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MX2014000293A - Sistema de membrana de transporte de oxigeno y metodo de transferencia de calor a reactores cataliticos/de proceso. - Google Patents

Sistema de membrana de transporte de oxigeno y metodo de transferencia de calor a reactores cataliticos/de proceso.

Info

Publication number
MX2014000293A
MX2014000293A MX2014000293A MX2014000293A MX2014000293A MX 2014000293 A MX2014000293 A MX 2014000293A MX 2014000293 A MX2014000293 A MX 2014000293A MX 2014000293 A MX2014000293 A MX 2014000293A MX 2014000293 A MX2014000293 A MX 2014000293A
Authority
MX
Mexico
Prior art keywords
transport membrane
oxygen transport
membrane elements
catalytic reactor
oxygen
Prior art date
Application number
MX2014000293A
Other languages
English (en)
Inventor
Sean M Kelly
Brian R Kromer
Michael M Litwin
Lee J Rosen
Gervase Maxwell Christie
Jamie R Wilson
Lawrence W Kosowski
Charles Robinson
Original Assignee
Praxair Technology Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Praxair Technology Inc filed Critical Praxair Technology Inc
Publication of MX2014000293A publication Critical patent/MX2014000293A/es

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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
    • C01B3/384—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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • 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
    • B01J19/2475—Membrane 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
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/2485—Monolithic 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
    • 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
    • B01J8/0285—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0229—Purification or separation processes
    • C01B13/0248—Physical processing only
    • C01B13/0251—Physical processing only by making use of membranes
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00309—Controlling the temperature by indirect heat exchange 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00504—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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00893—Feeding means for the reactants
    • B01J2208/00902—Nozzle-type feeding 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
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00157—Controlling the temperature by means of a burner
    • 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
    • C01B2203/02—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
    • C01B2203/0238—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a carbon dioxide 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
    • C01B2203/06—Integration with other chemical processes
    • C01B2203/062—Hydrocarbon production, e.g. Fischer-Tropsch process
    • 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
    • C01B2203/08—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
    • C01B2203/0827—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel at least part of the fuel being a recycle 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
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0872—Methods of cooling
    • C01B2203/0883—Methods of cooling by indirect heat exchange
    • 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
    • C01B2203/1041—Composition of the catalyst
    • C01B2203/1047—Group VIII metal catalysts
    • C01B2203/1052—Nickel or cobalt catalysts
    • C01B2203/1058—Nickel 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
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1235—Hydrocarbons
    • C01B2203/1241—Natural gas or methane
    • 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
    • Y02P20/141—Feedstock

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Analytical Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

Se proporciona un método y aparato para producir calor utilizado en un proceso de producción de gas de síntesis. El método y aparato divulgados incluyen una pluralidad de elementos tubulares de membrana de transporte de oxígeno adaptados para separar oxígeno de una corriente que contiene oxígeno que entra en contacto con el lado de retención de los elementos de la membrana. El oxígeno permeado es quemado con una corriente de gas de síntesis que contiene hidrógeno que entra en contacto con el lado de permeación de los elementos tubulares de la membrana de transporte de oxígeno generando así una corriente de producto de reacción y calor radiante. El presente método y aparato también incluyen al menos un reactor catalítico que contiene un catalizador para promover la reacción de reformado con vapor donde el reactor catalítico está rodeado por la pluralidad de elementos tubulares de la membrana de transporte de oxígeno. El factor de vista entre el reactor catalítico y la pluralidad de elementos tubulares de la membrana de transporte de oxígeno que irradian calor al reactor catalítico es mayor o igual a 0,5.
MX2014000293A 2011-07-08 2012-07-05 Sistema de membrana de transporte de oxigeno y metodo de transferencia de calor a reactores cataliticos/de proceso. MX2014000293A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US13/179,279 US8349214B1 (en) 2011-07-08 2011-07-08 Synthesis gas method and apparatus
PCT/US2012/045519 WO2013009560A1 (en) 2011-07-08 2012-07-05 Oxygen transport membrane system and method for transferring heat to catalytic/process reactors

Publications (1)

Publication Number Publication Date
MX2014000293A true MX2014000293A (es) 2014-06-23

Family

ID=46516866

Family Applications (2)

Application Number Title Priority Date Filing Date
MX2014000291A MX2014000291A (es) 2011-07-08 2012-07-05 Metodo y aparato para producir gas de sintesis.
MX2014000293A MX2014000293A (es) 2011-07-08 2012-07-05 Sistema de membrana de transporte de oxigeno y metodo de transferencia de calor a reactores cataliticos/de proceso.

