JP2011508043A5 - - Google Patents

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Publication number
JP2011508043A5
JP2011508043A5 JP2010540174A JP2010540174A JP2011508043A5 JP 2011508043 A5 JP2011508043 A5 JP 2011508043A5 JP 2010540174 A JP2010540174 A JP 2010540174A JP 2010540174 A JP2010540174 A JP 2010540174A JP 2011508043 A5 JP2011508043 A5 JP 2011508043A5
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JP
Japan
Prior art keywords
reactor
flow channel
reactor module
fischer
plant
Prior art date
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Granted
Application number
JP2010540174A
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English (en)
Japanese (ja)
Other versions
JP5571573B2 (ja
JP2011508043A (ja
Filing date
Publication date
Priority claimed from GBGB0725140.8A external-priority patent/GB0725140D0/en
Application filed filed Critical
Publication of JP2011508043A publication Critical patent/JP2011508043A/ja
Publication of JP2011508043A5 publication Critical patent/JP2011508043A5/ja
Application granted granted Critical
Publication of JP5571573B2 publication Critical patent/JP5571573B2/ja
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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JP2010540174A 2007-12-24 2008-09-24 触媒反応器 Active JP5571573B2 (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GBGB0725140.8A GB0725140D0 (en) 2007-12-24 2007-12-24 Catalytic Reactor
GB0725140.8 2007-12-24
PCT/GB2008/050855 WO2009081175A1 (en) 2007-12-24 2008-09-24 Catalytic reactor

Publications (3)

Publication Number Publication Date
JP2011508043A JP2011508043A (ja) 2011-03-10
JP2011508043A5 true JP2011508043A5 (https=) 2011-11-04
JP5571573B2 JP5571573B2 (ja) 2014-08-13

Family

ID=39048685

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010540174A Active JP5571573B2 (ja) 2007-12-24 2008-09-24 触媒反応器

Country Status (14)

Country Link
US (1) US8444939B2 (https=)
EP (1) EP2227325B1 (https=)
JP (1) JP5571573B2 (https=)
KR (1) KR20100101158A (https=)
CN (1) CN101932379B (https=)
AU (1) AU2008339634B2 (https=)
BR (1) BRPI0821525A8 (https=)
CA (1) CA2708821C (https=)
DK (1) DK2227325T3 (https=)
EA (1) EA019964B1 (https=)
GB (1) GB0725140D0 (https=)
MY (1) MY157456A (https=)
WO (1) WO2009081175A1 (https=)
ZA (1) ZA201004401B (https=)

