EA200901371A1 - Установка риформинга с высокоэффективным теплообменом для получения водорода - Google Patents

Установка риформинга с высокоэффективным теплообменом для получения водорода

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Publication number
EA200901371A1
EA200901371A1 EA200901371A EA200901371A EA200901371A1 EA 200901371 A1 EA200901371 A1 EA 200901371A1 EA 200901371 A EA200901371 A EA 200901371A EA 200901371 A EA200901371 A EA 200901371A EA 200901371 A1 EA200901371 A1 EA 200901371A1
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EA
Eurasian Patent Office
Prior art keywords
reforming
wall
combustion
section
fuel
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EA200901371A
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English (en)
Inventor
Ксенофон Верикиос
Димитриос К. Лигурас
Original Assignee
Гельбио С.А. Хайдроджен Энд Энерджи Продакшн Системс
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Application filed by Гельбио С.А. Хайдроджен Энд Энерджи Продакшн Системс filed Critical Гельбио С.А. Хайдроджен Энд Энерджи Продакшн Системс
Publication of EA200901371A1 publication Critical patent/EA200901371A1/ru

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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
    • 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
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/007—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • B01J19/0053—Details of the reactor
    • B01J19/006—Baffles
    • 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
    • B01J19/2415—Tubular reactors
    • 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
    • B01J19/2415—Tubular reactors
    • B01J19/2425—Tubular reactors 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B01J4/002—Nozzle-type elements
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B01J4/005—Feed or outlet devices as such, e.g. feeding tubes provided with baffles
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • 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
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00081—Tubes
    • 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
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00117—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
    • 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
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • B01J2219/00777—Baffles attached to the reactor wall horizontal
    • 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
    • C01B2203/08—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
    • C01B2203/08—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
    • C01B2203/0822—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel the fuel containing hydrogen
    • 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
    • C01B2203/1035—Catalyst coated on equipment surfaces, e.g. reactor walls
    • 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
    • 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
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

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  • 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)

Abstract

Описан агрегат с высокоэффективным теплообменом, включающий установку парового риформинга и камеру сгорания, который можно применять в устройстве для переработки топлива для получения водорода из топливного сырья. Агрегат включает секцию риформинга и секцию горения, разделенные стенкой. На облицовку стенки секции риформинга нанесен катализатор, способный инициировать реакции риформинга. На облицовку стенки секции горения нанесен катализатор, способный инициировать реакции горения. В секцию риформинга подают смесь пара и топлива, где ее подвергают риформингу для получения водорода. В секцию горения подают смесь топлива и воздуха, где ее сжигают для подачи тепла в установку риформинга. На катализаторе горения, нанесенном на одну сторону стенки, происходит каталитическое горение, тогда как на катализаторе риформинга, нанесенном на другую сторону стенки, происходит каталитический риформинг. Теплопередача через стенку является очень легкой и эффективной. Для создания реакторов любого размера можно объединить множество таких агрегатов.
EA200901371A 2007-05-25 2008-04-22 Установка риформинга с высокоэффективным теплообменом для получения водорода EA200901371A1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GR20070100314A GR1006128B (el) 2007-05-25 2007-05-25 Υψηλα θερμικα ολοκληρωμενος αναμορφωτης για παραγωγη υδρογονου
PCT/GR2008/000029 WO2008146052A1 (en) 2007-05-25 2008-04-22 Highly heat integrated reformer for hydrogen production

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Publication Number Publication Date
EA200901371A1 true EA200901371A1 (ru) 2010-06-30

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Country Status (7)

Country Link
US (1) US20100178219A1 (ru)
EP (1) EP2170766A1 (ru)
BR (1) BRPI0810937B1 (ru)
CA (1) CA2685299A1 (ru)
EA (1) EA200901371A1 (ru)
GR (1) GR1006128B (ru)
WO (1) WO2008146052A1 (ru)