Family Applications Before (1)

Application Number Title Priority Date Filing Date
MX2014000291A MX2014000291A (es) 2011-07-08 2012-07-05 Metodo y aparato para producir gas de sintesis.

Country Status (10)

Country Link
US (2) US8349214B1 (es)
EP (2) EP2729406A1 (es)
CN (2) CN103764550B (es)
BR (2) BR112014000327A2 (es)
CA (2) CA2839722A1 (es)
CL (2) CL2014000046A1 (es)
CO (2) CO6930346A2 (es)
MX (2) MX2014000291A (es)
RU (1) RU2579584C2 (es)
WO (2) WO2013009559A1 (es)

Families Citing this family (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9561476B2 (en) 2010-12-15 2017-02-07 Praxair Technology, Inc. Catalyst containing oxygen transport membrane
US8435332B2 (en) * 2011-04-08 2013-05-07 Praxair Technology, Inc. Oxygen separation module and apparatus
US9486735B2 (en) 2011-12-15 2016-11-08 Praxair Technology, Inc. Composite oxygen transport membrane
CN103987681B (zh) 2011-12-15 2016-08-24 普莱克斯技术有限公司 复合氧气传送膜
WO2013117948A1 (en) * 2012-02-06 2013-08-15 Helbio Societé Anonyme Hydrogen And Energy Production Systems Heat integrated reformer with catalytic combustion for hydrogen production
JP6078655B2 (ja) * 2012-10-31 2017-02-08 コリア・インスティテュート・オブ・マシナリー・アンド・マテリアルズＫｏｒｅａ Ｉｎｓｔｉｔｕｔｅ Ｏｆ Ｍａｃｈｉｎｅｒｙ ＆ Ｍａｔｅｒｉａｌｓ 純酸素燃焼と触媒転換工程を連携した融合型二酸化炭素転換システム
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
WO2014107707A2 (en) 2013-01-07 2014-07-10 Praxair Technology, Inc. High emissivity and high temperature diffusion barrier coatings for an oxygen transport membrane assembly
CA2909974C (en) 2013-04-26 2019-03-05 Praxair Technology, Inc. Method and system for producing a synthesis gas in an oxygen transport membrane based reforming system
US9023245B2 (en) * 2013-04-26 2015-05-05 Praxair Technology, Inc. Method and system for producing a synthesis gas using an oxygen transport membrane based reforming system with secondary reforming
US9115045B2 (en) 2013-04-26 2015-08-25 Praxair Technology, Inc. Method and system for producing methanol using an oxygen transport membrane based reforming system
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
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
US9365422B2 (en) 2013-04-26 2016-06-14 Praxair Technology, Inc. Method and system for producing a synthesis gas in an oxygen transport membrane based reforming system with recycling of the produced synthesis gas
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
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
US20140319425A1 (en) * 2013-04-26 2014-10-30 Shrikar Chakravarti Method and system for producing a synthesis gas in an oxygen transport membrane based reforming system using a combined feed stream
DE102013107610A1 (de) * 2013-07-17 2015-01-22 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Membrantrennverfahren und Membrananlage zur energieeffizienten Erzeugung von Sauerstoff
CN105517950B (zh) * 2013-09-05 2018-12-14 普莱克斯技术有限公司 用于使用具有二级重整和辅助热源的基于氧传输膜的重整系统来生产合成气的方法和系统
MX383132B (es) * 2013-09-05 2025-03-13 Praxair Technology Inc Metodo para producir metanol usando un sistema reformador integrado con base en membrana de transporte de oxigeno.
CN106413873B (zh) * 2013-10-07 2019-10-18 普莱克斯技术有限公司 陶瓷氧输送膜片阵列重整反应器
WO2015054363A2 (en) 2013-10-08 2015-04-16 Praxair Technology, Inc. System method for temperature control in an oxygen transport membrane based reactor
US9556027B2 (en) 2013-12-02 2017-01-31 Praxair Technology, Inc. Method and system for producing hydrogen using an oxygen transport membrane based reforming system with secondary reforming
CA2937943A1 (en) 2014-02-12 2015-08-20 Praxair Technology, Inc. Oxygen transport membrane reactor based method and system for generating electric power
CN106103339B (zh) 2014-03-05 2018-09-04 普莱克斯技术有限公司 用于由fischer-tropsch方法使用由基于氧传输膜的重整反应器产生的合成气体产生液态烃产物的方法
WO2015160609A1 (en) 2014-04-16 2015-10-22 Praxair Technology, Inc. Method and system for oxygen transport membrane enhanced integrated gasifier combined cycle (igcc)
US9789445B2 (en) 2014-10-07 2017-10-17 Praxair Technology, Inc. Composite oxygen ion transport membrane
WO2016178915A1 (en) 2015-05-01 2016-11-10 Velocys Technologies, Ltd. Process for operating an integrated gas-to-liquids facility
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
JP2019513081A (ja) 2016-04-01 2019-05-23 プラクスエア・テクノロジー・インコーポレイテッド 触媒含有酸素輸送膜
US20180178188A1 (en) * 2016-12-22 2018-06-28 Extiel Holdings, Llc Sectionalized box style steam methane reformer
EP3596005B1 (en) 2017-03-16 2021-05-19 Praxair Technology, Inc. Method and system for producing hydrogen using an oxygen transport membrane based reforming system
US10822233B2 (en) 2018-05-11 2020-11-03 Doosan Fuel Cell America, Inc. Reformer including catalyst in an inlet plenum
EP3797085A1 (en) 2018-05-21 2021-03-31 Praxair Technology, Inc. Otm syngas panel with gas heated reformer
US20230070799A1 (en) 2020-01-13 2023-03-09 Praxair Technology, Inc. Oxygen transport membrane reactors for decarbonization
KR102701705B1 (ko) * 2021-10-06 2024-09-03 두산에너빌리티 주식회사 복합 개질기
US11819815B2 (en) * 2021-11-19 2023-11-21 Infinium Technology, Llc Catalytic reactor for the conversion of carbon dioxide and hydrogen to syngas
CA3168940A1 (en) * 2022-03-02 2023-09-02 Christopher J. Nagel Processes for producing reactant chemical substances

