JP4505184B2 - 小型燃料気体改質器組立物 - Google Patents
小型燃料気体改質器組立物 Download PDFInfo
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- JP4505184B2 JP4505184B2 JP2002559163A JP2002559163A JP4505184B2 JP 4505184 B2 JP4505184 B2 JP 4505184B2 JP 2002559163 A JP2002559163 A JP 2002559163A JP 2002559163 A JP2002559163 A JP 2002559163A JP 4505184 B2 JP4505184 B2 JP 4505184B2
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- gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
- F28D7/12—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- 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
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
-
- 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
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00157—Controlling the temperature by means of a burner
-
- 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
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00186—Controlling or regulating processes controlling the composition of the reactive mixture
-
- 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
- B01J2219/2451—Geometry of the reactor
- B01J2219/2453—Plates arranged in parallel
-
- 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
- B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
-
- 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
- B01J2219/2479—Catalysts coated on the surface of plates or inserts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
- C01B2203/82—Several process steps of C01B2203/02 - C01B2203/08 integrated into a single apparatus
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Description
Claims (9)
- (a) 燃料気体と水蒸気の混合物を受け取るための複数の燃料気体通路と、
(b) 燃焼器気体流れを受け取るための複数の燃焼器気体通路であって、前記燃焼器気体通路と前記燃料気体通路が、互いに熱交換関係に配置され、それによって、前記燃焼器通路からの熱が、前記燃料気体通路へ移動する、複数の燃焼器気体通路と、
(c) 前記燃焼器気体通路の第1の部分と、前記燃焼器気体通路の第2の部分と、
を備える炭化水素燃料気体流れ改質器組立体であって、前記燃焼器気体通路の前記第1の部分は、隣接する燃料気体通路と並流気体流れ方向に配置され、前記燃焼器気体通路の前記第2の部分は、隣接する燃料気体通路と向流気体流れ方向に配置され、それによって、前記燃焼器気体通路の前記第1の部分の中の燃焼器気体は、隣接する燃料気体通路内の燃料気体と同じ方向に流れ、前記燃焼器気体通路の前記第2の部分の中の燃焼器気体は、隣接する燃料気体通路内の燃料気体と反対の方向に流れることを特徴とする炭化水素燃料気体流れ改質器組立体。 - 前記燃焼器気体通路の前記第1の部分は、前記組立体内の複数の燃焼器気体通路の少なくとも50パーセントから成ることを特徴とする請求項1記載の燃料気体流れ改質器組立体。
- 前記燃焼器気体通路の前記第1の部分は、前記組立体内の複数の燃焼器気体通路の少なくとも66パーセントから成ることを特徴とする請求項2記載の燃料気体流れ改質器組立体。
- 前記燃焼器気体通路の前記第1の部分は、前記組立体内の複数の燃焼器気体通路の少なくとも70パーセントから成ることを特徴とする請求項2記載の燃料気体流れ改質器組立体。
- 前記燃焼器気体通路の前記第1の部分は、前記組立体内の複数の燃焼器気体通路の50パーセントから70パーセントの範囲にあることを特徴とする請求項1記載の燃料気体流れ改質器組立体。
- 前記組立体は、燃焼器気体通路と燃料気体通路とを含む一続きのモジュールから作製され、このモジュールのそれぞれは、そのそれぞれの中の燃焼器気体通路の全体の数の少なくとも66パーセントの濃度で前記燃焼器気体通路の前記第1の部分を含むことを特徴とする請求項1記載の燃料気体流れ改質器組立体。
- (a) 燃料気体と水蒸気の混合物を受け取るための複数の燃料気体通路と、
(b) 燃焼器気体流れを受け取るための複数の燃焼器気体通路であって、前記燃焼器気体通路と前記燃料気体通路が、互いに熱交換関係に配置され、それによって、前記燃焼器通路からの熱が、前記燃料気体通路へ移動する、複数の燃焼器気体通路と、
c) 前記燃焼器気体通路の第1の部分と、前記燃焼器気体通路の第2の部分と、