Families Citing this family (64)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009039276A1 (de) 2009-08-28 2011-03-10 Bekon Energy Technologies Gmbh & Co. Kg Reaktormodul für endotherme Reaktionen sowie Reaktor mit einer Mehrzahl von solchen Reaktormodulen
CA2785351A1 (en) * 2009-12-22 2011-06-30 Airscience Technologies System and process for the production of hydrogen from raw gas using a nanoparticle ceria based catalyst
US9227844B2 (en) * 2010-01-19 2016-01-05 Haldor Topsoe A/S Heat exchange reformer with double-tubes for reforming hydrocarbons
US11073280B2 (en) 2010-04-01 2021-07-27 Clearsign Technologies Corporation Electrodynamic control in a burner system
US9561476B2 (en) 2010-12-15 2017-02-07 Praxair Technology, Inc. Catalyst containing oxygen transport membrane
US9486735B2 (en) 2011-12-15 2016-11-08 Praxair Technology, Inc. Composite oxygen transport membrane
EP2791082B1 (en) 2011-12-15 2021-01-20 Praxair Technology, Inc. Method of producing composite oxygen transport membrane
US11607657B2 (en) 2012-02-06 2023-03-21 Helbio S.A. Heat integrated reformer with catalytic combustion for hydrogen production
CA2862527C (en) * 2012-02-06 2021-06-29 Helbio Societe Anonyme Hydrogen And Energy Production Systems Heat integrated reformer with catalytic combustion for hydrogen production
CA3137624C (en) 2012-03-08 2023-06-20 Helbio Societe Anonyme Hydrogen And Energy Production Systems Catalytically heated fuel processor with replaceable structured supports bearing catalyst for fuel cell
EP2671842A1 (en) * 2012-06-06 2013-12-11 Ammonia Casale S.A. A process for gas-heated reforming of a hydrocarbon source and a related plant
WO2014001438A1 (en) * 2012-06-29 2014-01-03 Haldor Topsøe A/S Purification of a raw gas by hydrogenation
US9969645B2 (en) 2012-12-19 2018-05-15 Praxair Technology, Inc. Method for sealing an oxygen transport membrane assembly
US9453644B2 (en) 2012-12-28 2016-09-27 Praxair Technology, Inc. Oxygen transport membrane based advanced power cycle with low pressure synthesis gas slip stream
US10119704B2 (en) 2013-02-14 2018-11-06 Clearsign Combustion Corporation Burner system including a non-planar perforated flame holder
US11460188B2 (en) 2013-02-14 2022-10-04 Clearsign Technologies Corporation Ultra low emissions firetube boiler burner
US10571124B2 (en) 2013-02-14 2020-02-25 Clearsign Combustion Corporation Selectable dilution low NOx burner
CN104884868B (zh) 2013-02-14 2018-02-06 克利尔赛恩燃烧公司 用于具有穿孔火焰稳定器的燃烧器的启动方法和机构
US10125983B2 (en) 2013-02-14 2018-11-13 Clearsign Combustion Corporation High output porous tile burner
US10458649B2 (en) 2013-02-14 2019-10-29 Clearsign Combustion Corporation Horizontally fired burner with a perforated flame holder
US10386062B2 (en) 2013-02-14 2019-08-20 Clearsign Combustion Corporation Method for operating a combustion system including a perforated flame holder
US10190767B2 (en) 2013-03-27 2019-01-29 Clearsign Combustion Corporation Electrically controlled combustion fluid flow
US9611144B2 (en) 2013-04-26 2017-04-04 Praxair Technology, Inc. Method and system for producing a synthesis gas in an oxygen transport membrane based reforming system that is free of metal dusting corrosion
US9296671B2 (en) 2013-04-26 2016-03-29 Praxair Technology, Inc. Method and system for producing methanol using an integrated oxygen transport membrane based reforming system
US9212113B2 (en) 2013-04-26 2015-12-15 Praxair Technology, Inc. Method and system for producing a synthesis gas using an oxygen transport membrane based reforming system with secondary reforming and auxiliary heat source
US9938145B2 (en) 2013-04-26 2018-04-10 Praxair Technology, Inc. Method and system for adjusting synthesis gas module in an oxygen transport membrane based reforming system
EP3049721A4 (en) 2013-09-23 2017-09-20 Clearsign Combustion Corporation Burner system employing multiple perforated flame holders, and method of operation
US11047572B2 (en) 2013-09-23 2021-06-29 Clearsign Technologies Corporation Porous flame holder for low NOx combustion
US9776153B2 (en) 2013-10-07 2017-10-03 Praxair Technology, Inc. Ceramic oxygen transport membrane array reactor and reforming method
WO2015054323A1 (en) 2013-10-07 2015-04-16 Clearsign Combustion Corporation Pre-mixed fuel burner with perforated flame holder
US9452388B2 (en) 2013-10-08 2016-09-27 Praxair Technology, Inc. System and method for air temperature control in an oxygen transport membrane based reactor
US20150104748A1 (en) 2013-10-14 2015-04-16 Clearsign Combustion Corporation Electrodynamic combustion control (ecc) technology for biomass and coal systems
WO2015061760A1 (en) * 2013-10-24 2015-04-30 Clearsign Combustion Corporation System and combustion reaction holder configured to transfer heat from a combustion reaction to a fluid
