TW200633926A - Apparatus and method for hydrogen generation - Google Patents
Apparatus and method for hydrogen generationInfo
- Publication number
- TW200633926A TW200633926A TW095102682A TW95102682A TW200633926A TW 200633926 A TW200633926 A TW 200633926A TW 095102682 A TW095102682 A TW 095102682A TW 95102682 A TW95102682 A TW 95102682A TW 200633926 A TW200633926 A TW 200633926A
- Authority
- TW
- Taiwan
- Prior art keywords
- reformer
- gas
- reformed
- hydrocarbon gas
- reforming
- Prior art date
Links
Classifications
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- 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
- C01B3/382—Multi-step processes
-
- 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
-
- 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
- C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
- C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
- C01B3/26—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using catalysts
-
- 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
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0244—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being an autothermal reforming step, e.g. secondary reforming processes
-
- 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
- C01B2203/0838—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel
- C01B2203/0844—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel the non-combustive exothermic reaction being another reforming reaction as defined in groups C01B2203/02 - C01B2203/0294
-
- 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
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1288—Evaporation of one or more of the different feed components
- C01B2203/1294—Evaporation by heat exchange with hot process stream
-
- 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
- C01B2203/14—Details of the flowsheet
- C01B2203/142—At least two reforming, decomposition or partial oxidation steps in series
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Abstract
This present invention provides a hydrogen generator with excellent energy efficiency and can reduce equipment cost. In the hydrogen generator, a hydrocarbon gas is reformed to produce a reformed hydrogen-rich gas. The hydrogen generator comprises a reformer 1 for catalytically reacting the hydrocarbon gas together with oxygen with a catalyst to perform combustion and reforming of the hydrocarbon gas and a first heat exchanger 3 for heating the hydrocarbon gas to be introduced into the reformer 1 after heat exchange between the reformed gas and the hydrocarbon gas in a reformed gas passage 25 provided on the downstream side of the reformer 1. According to the above construction, the raw material gas to be introduced into the reformer 1 is heated by the heat of the reformed gas produced by the combustion and reforming, without the need to externally supply heat energy necessary for reforming by a burner of the like. Accordingly, the energy efficiency is improved. Furthermore, since the need to provide any burner in the reformer 1 is eliminated, the structure of the reformer 1 per se can be simplified, and at the same time, the structure for imparting heat resistance and pressure resistance can also be simplified. This advantage leads to a reduction in equipment cost.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005020910A JP5165832B2 (en) | 2005-01-28 | 2005-01-28 | Hydrogen generating apparatus and method |
Publications (2)
Publication Number | Publication Date |
---|---|
TW200633926A true TW200633926A (en) | 2006-10-01 |
TWI394710B TWI394710B (en) | 2013-05-01 |
Family
ID=36740558
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW095102682A TWI394710B (en) | 2005-01-28 | 2006-01-24 | Apparatus and method for producing hydrogen |
Country Status (5)
Country | Link |
---|---|
JP (1) | JP5165832B2 (en) |
KR (1) | KR101241848B1 (en) |