を備える炭化水素燃料気体流れ改質器組立体モジュールであって、前記燃焼器気体通路の前記第1の部分は、隣接する燃料気体通路と並流気体流れ方向に配置され、前記燃焼器気体通路の前記第2の部分は、隣接する燃料気体通路と向流気体流れ方向に配置され、それによって、前記燃焼器気体通路の前記第1の部分の中の燃焼器気体は、隣接する燃料気体通路内の燃料気体と同じ方向に流れ、前記燃焼器気体通路の前記第2の部分の中の燃焼器気体は、隣接する燃料気体通路内の燃料気体と反対の方向に流れることを特徴とする炭化水素燃料気体流れ改質器組立体モジュール。 - 前記燃焼器気体通路の前記第1の部分は、前記組立体内の複数の燃焼器気体通路の少なくとも50パーセントから成ることを特徴とする請求項7記載の気体流れ改質器組立体モジュール。
- 前記燃焼器気体通路の前記第1の部分は、前記組立体内の複数の燃焼器気体通路の少なくとも66パーセントから成ることを特徴とする請求項8記載の気体流れ改質器組立体モジュール。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US26408901P | 2001-01-26 | 2001-01-26 | |
US09/814,911 US6773684B2 (en) | 2001-01-26 | 2001-03-23 | Compact fuel gas reformer assemblage |
PCT/US2002/001776 WO2002058837A1 (en) | 2001-01-26 | 2002-01-22 | Compact fuel gas reformer assemblage |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2004527437A JP2004527437A (ja) | 2004-09-09 |
JP4505184B2 true JP4505184B2 (ja) | 2010-07-21 |
Family
ID=26950241
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2002559163A Expired - Fee Related JP4505184B2 (ja) | 2001-01-26 | 2002-01-22 | 小型燃料気体改質器組立物 |
Country Status (4)
Country | Link |
---|---|
US (1) | US6773684B2 (ja) |
EP (1) | EP1365857A4 (ja) |
JP (1) | JP4505184B2 (ja) |
WO (1) | WO2002058837A1 (ja) |
Families Citing this family (35)
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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 |
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 |
US7294734B2 (en) * | 2003-05-02 | 2007-11-13 | Velocys, Inc. | Process for converting a hydrocarbon to an oxygenate or a nitrile |
CA2526965C (en) * | 2003-05-16 | 2011-10-11 | Velocys Inc. | Process for forming an emulsion using microchannel process technology |
US8580211B2 (en) * | 2003-05-16 | 2013-11-12 | Velocys, Inc. | Microchannel with internal fin support for catalyst or sorption medium |
US7485671B2 (en) * | 2003-05-16 | 2009-02-03 | Velocys, Inc. | Process for forming an emulsion using microchannel process technology |
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 |
US9023900B2 (en) | 2004-01-28 | 2015-05-05 | Velocys, Inc. | Fischer-Tropsch synthesis using microchannel technology and novel catalyst and microchannel reactor |
US7084180B2 (en) * | 2004-01-28 | 2006-08-01 | 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 |
DE102004007344A1 (de) * | 2004-02-14 | 2005-09-01 | Robert Bosch Gmbh | Integrierter Reaktor zur thermischen Kopplung von Reaktionen und Verfahren zur Steuerung des Temperaturfeldes in einem solchen Reaktor |
KR100599712B1 (ko) * | 2004-06-24 | 2006-07-12 | 삼성에스디아이 주식회사 | 연료 전지 시스템 및 개질기 |
EP1781389A2 (en) * | 2004-07-23 | 2007-05-09 | Velocys, Inc. | Distillation process using microchannel technology |
US7305850B2 (en) * | 2004-07-23 | 2007-12-11 | Velocys, Inc. | Distillation process using microchannel technology |
WO2006020709A1 (en) * | 2004-08-12 | 2006-02-23 | Velocys Inc. | Process for converting ethylene to ethylene oxide using microchannel process technology |
JP5643474B2 (ja) * | 2004-10-01 | 2014-12-17 | ヴェロシス,インク. | マイクロチャネルプロセス技術を用いる多相混合プロセス |