EP3066385A4 (en) 2013-11-08 2017-11-15 Clearsign Combustion Corporation Combustion system with flame location actuation
WO2015084729A1 (en) 2013-12-02 2015-06-11 Praxair Technology, Inc. Method and system for producing hydrogen using an oxygen transport membrane based reforming system with secondary reforming
CN105960565B (zh) 2014-01-24 2019-11-12 克利尔赛恩燃烧公司 低NOx火管锅炉
US9562472B2 (en) 2014-02-12 2017-02-07 Praxair Technology, Inc. Oxygen transport membrane reactor based method and system for generating electric power
WO2015123381A1 (en) 2014-02-14 2015-08-20 Clearsign Combustion Corporation Down-fired burner with a perforated flame holder
WO2015160609A1 (en) 2014-04-16 2015-10-22 Praxair Technology, Inc. Method and system for oxygen transport membrane enhanced integrated gasifier combined cycle (igcc)
US9791171B2 (en) 2014-07-28 2017-10-17 Clearsign Combustion Corporation Fluid heater with a variable-output burner including a perforated flame holder and method of operation
US9885496B2 (en) 2014-07-28 2018-02-06 Clearsign Combustion Corporation Fluid heater with perforated flame holder
US9828288B2 (en) 2014-08-13 2017-11-28 Clearsign Combustion Corporation Perforated burner for a rotary kiln
WO2016057164A1 (en) 2014-10-07 2016-04-14 Praxair Technology, Inc Composite oxygen ion transport membrane
US9702547B2 (en) 2014-10-15 2017-07-11 Clearsign Combustion Corporation Current gated electrode for applying an electric field to a flame
US10632437B2 (en) * 2014-10-22 2020-04-28 Korea Institute Of Energy Research Shell-and-tube type reactor for reforming natural gas and a preparation method of syngas or hydrogen gas by using the same
JP2016117621A (ja) * 2014-12-22 2016-06-30 株式会社Ｓｃｒｅｅｎホールディングス 触媒構造体の製造装置および製造方法
JP2016117028A (ja) * 2014-12-22 2016-06-30 国立大学法人徳島大学 触媒構造体および水素製造装置
WO2016134061A1 (en) 2015-02-17 2016-08-25 Clearsign Combustion Corporation Perforated flame holder with adjustable fuel nozzle
US10441922B2 (en) 2015-06-29 2019-10-15 Praxair Technology, Inc. Dual function composite oxygen transport membrane
US10118823B2 (en) 2015-12-15 2018-11-06 Praxair Technology, Inc. Method of thermally-stabilizing an oxygen transport membrane-based reforming system
US9938146B2 (en) 2015-12-28 2018-04-10 Praxair Technology, Inc. High aspect ratio catalytic reactor and catalyst inserts therefor
US10088153B2 (en) 2015-12-29 2018-10-02 Clearsign Combustion Corporation Radiant wall burner including perforated flame holders
EP3403026B1 (en) 2016-01-13 2021-12-15 ClearSign Technologies Corporation Combustion system comprising a first and a second perforated flame holder, separated by a gap
US11052353B2 (en) 2016-04-01 2021-07-06 Praxair Technology, Inc. Catalyst-containing oxygen transport membrane
EP3449183B1 (en) 2016-04-29 2023-12-06 ClearSign Technologies Corporation Burner system with discrete transverse flame stabilizers
WO2017208269A1 (en) * 2016-05-31 2017-12-07 Kt - Kinetics Technology Spa Catalyst for low temperature ethanol steam reforming and related process
US10514165B2 (en) 2016-07-29 2019-12-24 Clearsign Combustion Corporation Perforated flame holder and system including protection from abrasive or corrosive fuel
US10539326B2 (en) 2016-09-07 2020-01-21 Clearsign Combustion Corporation Duplex burner with velocity-compensated mesh and thickness
WO2018085152A1 (en) 2016-11-04 2018-05-11 Clearsign Combustion Corporation Plasma pilot
WO2018208695A1 (en) 2017-05-08 2018-11-15 Clearsign Combustion Corporation Combustion system including a mixing tube and a perforated flame holder
US11136238B2 (en) 2018-05-21 2021-10-05 Praxair Technology, Inc. OTM syngas panel with gas heated reformer
CN112387218B (zh) * 2020-11-04 2022-09-13 大连海事大学 一种自热型列管式重整制氢反应器
CN112577031A (zh) * 2020-12-10 2021-03-30 广东醇氢新能源研究院有限公司 一种氢气反应器和制氢系统
CN112999986A (zh) * 2021-04-21 2021-06-22 广东蓝玖新能源科技有限公司 板式反应器

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE9320711U1 (de) * 1993-07-21 1995-01-19 Fraunhofer Ges Forschung Chemischer Reaktor mit integriertem Brenner
JP3442167B2 (ja) * 1993-12-28 2003-09-02 千代田化工建設株式会社 改質器における伝熱方法
GR1003235B (el) * 1998-05-22 1999-10-13 Διεργασια παραγωγης υδρογονου και ηλεκτρικης ενεργειας απο αναμορφωση βιο-αιθανολης, με χρηση κυψελιδων καυσιμου και με μηδενικη εκπομπη ρυπων
US6274101B1 (en) * 1998-09-08 2001-08-14 Uop Llc Apparatus for in-situ reaction heating
CN1217732C (zh) * 2000-10-27 2005-09-07 环球油品公司 利用板排列加热和预热反应物的方法和设备
WO2003035546A1 (en) * 2001-10-22 2003-05-01 Lattice Intellectual Property Ltd Method and apparatus for steam reforming
US7179313B2 (en) * 2002-08-02 2007-02-20 Catacel Corp. Regenerative autothermal catalytic steam reformer
JP2007091584A (ja) * 2005-09-27 2007-04-12 Samsung Sdi Co Ltd 燃料改質装置

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