CN (1) | CN101111452B (en) |
TW (1) | TWI394710B (en) |
WO (1) | WO2006080544A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI617508B (en) * | 2016-11-21 | 2018-03-11 | Huang Heng Xin | Biogas catalyst cogeneration unit and operation method thereof |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5400425B2 (en) * | 2009-03-03 | 2014-01-29 | Jx日鉱日石エネルギー株式会社 | Hydrogen production apparatus and fuel cell system |
KR101394346B1 (en) * | 2012-02-29 | 2014-05-14 | 성균관대학교산학협력단 | Thermophotovoltaic apparatus having reformer for generating hydrogen |
KR101487835B1 (en) | 2014-03-13 | 2015-01-30 | 성균관대학교산학협력단 | Thermophotovoltaic apparatus having reformer for generating hydrogen |
CN104609369B (en) * | 2015-01-30 | 2015-11-18 | 山东益丰生化环保股份有限公司 | A kind ofly petroleum refinery is resolved the method that exhaust gas conversion becomes process for making hydrogen unstripped gas |
CN104609368B (en) * | 2015-01-30 | 2016-06-22 | 山东益丰生化环保股份有限公司 | A kind of petroleum refinery is resolved the method that exhaust gas conversion becomes process for making hydrogen unstripped gas |
CN106556668B (en) * | 2015-09-30 | 2020-07-10 | 中国石油化工股份有限公司 | Movable hydrocarbon steam conversion hydrogen production catalyst test platform and test method |
JP6944349B2 (en) * | 2017-11-09 | 2021-10-06 | エア・ウォーター株式会社 | Hydrogen generator |
KR102094646B1 (en) | 2019-10-14 | 2020-03-30 | 주식회사 트리신 | Highly efficient steam reforming hydrogen production apparatus with hydrodesulfurization |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4909808A (en) * | 1987-10-14 | 1990-03-20 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Steam reformer with catalytic combustor |
JPH05253436A (en) * | 1992-03-16 | 1993-10-05 | Mitsui Eng & Shipbuild Co Ltd | Production of co gas free from ch4 |
JP2001151502A (en) * | 1999-11-26 | 2001-06-05 | Daikin Ind Ltd | Fuel reforming device |
US6485853B1 (en) * | 2000-06-27 | 2002-11-26 | General Motors Corporation | Fuel cell system having thermally integrated, isothermal co-cleansing subsystem |
JP2002050386A (en) * | 2000-08-04 | 2002-02-15 | Babcock Hitachi Kk | Hydrogen producing device for fuel cell |
JP4968984B2 (en) * | 2001-01-12 | 2012-07-04 | 三洋電機株式会社 | Fuel cell reformer |
JP2002274805A (en) * | 2001-01-12 | 2002-09-25 | Toyota Motor Corp | Control of reformer having heat exchanger employing reform material as refrigerant |
JP2002293510A (en) * | 2001-03-28 | 2002-10-09 | Osaka Gas Co Ltd | Carbon monoxide converter |
JP2003103171A (en) * | 2001-09-28 | 2003-04-08 | Nippon Oil Corp | Catalyst and method for auto thermal reforming, hydrogen producing device and fuel cell system |
JP2003212508A (en) * | 2002-01-24 | 2003-07-30 | Honda Motor Co Ltd | Method of controlling supply of water in reforming system |
US20030192251A1 (en) * | 2002-04-12 | 2003-10-16 | Edlund David J. | Steam reforming fuel processor |
JP4175921B2 (en) * | 2003-03-12 | 2008-11-05 | 東京瓦斯株式会社 | Heat recovery system in hydrogen production equipment |
-
2005
- 2005-01-28 JP JP2005020910A patent/JP5165832B2/en active Active
-
2006
- 2006-01-24 TW TW095102682A patent/TWI394710B/en active
- 2006-01-25 WO PCT/JP2006/301608 patent/WO2006080544A1/en not_active Application Discontinuation
- 2006-01-25 KR KR1020077018208A patent/KR101241848B1/en active IP Right Grant
- 2006-01-25 CN CN2006800035540A patent/CN101111452B/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI617508B (en) * | 2016-11-21 | 2018-03-11 | Huang Heng Xin | Biogas catalyst cogeneration unit and operation method thereof |
Also Published As
Publication number | Publication date |
---|---|
KR101241848B1 (en) | 2013-03-11 |
CN101111452B (en) | 2012-09-05 |
JP2006206382A (en) | 2006-08-10 |
TWI394710B (en) | 2013-05-01 |
JP5165832B2 (en) | 2013-03-21 |
CN101111452A (en) | 2008-01-23 |
WO2006080544A1 (en) | 2006-08-03 |
KR20070099644A (en) | 2007-10-09 |
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