KR100802373B1 - 마이크로채널 촉매 반응기 중 액체 연료의 탈수소화법 - Google Patents
마이크로채널 촉매 반응기 중 액체 연료의 탈수소화법 Download PDFInfo
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- KR100802373B1 KR100802373B1 KR1020060000540A KR20060000540A KR100802373B1 KR 100802373 B1 KR100802373 B1 KR 100802373B1 KR 1020060000540 A KR1020060000540 A KR 1020060000540A KR 20060000540 A KR20060000540 A KR 20060000540A KR 100802373 B1 KR100802373 B1 KR 100802373B1
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- H01M8/00—Fuel cells; Manufacture thereof
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- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/065—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloys; by dehydriding metallic substances
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- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/0005—Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes
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- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
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- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
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- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00819—Materials of construction
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- B01J2219/00851—Additional features
- B01J2219/00858—Aspects relating to the size of the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- 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
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00851—Additional features
- B01J2219/00867—Microreactors placed in series, on the same or on different supports
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- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00873—Heat exchange
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00891—Feeding or evacuation
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- 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
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00905—Separation
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- 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
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00993—Design aspects
- B01J2219/00997—Strategical arrangements of multiple microreactor systems
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- 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
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- 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
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Abstract
Description
Claims (15)
- 액체 유기 화합물이 초기에는 수소화된 형태이고, 이후 촉매적으로 탈수소화되어 탈수소화된 유기 화합물을 포함하는 액체 부산물과 수소 가스를 생성하는 가역적 수소화/탈수소화가 가능한 액체 유기 화합물로부터 수소를 발생하는 방법으로서,(a) 상기 가역적 수소화/탈수소화가 가능한 액체 유기 화합물을 1종 이상의 탈수소화 촉매가 포함된 마이크로채널 반응기에 도입시키는 단계;(b) 상기 유기 화합물과 탈수소화된 유기 화합물을 포함하는 액체 부산물 양쪽 모두가 액체 상태로 유지되는 액체 상태 조건하에 상기 유기 화합물을 탈수소화시키는 단계;(c) 탈수소화된 유기 화합물을 포함하는 액체 부산물과 가스 상태의 수소를 포함하는 반응 산물을 회수하는 단계;(d) 반응 산물을 탈수소화된 유기 화합물을 포함하는 액체 부산물과 가스 상태의 수소로 분리하는 단계;(e) 가스 상태의 수소를 회수하는 단계; 및(f) 탈수소화된 유기 화합물을 포함하는 액체 부산물을 회수하는 단계를 포함하는 것인 액체 유기 화합물로부터 수소를 발생하는 방법.
- 제1항에 있어서, 단계 (b)의 탈수소화를 0.2 기압 내지 100 기압의 압력에서 수행하는 것인 방법.
- 제2항에 있어서, 탈수소화 온도가 60℃ 내지 300℃인 것인 방법.
- 제1항에 있어서, 탈수소화를 다수의 마이크로채널 반응기 중에서 수행하고, 이때 각각의 연속되는 반응기 내 압력이 이전 반응기 압력보다 낮은 것인 방법.
- 제1항에 있어서, 유기 화합물의 증기압이 220℃에서 10 mm 수은 미만인 것인 방법.
- 제2항에 있어서, 유기 화합물이 탈수소화시 파이-컨주게이트된 기재를 형성하는 것인 방법.
- 제4항에 있어서, 각각의 마이크로채널 반응기에서 생산된 수소의 부피가 동일한 것인 방법.
- 제2항에 있어서, 액체 유기 화합물이 신장된(extended) 다환식 방향족 탄화수소, 질소 헤테로원자를 가지는 신장된 파이-컨주게이트된 기재, 질소가 아닌 다른 헤테로원자를 가지는 신장된 파이-컨주게이트된 기재, 파이-컨주게이트된 유기 중합체 및 올리고머, 이온성 파이-컨주게이트된 기재, 다수의 질소 헤테로원자를 가지는 파이-컨주게이트된 단환식 기재, 1 이상의 삼중결합기를 가지는 파이-컨주게이트된 기재 및 피치(pitch)의 수소화된 형태로 구성되는 군으로부터 선택되는 1종 이상을 포함하는 것인 방법.
- 제2항에 있어서, 수소화된 형태의 액체 유기 화합물이 피렌, 페릴렌, 코로넨, 오발렌, 피센 및 루비센, 플루오렌, 인덴 및 아세나나프틸렌 및 피란트론으로 구성된 군으로부터 선택된 1종 이상을 포함하는 것인 방법.
- 제2항에 있어서, 유기 화합물이 N-메틸카르바졸, N-에틸카르바졸, N-n-프로필카르바졸 및 N-이소-프로필카르바졸 및 이들의 혼합물로 구성된 군으로부터 선택되는 1종 이상을 포함하는 것인 방법.
- 제1항에 있어서, 탈수소화를 다수의 마이크로채널 반응기 중에서 수행하고, 이때 각각의 연속되는 반응기 내 온도가 이전 반응기 온도보다 높은 것인 방법.
- 제1항에 있어서, 채널이 열전달 유체를 운송하는데 사용하기 위해 반응기 채널 중에 제공되는 것인 방법.