CA2586971C (en) * | 2004-11-12 | 2013-07-23 | Velocys Inc. | Process using microchannel technology for conducting alkylation or acylation reaction |
WO2006055609A1 (en) | 2004-11-16 | 2006-05-26 | Velocys Inc. | Multiphase reaction process using microchannel technology |
CA2587412C (en) * | 2004-11-17 | 2013-03-26 | Velocys Inc. | Emulsion process using microchannel process technology |
US7507274B2 (en) * | 2005-03-02 | 2009-03-24 | Velocys, Inc. | Separation process using microchannel technology |
WO2006127889A2 (en) * | 2005-05-25 | 2006-11-30 | Velocys Inc. | Support for use in microchannel processing |
US20070004810A1 (en) * | 2005-06-30 | 2007-01-04 | Yong Wang | Novel catalyst and fischer-tropsch synthesis process using same |
WO2007008495A2 (en) * | 2005-07-08 | 2007-01-18 | Velocys Inc. | Catalytic reaction process using microchannel technology |
US8038959B2 (en) | 2005-09-08 | 2011-10-18 | Casio Computer Co., Ltd. | Reacting device |
TWI338967B (en) * | 2006-01-17 | 2011-03-11 | Casio Computer Co Ltd | Reactor device |
JP2010210118A (ja) * | 2009-03-09 | 2010-09-24 | Jamco Corp | 漏水防止用安全弁を備えた旅客機搭載用スチームオーブン |
US8263006B2 (en) * | 2009-05-31 | 2012-09-11 | Corning Incorporated | Reactor with upper and lower manifold structures |
US8690977B2 (en) * | 2009-06-25 | 2014-04-08 | Sustainable Waste Power Systems, Inc. | Garbage in power out (GIPO) thermal conversion process |
KR101973576B1 (ko) | 2010-03-02 | 2019-04-29 | 벨로시스, 인코포레이티드 | 용접, 라미네이트식 장치 및 이의 제조 방법과, 상기 장치의 사용 방법 |
GB201214122D0 (en) | 2012-08-07 | 2012-09-19 | Oxford Catalysts Ltd | Treating of catalyst support |
EP2979752A1 (en) * | 2014-07-29 | 2016-02-03 | Nederlandse Organisatie voor toegepast- natuurwetenschappelijk onderzoek TNO | A catalyzing reactor, a method for producing a catalyzing reactor and a use of catalyzing reactor |
GB2554618B (en) | 2015-06-12 | 2021-11-10 | Velocys Inc | Synthesis gas conversion process |
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US6117578A (en) * | 1998-04-16 | 2000-09-12 | International Fuel Cells, Llc | Catalyzed wall fuel gas reformer |
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US6159358A (en) * | 1998-09-08 | 2000-12-12 | Uop Llc | Process and apparatus using plate arrangement for reactant heating and preheating |
DE19948221C1 (de) * | 1999-10-06 | 2001-05-03 | Xcellsis Gmbh | Dampfreformierungsanlage |
-
2001
- 2001-03-23 US US09/814,911 patent/US6773684B2/en not_active Expired - Fee Related
-
2002
- 2002-01-22 EP EP02720832A patent/EP1365857A4/en not_active Withdrawn
- 2002-01-22 WO PCT/US2002/001776 patent/WO2002058837A1/en active Application Filing
- 2002-01-22 JP JP2002559163A patent/JP4505184B2/ja not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP1365857A4 (en) | 2006-06-07 |
US6773684B2 (en) | 2004-08-10 |
WO2002058837A1 (en) | 2002-08-01 |
JP2004527437A (ja) | 2004-09-09 |
EP1365857A1 (en) | 2003-12-03 |
US20020102195A1 (en) | 2002-08-01 |
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