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2002349143A1 (en) * 2001-12-05 2003-06-17 GTL Mircosystems AG Process an apparatus for steam-methane reforming
MY180104A (en) * 2007-10-02 2020-11-23 Compactgtl Plc Gas-to-liquid plant using parallel units
GB0915036D0 (en) * 2009-08-28 2009-09-30 Compactgtl Plc Catalytic reaction module
JP5581028B2 (ja) * 2009-09-16 2014-08-27 住友精密工業株式会社 触媒反応器
KR101031886B1 (ko) * 2009-10-07 2011-05-02 한국에너지기술연구원 Ft 슬러리 기포탑 반응기의 반응열 제거용 혼합형 냉각장치
GB0918738D0 (en) * 2009-10-26 2009-12-09 Compactgtl Plc Reactor with channels
KR101297597B1 (ko) * 2011-04-19 2013-08-19 한국화학연구원 합성가스로부터 탄화수소를 제조하기 위한 반응장치
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
WO2013117948A1 (en) 2012-02-06 2013-08-15 Helbio Societé Anonyme Hydrogen And Energy Production Systems Heat integrated reformer with catalytic combustion for hydrogen production
US11607657B2 (en) 2012-02-06 2023-03-21 Helbio S.A. Heat integrated reformer with catalytic combustion for hydrogen production
WO2013123239A1 (en) 2012-02-17 2013-08-22 Ceramatec, Inc. Advanced fischer tropsch system
US9162935B2 (en) 2012-02-21 2015-10-20 Ceramatec, Inc. Compact FT combined with micro-fibrous supported nano-catalyst
EP2817090A4 (en) 2012-02-21 2016-01-20 Ceramatec Inc COMPACT FISCHER TROPSCH SYSTEM WITH INTEGRATED PRIMARY AND SECONDARY BED TEMPERATURE CONTROL
JP2015517175A (ja) 2012-03-08 2015-06-18 ヘルビオ ソシエテ アノニム ハイドロジェン アンド エナジー プロダクション システムズ 燃料電池のための触媒を支持する置換可能な構造化支持部を含む触媒加熱式燃料処理装置
US9255746B2 (en) 2012-10-26 2016-02-09 Modine Manufacturing Company Reactor core for use in a chemical reactor, and method of making the same
GB201302301D0 (en) * 2013-02-08 2013-03-27 Process Systems Entpr Ltd Reactor and reaction method
US9676623B2 (en) 2013-03-14 2017-06-13 Velocys, Inc. Process and apparatus for conducting simultaneous endothermic and exothermic reactions
WO2015037597A1 (ja) * 2013-09-13 2015-03-19 株式会社Ihi リアクタ
CN110813197B (zh) * 2014-05-12 2022-02-18 尤尼威蒂恩技术有限责任公司 使用具有堆叠气流间隙的插入组件的系统和方法
KR102003429B1 (ko) * 2016-10-19 2019-07-24 주식회사 포스코건설 합성석유 제조장치 및 제조방법
US10543470B2 (en) 2017-04-28 2020-01-28 Intramicron, Inc. Reactors and methods for processes involving partial oxidation reactions
US10544371B2 (en) 2018-05-11 2020-01-28 Intramicron, Inc. Channel reactors
JP7271865B2 (ja) * 2018-05-17 2023-05-12 株式会社Ihi 反応装置
EP3599075A1 (de) * 2018-07-27 2020-01-29 Siemens Aktiengesellschaft Reaktor zur durchführung einer chemischen gleichgewichtsreaktion
CN112221439A (zh) * 2020-09-09 2021-01-15 中石化宁波工程有限公司 用于微通道反应器的分布板及具有其的微通道反应器
CN113345611B (zh) * 2021-05-11 2022-12-13 哈尔滨工程大学 一种板型燃料元件多矩形流道均匀释热模拟试验装置
CN116272686B (zh) * 2023-01-03 2024-09-27 东方电气集团东方锅炉股份有限公司 一种混合流列管式固定床反应器

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GB1116345A (en) * 1964-06-16 1968-06-06 Marston Excelsior Ltd Improvements in or relating to chemical catalytic reactors and like process vessels in which fluids are contacted with solid materials
ZA782775B (en) * 1977-06-27 1979-05-30 Minnesota Mining & Mfg Catalytic reactor for isothermal reactions
GB2223237B (en) * 1988-07-21 1992-09-16 Shell Int Research Shut-down process for a fischer-tropsch reactor, and said reactor
GB0116894D0 (en) * 2001-07-11 2001-09-05 Accentus Plc Catalytic reactor
GB0124999D0 (en) * 2001-10-18 2001-12-05 Accentus Plc Catalytic reactor
AU2002349143A1 (en) 2001-12-05 2003-06-17 GTL Mircosystems AG Process an apparatus for steam-methane reforming
RU2310677C2 (ru) * 2002-12-02 2007-11-20 КОМПАКТДЖТЛ ПиЭлСи Каталитический реактор и способ
GB0413400D0 (en) * 2004-06-16 2004-07-21 Accentus Plc Catalytic plant and process
GB0501731D0 (en) 2005-01-31 2005-03-02 Accentus Plc Catalytic reactor
GB0504622D0 (en) 2005-03-05 2005-04-13 Accentus Plc Catalytic reactors
BRPI0711443A2 (pt) * 2006-05-08 2011-11-01 Compactgtl Plc reator catalìtico compacto, métodos de realizar combustão, e de realizar uma reação rápida no mesmo, e, de controlar o gradiente térmico em um reator catalìtico

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