JP2000185906A5 - - Google Patents

Download PDF

Info

Publication number
JP2000185906A5
JP2000185906A5 JP1999245109A JP24510999A JP2000185906A5 JP 2000185906 A5 JP2000185906 A5 JP 2000185906A5 JP 1999245109 A JP1999245109 A JP 1999245109A JP 24510999 A JP24510999 A JP 24510999A JP 2000185906 A5 JP2000185906 A5 JP 2000185906A5
Authority
JP
Japan
Prior art keywords
reactor
heat exchange
outer tube
autothermal
heat
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
JP1999245109A
Other languages
English (en)
Japanese (ja)
Other versions
JP2000185906A (ja
Filing date
Publication date
Priority claimed from DK199801098A external-priority patent/DK173742B1/da
Application filed filed Critical
Publication of JP2000185906A publication Critical patent/JP2000185906A/ja
Publication of JP2000185906A5 publication Critical patent/JP2000185906A5/ja
Pending legal-status Critical Current

Links

JP11245109A 1998-09-01 1999-08-31 合成ガス製造のための方法及び反応器システム Pending JP2000185906A (ja)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DK199801098 1998-09-01
DK199801098A DK173742B1 (da) 1998-09-01 1998-09-01 Fremgangsmåde og reaktorsystem til fremstilling af syntesegas

Publications (2)

Publication Number Publication Date
JP2000185906A JP2000185906A (ja) 2000-07-04
JP2000185906A5 true JP2000185906A5 (enExample) 2006-08-17

Family

ID=8100972

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11245109A Pending JP2000185906A (ja) 1998-09-01 1999-08-31 合成ガス製造のための方法及び反応器システム

Country Status (9)

Country Link
US (1) US6224789B1 (enExample)
EP (1) EP0983963A3 (enExample)
JP (1) JP2000185906A (enExample)
CN (1) CN1124226C (enExample)
AU (1) AU753603B2 (enExample)
DK (1) DK173742B1 (enExample)
NO (1) NO994029L (enExample)
NZ (1) NZ337468A (enExample)
ZA (1) ZA995562B (enExample)

Families Citing this family (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0025150D0 (en) † 2000-10-13 2000-11-29 Air Prod & Chem A process and apparatus for the production of synthesis gas
US20040161381A1 (en) * 1999-12-02 2004-08-19 Thomsen Soren Gyde Process and reactor for carrying out non-adiabatic catalytic reactions
ES2427927T3 (es) * 1999-12-02 2013-11-04 Haldor Topsoe A/S Proceso para realización de reacciones catalíticas no adiabáticas
US6544494B2 (en) * 2001-05-14 2003-04-08 General Motors Corporation Reformate preheat of ATR reactants
US6890672B2 (en) 2001-06-26 2005-05-10 Idatech, Llc Fuel processor feedstock delivery system
US6855272B2 (en) * 2001-07-18 2005-02-15 Kellogg Brown & Root, Inc. Low pressure drop reforming exchanger
MY138154A (en) * 2001-10-22 2009-04-30 Shell Int Research Process to prepare a hydrogen and carbon monoxide containing gas
US6783879B2 (en) * 2002-01-11 2004-08-31 General Motors Corporation Dynamic fuel processor mechanization and control
US7208530B2 (en) * 2002-02-05 2007-04-24 The Regents Of The University Of California Production of synthetic transportation fuels from carbonaceous material using self-sustained hydro-gasification
US20030162846A1 (en) * 2002-02-25 2003-08-28 Wang Shoou-L Process and apparatus for the production of synthesis gas
EP1516663A3 (en) * 2002-04-14 2006-03-22 IdaTech, LLC. Steam reformer with burner
US20030223926A1 (en) 2002-04-14 2003-12-04 Edlund David J. Steam reforming fuel processor, burner assembly, and methods of operating the same
EP1413547A1 (en) * 2002-09-26 2004-04-28 Haldor Topsoe A/S Process for the production of synthesis gas
ATE502894T1 (de) * 2002-09-26 2011-04-15 Haldor Topsoe As Verfahren zur herstellung von synthesegas
CA2410927A1 (fr) * 2002-11-05 2004-05-05 Michel Petitclerc Reacteur a chauffage electrique pour le reformage en phase gazeuse
ES2381105T3 (es) * 2003-02-05 2012-05-23 Haldor Topsoe A/S Procedimiento para el tratamiento de gas de síntesis
US8273139B2 (en) * 2003-03-16 2012-09-25 Kellogg Brown & Root Llc Catalytic partial oxidation reforming
BRPI0408349A (pt) * 2003-03-18 2006-03-21 Kellogg Brown & Root Inc processos para produzir hidrogênio, para gerar uma corrente elétrica e de hidrotratamento, e, aparelho para preparar singás
CN1832900A (zh) * 2003-04-15 2006-09-13 国际壳牌研究有限公司 制备合成气的方法
US7485767B2 (en) * 2005-06-29 2009-02-03 Exxonmobil Chemical Patents Inc. Production of synthesis gas blends for conversion to methanol or Fischer-Tropsch liquids
KR100762685B1 (ko) * 2005-11-10 2007-10-04 삼성에스디아이 주식회사 개질기 및 이를 채용한 연료전지 시스템
US7939051B2 (en) 2006-05-23 2011-05-10 Idatech, Llc Hydrogen-producing fuel processing assemblies, heating assemblies, and methods of operating the same
US7772292B2 (en) 2006-05-31 2010-08-10 Exxonmobil Chemical Patents Inc. Synthesis gas production and use
US20080260631A1 (en) * 2007-04-18 2008-10-23 H2Gen Innovations, Inc. Hydrogen production process
US7790059B2 (en) * 2007-10-18 2010-09-07 Air Products And Chemicals, Inc. Staged hydrocarbon/steam reformer apparatus and method
EP2421794B1 (en) 2009-04-22 2014-09-03 Shell Internationale Research Maatschappij B.V. Process for the preparation of hydrogen and carbon monoxide containing gas
KR101028850B1 (ko) 2009-07-09 2011-04-12 한국에너지기술연구원 컴팩트 고체산화물 연료전지 시스템
PL2526044T3 (pl) * 2010-01-19 2019-05-31 Topsoe Haldor As Sposób reformowania węglowodorów
EP2676924A1 (en) 2012-06-21 2013-12-25 Haldor Topsoe A/S Process for Reforming Hydrocarbons
GB201219960D0 (en) * 2012-11-06 2012-12-19 Johnson Matthey Plc Process
WO2015128395A1 (en) * 2014-02-28 2015-09-03 Haldor Topsøe A/S Process for the production of synthesis gas
EP3296255A1 (de) * 2016-09-14 2018-03-21 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Reformerrohr mit strukturiertem katalysator und verbessertem wärmehaushalt
UA126249C2 (uk) 2017-12-08 2022-09-07 Хальдор Топсьое А/С Система і спосіб виробництва синтез-газу
US10633603B2 (en) 2018-01-04 2020-04-28 Chevron Phillips Chemical Company Lp Optimized reactor configuration for optimal performance of the aromax catalyst for aromatics synthesis
US10537867B2 (en) 2018-01-04 2020-01-21 Chevron Phillips Chemical Company Lp Optimized reactor configuration for optimal performance of the aromax catalyst for aromatics synthesis
EP4433416A1 (en) 2021-11-15 2024-09-25 Topsoe A/S Blue hydrogen process and plant
ES3036321T3 (en) 2022-11-16 2025-09-17 Topsoe As Plant and process for producing hydrogen with improved operation of a low temperature co2 removal unit
EP4649051A1 (en) 2023-01-10 2025-11-19 Topsoe A/S Blue hydrogen process and plant

