KR960034070A - Methanol Reformer for High Purity Hydrogen Production - Google Patents
Methanol Reformer for High Purity Hydrogen Production Download PDFInfo
- Publication number
- KR960034070A KR960034070A KR1019950006785A KR19950006785A KR960034070A KR 960034070 A KR960034070 A KR 960034070A KR 1019950006785 A KR1019950006785 A KR 1019950006785A KR 19950006785 A KR19950006785 A KR 19950006785A KR 960034070 A KR960034070 A KR 960034070A
- Authority
- KR
- South Korea
- Prior art keywords
- reforming
- pipe
- combustion catalyst
- combustion
- supply pipe
- Prior art date
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Classifications
-
- 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
- C01B3/323—Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents
- C01B3/326—Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents characterised by the catalyst
-
- 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
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam 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
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1005—Arrangement or shape of catalyst
- C01B2203/1023—Catalysts in the form of a monolith or honeycomb
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
본 발명은 메탄올을 물과 혼합하여 개질촉매상에서 수소 및 일산화탄소, 이산화탄소 등을 생산한 뒤, PSA(presure swing adsorptin) 장치를 통하여 고순도를 분리, 생산하기 위한 메탄올 개질장치에 관한 것으로서 더욱 상세하게는 메탄올 개질장치 내부에 다수의 연소촉매층 및 연소실내의 온도를 가능한 낮게 유지하고, 개질촉매층의 최적의 노도분포를 구현하여 열효율을 향상시키고, 또한 연소촉매층 사이에 원료기화코일을 구비하여 개질장치의 단순화 및 소형화를 이룰 수 있도록 한 개질장치에 관한 것으로서, 개질장치(1) 내부에 이중관형태의 단관식 개질관(9)이 설치되고 개질관의 내부에는 개질촉매(10)가 충진되어 있는 개질장치에 있어서 개질관(9)의 내측 공간에 다수의 연소촉매층(2)이 일정한 간격을 두고 설치되어 있고 연소촉매층(2) 중심부에 다공성 연료공급관(3)이 관통되어 설치되어 있으며, 연소촉매층(2) 사이에 원료기화코일(4)이 연료공급관(3)의 주위로 설치되어 있는 구성으로 된 것이다.The present invention relates to a methanol reformer for separating and producing high purity through a PSA (presure swing adsorptin) apparatus after producing methanol, water, hydrogen and carbon monoxide, carbon dioxide, etc. in a reforming catalyst. Keeping the temperature of the plurality of combustion catalyst layers and the combustion chamber as low as possible in the reforming apparatus, and realizing the optimum distribution of the reforming catalyst layer, improving the thermal efficiency, and also providing the raw material vaporization coil between the combustion catalyst layers to simplify the reforming apparatus and In the reforming apparatus to achieve a miniaturization, the reforming apparatus in which the reformer 1 is provided with a single-pipe reformed tube 9 in the form of a double pipe, and the reforming catalyst 10 is filled in the reformed tube. A plurality of combustion catalyst layers 2 are provided at regular intervals in the inner space of the reforming pipe 9 and are located at the center of the combustion catalyst layer 2. St. fuel supply pipe, and (3) are installed with a through, but a configuration in which a raw material vaporizing coil 4 between the combustion catalyst layer (2) is provided around the fuel supply pipe (3).
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.
