-02-01
DE60307885D1 (de) 2006-10-05
AU2003285558A1 (en) 2004-06-23
AU2003285558B2 (en) 2009-07-16
WO2004050799A1 (en) 2004-06-17
RU2310677C2 (ru) 2007-11-20
JP4446388B2 (ja) 2010-04-07
EP1567616B1 (de) 2006-08-23

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