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8728882D0 (en) * 1987-12-10 1988-01-27 Ici Plc Hydrogen
EP0334540B1 (en) * 1988-03-24 1993-10-20 Imperial Chemical Industries Plc Two-step steam-reforming process
US5122299A (en) * 1989-12-11 1992-06-16 The M. W. Kellogg Company Autothermal steam reforming process
US5011625A (en) * 1989-12-11 1991-04-30 The M. W. Kellogg Company Autothermal steam reforming process
DE69800734T2 (de) * 1997-01-22 2001-08-09 Haldor Topsoee A/S, Lyngby Erzeugung eines Synthesegases durch Dampfreformierung unter Verwendung eines katalysierten Hardware
DK173052B1 (da) * 1997-05-05 1999-12-06 Topsoe Haldor As Fremgangsmåde til fremstilling af ammoniak syntesegas

Similar Documents

Publication Publication Date Title
JP2000185906A5 (enExample)
RU2218301C2 (ru) Способ и устройство для получения синтез-газа
CA2436997A1 (en) Reactor module for use in a compact fuel processor
JP4479117B2 (ja) 燃料改質装置
RU98102132A (ru) Способ и устройство для получения синтез-газа
RU2354607C2 (ru) Способ и устройство для получения синтез-газа
NL8500238A (nl) Autothermische bereiding van synthesegas.
CN1246441A (zh) 制备合成气的方法和反应器系统
CN111617728A (zh) 一种热交换式重整反应器及重整制氢系统
JPH0449147Y2 (enExample)
JP2011505314A (ja) アンモニア製造法の効率を改善すること
JP2004269345A (ja) 合成ガスの製造方法およびその装置
CN108404821A (zh) 一种节能型高效径向甲醇反应器
US6214296B1 (en) Method of catalytic reaction carried out near the optimal temperature and an apparatus for the method
GB1065044A (en) Catalytic reaction
CN1683065B (zh) 用于冷却放热反应区的方法和反应器单元
RU2005131948A (ru) Реформинг-установка частичного окисления-устройство теплообменника реформинга
CN206950989U (zh) 一种VOCs废气催化氧化设备
CN119957923A (zh) 工业废气催化燃烧设备
CN88100966A (zh) 带有至少一个催化剂床和中心热交换器的二级氨转换器
JP4189732B2 (ja) 内熱式水蒸気改質装置
JP2601707B2 (ja) 触媒反応装置
JP2003156292A (ja) 熱交換器
CN208205892U (zh) 天然气制氢系统中的集成式换热设备
JPH09165202A (ja) 水蒸気改質器