- 제1항에 있어서, 상기 액체 유기화합물 도입 단계는 액체 가압단계를 포함하는 것인 방법.
- 제1항에 있어서, 상기 마이크로채널 반응기의 길이는 액체 흐름에 평행인 것인 방법.
- 제1항에 있어서, 열은 반응기를 통해 열교환유체를 순환시킴으로써 마이크로채널 반응기에 공급되는 것인 방법.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/029,059 US7485161B2 (en) | 2005-01-04 | 2005-01-04 | Dehydrogenation of liquid fuel in microchannel catalytic reactor |
US11/029,059 | 2005-01-04 |
Publications (2)
Publication Number | Publication Date |
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KR20060080128A KR20060080128A (ko) | 2006-07-07 |
KR100802373B1 true KR100802373B1 (ko) | 2008-02-13 |
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Application Number | Title | Priority Date | Filing Date |
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KR1020060000540A KR100802373B1 (ko) | 2005-01-04 | 2006-01-03 | 마이크로채널 촉매 반응기 중 액체 연료의 탈수소화법 |
Country Status (9)
Country | Link |
---|---|
US (2) | US7485161B2 (ko) |
JP (1) | JP4638357B2 (ko) |
KR (1) | KR100802373B1 (ko) |
CN (1) | CN1810630A (ko) |
BR (1) | BRPI0505651A (ko) |
CA (1) | CA2531733C (ko) |
MX (1) | MXPA05013936A (ko) |
MY (1) | MY140985A (ko) |
TW (1) | TWI303244B (ko) |
Families Citing this family (48)
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JP5737853B2 (ja) * | 2010-03-29 | 2015-06-17 | 千代田化工建設株式会社 | 貯蔵・輸送用水素の製造方法 |
CN101823692B (zh) * | 2010-04-20 | 2012-03-14 | 浙江大学 | 以哌啶为介质的可逆吸放氢方法及装置 |
EP2620410B1 (en) | 2010-07-26 | 2018-03-21 | Council of Scientific & Industrial Research | An improved process for the storage delivery of hydrogen by dehydrogenation using catalyst |
US9180424B2 (en) | 2010-09-11 | 2015-11-10 | Albert Chin-Tang Wey | Infrared assisted hydrogen generation |
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DE102011115950A1 (de) * | 2011-10-09 | 2013-04-11 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Energiequelle zum Betrieb von Unterwasserschiffen |
US9289741B2 (en) * | 2012-02-01 | 2016-03-22 | Battelle Memorial Institute | Suspended-slurry reactor |
DE102012216669A1 (de) * | 2012-09-18 | 2014-03-20 | H2-Industries AG | Anordnung und Verfahren zur Energieversorgung von Schiffen |
KR102232690B1 (ko) | 2013-01-30 | 2021-03-29 | 삼성디스플레이 주식회사 | 신규 헤테로고리 화합물 및 이를 포함한 유기 발광 소자 |
WO2015005280A1 (ja) * | 2013-07-09 | 2015-01-15 | 学校法人早稲田大学 | 水素担体および水素発生方法 |
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KR102044866B1 (ko) | 2013-08-21 | 2019-11-15 | 삼성디스플레이 주식회사 | 헤테로고리 화합물 및 이를 포함한 유기 발광 소자 |
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KR102191996B1 (ko) | 2013-09-27 | 2020-12-17 | 삼성디스플레이 주식회사 | 헤테로고리 화합물 및 이를 포함한 유기 발광 소자 |
KR102191994B1 (ko) | 2013-10-02 | 2020-12-17 | 삼성디스플레이 주식회사 | 화합물 및 이를 포함한 유기 발광 소자 |
GB2534803A (en) * | 2013-10-21 | 2016-08-03 | Air Prod & Chem | Multi-zone dehydrogenation reactor and ballasting system for storage and delivery of hydrogen |
KR101706742B1 (ko) | 2013-12-09 | 2017-02-15 | 삼성디스플레이 주식회사 | 화합물 및 이를 포함한 유기 발광 소자 |
KR102177212B1 (ko) | 2013-12-11 | 2020-11-11 | 삼성디스플레이 주식회사 | 화합물 및 이를 포함한 유기 발광 소자 |
DE102014006430A1 (de) | 2014-05-02 | 2015-11-05 | Hydrogenious Technologies Gmbh | Verfahren zur Energieversorgung insbesondere netzferner oder mobiler Verbraucher, Vorrichtung zum Durchführen eines solchen Verfahrens und darin verwendbares Stoffgemisch |
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US20060143981A1 (en) | 2006-07-06 |
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KR20060080128A (ko) | 2006-07-07 |
CA2531733A1 (en) | 2006-07-04 |
MXPA05013936A (es) | 2006-07-03 |
CN1810630A (zh) | 2006-08-02 |
JP2006188425A (ja) | 2006-07-20 |
US7485161B2 (en) | 2009-02-03 |
MY140985A (en) | 2010-02-12 |
TWI303244B (en) | 2008-11-21 |
JP4638357B2 (ja) | 2011-02-23 |
BRPI0505651A (pt) | 2006-09-19 |
TW200624416A (en) | 2006-07-16 |
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