제2도는 본 발명에 의한 메탄올 개질장치의 정단면도, 제3도는 본 발명에 의한 메탄올 개질장치를 이용한 고순도 수소 제조.2 is a front sectional view of a methanol reformer according to the present invention, and FIG. 3 is a high purity hydrogen production using the methanol reformer according to the present invention.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019950006785A KR100314829B1 (en) | 1995-03-28 | 1995-03-28 | Methanol reforming apparatus for fabricating highly purified hydrogen |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019950006785A KR100314829B1 (en) | 1995-03-28 | 1995-03-28 | Methanol reforming apparatus for fabricating highly purified hydrogen |
Publications (2)
Publication Number | Publication Date |
---|---|
KR960034070A true KR960034070A (en) | 1996-10-22 |
KR100314829B1 KR100314829B1 (en) | 2002-06-26 |
Family
ID=37531494
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019950006785A KR100314829B1 (en) | 1995-03-28 | 1995-03-28 | Methanol reforming apparatus for fabricating highly purified hydrogen |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR100314829B1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100648730B1 (en) * | 2005-04-22 | 2006-11-23 | 삼성에스디아이 주식회사 | Reformer for fuel cell system |
KR100667953B1 (en) * | 2005-07-29 | 2007-01-11 | 삼성에스디아이 주식회사 | Reformer and fuel cell system with the same |
US8017088B2 (en) | 2005-09-27 | 2011-09-13 | Samsung Sdi Co., Ltd. | Fuel reformer |
CN110429308A (en) * | 2019-08-06 | 2019-11-08 | 强伟氢能科技有限公司 | A kind of hydrogen from methyl alcohol electricity generation system |
Families Citing this family (10)
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---|---|---|---|---|
KR100805582B1 (en) | 2006-08-16 | 2008-02-20 | 삼성에스디아이 주식회사 | Heater for the fuel cell system |
KR101830954B1 (en) * | 2016-06-08 | 2018-04-04 | 한국에너지기술연구원 | Hydrogen production system including unit for removal of carbon monoxide |
KR101817569B1 (en) | 2015-06-26 | 2018-01-11 | 한국에너지기술연구원 | A heat-exchange reactor producing hydrogen from carbon compound |
KR101841188B1 (en) * | 2016-07-19 | 2018-03-23 | (주)신넥앤테크 | Fuel Processor for PEMFC with excellent reaction efficiency |
KR101866500B1 (en) | 2016-11-14 | 2018-07-04 | 한국에너지기술연구원 | Hydrogen production rector including carbon monoxide removing unit |
KR102005715B1 (en) | 2017-11-22 | 2019-08-01 | 한국에너지기술연구원 | Hydrogen production reactor including feed preheating part |
KR20190059638A (en) | 2017-11-23 | 2019-05-31 | 한국에너지기술연구원 | Catalytic combustor of a liquid fuel containing high water content |
KR102241298B1 (en) * | 2019-05-07 | 2021-04-16 | 주식회사 동양아이에프 | Reforming reaction apparatus with high-frequency induction heating for hydrogen production |
KR102576442B1 (en) * | 2021-03-26 | 2023-09-07 | 금오공과대학교 산학협력단 | Electrochemical splitting device for producting hydrogen based on ethylene glycol and terephthalic acid, hydrogen production method and hydrogen production apparatus through electrochemical splitting using the same |
KR102576440B1 (en) * | 2021-03-26 | 2023-09-07 | 금오공과대학교 산학협력단 | Electrochemical splitting device for producting hydrogen based on methanol, hydrogen production method and hydrogen production apparatus through electrochemical splitting pure methanol using the same |
-
1995
- 1995-03-28 KR KR1019950006785A patent/KR100314829B1/en not_active IP Right Cessation
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100648730B1 (en) * | 2005-04-22 | 2006-11-23 | 삼성에스디아이 주식회사 | Reformer for fuel cell system |
US7842109B2 (en) | 2005-04-22 | 2010-11-30 | Samsung Sdi Co., Ltd. | Reformer for fuel cell system having increased heat transfer efficiency |
KR100667953B1 (en) * | 2005-07-29 | 2007-01-11 | 삼성에스디아이 주식회사 | Reformer and fuel cell system with the same |
US7682587B2 (en) | 2005-07-29 | 2010-03-23 | Samsung Sdi Co., Ltd. | Fuel cell reformer |
US8017088B2 (en) | 2005-09-27 | 2011-09-13 | Samsung Sdi Co., Ltd. | Fuel reformer |
CN110429308A (en) * | 2019-08-06 | 2019-11-08 | 强伟氢能科技有限公司 | A kind of hydrogen from methyl alcohol electricity generation system |
Also Published As
Publication number | Publication date |
---|---|
KR100314829B1 (en) | 2002-06-26 |
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