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6048472A (en) 1997-12-23 2000-04-11 Air Products And Chemicals, Inc. Production of synthesis gas by mixed conducting membranes
US6296686B1 (en) * 1998-06-03 2001-10-02 Praxair Technology, Inc. Ceramic membrane for endothermic reactions
US6139810A (en) 1998-06-03 2000-10-31 Praxair Technology, Inc. Tube and shell reactor with oxygen selective ion transport ceramic reaction tubes
US6114400A (en) 1998-09-21 2000-09-05 Air Products And Chemicals, Inc. Synthesis gas production by mixed conducting membranes with integrated conversion into liquid products
US6394043B1 (en) * 2000-12-19 2002-05-28 Praxair Technology, Inc. Oxygen separation and combustion apparatus and method
US6695983B2 (en) * 2001-04-24 2004-02-24 Praxair Technology, Inc. Syngas production method utilizing an oxygen transport membrane
US6783750B2 (en) * 2001-08-22 2004-08-31 Praxair Technology, Inc. Hydrogen production method
RU2198838C1 (ru) * 2002-01-29 2003-02-20 Писаренко Елена Витальевна Способ получения метанола
US20070029342A1 (en) 2002-10-04 2007-02-08 Alexander Cross Laboratory workstation for providing samples
US7261751B2 (en) 2004-08-06 2007-08-28 Conocophillips Company Synthesis gas process comprising partial oxidation using controlled and optimized temperature profile
US7427368B2 (en) 2005-08-16 2008-09-23 Praxair Technology, Inc. Synthesis gas and carbon dioxide generation method
US7858214B2 (en) 2005-09-21 2010-12-28 Delphi Technologies, Inc. Method and apparatus for light internal reforming in a solid oxide fuel cell system
US20070292342A1 (en) 2006-06-19 2007-12-20 John William Hemmings Synthesis gas production method and reactor
US7856829B2 (en) * 2006-12-15 2010-12-28 Praxair Technology, Inc. Electrical power generation method
US8262755B2 (en) * 2007-06-05 2012-09-11 Air Products And Chemicals, Inc. Staged membrane oxidation reactor system
RU2388118C1 (ru) * 2008-09-26 2010-04-27 Дмитрий Львович Астановский Установка для производства электроэнергии из углеводородного сырья
RU2417834C1 (ru) * 2009-10-09 2011-05-10 Андрей Юрьевич Беляев Конвектор для осуществления газофазных каталитических процессов
US20110142722A1 (en) * 2009-12-14 2011-06-16 John William Hemmings Method and apparatus for producing synthesis gas

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WO2013009559A1 (en) 2013-01-17
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CA2839722A1 (en) 2013-01-17
US9180419B2 (en) 2015-11-10
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