CA2227598A1 - Synthesis gas production by steam reforming using catalyzed hardware - Google Patents
Synthesis gas production by steam reforming using catalyzed hardwareInfo
- Publication number
- CA2227598A1 CA2227598A1 CA002227598A CA2227598A CA2227598A1 CA 2227598 A1 CA2227598 A1 CA 2227598A1 CA 002227598 A CA002227598 A CA 002227598A CA 2227598 A CA2227598 A CA 2227598A CA 2227598 A1 CA2227598 A1 CA 2227598A1
- Authority
- CA
- Canada
- Prior art keywords
- steam reforming
- hydrogen
- steam
- gas
- synthesis gas
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 238000000629 steam reforming Methods 0.000 title abstract 5
- 230000015572 biosynthetic process Effects 0.000 title 1
- 238000004519 manufacturing process Methods 0.000 title 1
- 238000003786 synthesis reaction Methods 0.000 title 1
- 239000007789 gas Substances 0.000 abstract 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 4
- 229910052739 hydrogen Inorganic materials 0.000 abstract 4
- 239000001257 hydrogen Substances 0.000 abstract 4
- 239000003054 catalyst Substances 0.000 abstract 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000010409 thin film Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/06—Catalytic reforming characterised by the catalyst used
- C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof
-
- 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
- B01J15/00—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor
- B01J15/005—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; 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
- 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
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
- B01J19/243—Tubular reactors spirally, concentrically or zigzag wound
-
- 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
- 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
-
- 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
- C01B3/40—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 characterised by the catalyst
-
- 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
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- 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
- C01B2203/0816—Heating by flames
-
- 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
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0866—Methods of heating the process for making hydrogen or synthesis gas by combination of different heating methods
-
- 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
- C01B2203/14—Details of the flowsheet
- C01B2203/142—At least two reforming, decomposition or partial oxidation steps in series
- C01B2203/143—Three or more reforming, decomposition or partial oxidation steps in series
-
- 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
- Y02E60/32—Hydrogen storage
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Abstract
The present invention provides an improvement in a process for the preparation of hydrogen and a carbon monoxide-rich gas by steam reforming of a hydrogen-rich gas in the presence of a steam reforming catalyst. The improvement comprising the essential steps of passing a heated, prereformed hydrogen feedstock through a second tubular reactor which is provided with a thin film of the steam reforming catalyst, and which is heated by the burning of fuel, thereby to obtain a partially-steam-reformed gas effluent and hot flue gas, passing the partially-steam-reformed gas effluent through a fixed bed, steam reforming catalyst, and withdrawing a product gas stream comprising hydrogen and a carbon monoxide- rich gas from the fixed bed.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US3539697P | 1997-01-22 | 1997-01-22 | |
US60/035,396 | 1997-01-22 |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2227598A1 true CA2227598A1 (en) | 1998-07-22 |
CA2227598C CA2227598C (en) | 2007-09-11 |
Family
ID=21882426
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002227598A Expired - Fee Related CA2227598C (en) | 1997-01-22 | 1998-01-21 | Synthesis gas production by steam reforming using catalyzed hardware |
Country Status (16)
Country | Link |
---|---|
US (1) | US5932141A (en) |
EP (1) | EP0855366B1 (en) |
JP (1) | JP4521735B2 (en) |
KR (1) | KR100547540B1 (en) |
CN (1) | CN1269724C (en) |
AT (1) | ATE200884T1 (en) |
AU (1) | AU728728C (en) |
CA (1) | CA2227598C (en) |
DE (1) | DE69800734T2 (en) |
DK (1) | DK0855366T3 (en) |
ES (1) | ES2158621T3 (en) |
NO (1) | NO318107B1 (en) |
NZ (1) | NZ329613A (en) |
RU (1) | RU2218301C2 (en) |
TW (1) | TW482741B (en) |
UA (1) | UA61888C2 (en) |
Families Citing this family (63)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK173496B1 (en) * | 1998-07-16 | 2001-01-02 | Topsoe Haldor As | Process for producing synthesis gas by steam vapor reforming using a catalyzed metal surface |
KR100401369B1 (en) | 1998-07-21 | 2003-10-17 | 할도르 토프쉐 에이/에스 | Synthesis gas production by steam reforming |
DK173742B1 (en) * | 1998-09-01 | 2001-08-27 | Topsoe Haldor As | Process and reactor system for producing synthesis gas |
DK173897B1 (en) | 1998-09-25 | 2002-02-04 | Topsoe Haldor As | Process for autothermal reforming of a hydrocarbon feed containing higher hydrocarbons |
EP1584603A3 (en) * | 1999-05-27 | 2007-06-13 | Haldor Topsoe A/S | Steam reforming reactor for synthesis gas production |
EP1055637B1 (en) | 1999-05-27 | 2005-11-02 | Haldor Topsoe A/S | Synthesis gas production by steam reforming |
EP1069070B1 (en) * | 1999-07-15 | 2011-11-30 | Haldor Topsoe A/S | Process for the catalytic steam reforming of a hydrocarbon feedstock |
US20040161381A1 (en) * | 1999-12-02 | 2004-08-19 | Thomsen Soren Gyde | Process and reactor for carrying out non-adiabatic catalytic reactions |
PT1106570E (en) * | 1999-12-02 | 2013-10-15 | Haldor Topsoe As | Process for carrying out non-adiabatic catalytic reactions |
AU2002211388A1 (en) | 2000-10-02 | 2002-04-15 | Chevron U.S.A. Inc. | Process for reducing coke formation in hydrocarbon processing by application of radio frequency electromagnetic radiation |
RU2167808C1 (en) * | 2000-10-09 | 2001-05-27 | Пискунов Семен Евсеевич | Synthetic gas generation process |
US6890672B2 (en) | 2001-06-26 | 2005-05-10 | Idatech, Llc | Fuel processor feedstock delivery system |
US6818028B2 (en) * | 2001-07-18 | 2004-11-16 | Kellogg Brown & Root, Inc. | Steam-methane reformer furnace with convection-heated pre-reformer |
AU2003219821A1 (en) * | 2002-02-22 | 2003-09-09 | Chevron U.S.A. Inc. | Process for reducing metal catalyzed coke formation in hydrocarbon processing |
US20030223926A1 (en) | 2002-04-14 | 2003-12-04 | Edlund David J. | Steam reforming fuel processor, burner assembly, and methods of operating the same |
EP1403217A1 (en) | 2002-09-26 | 2004-03-31 | Haldor Topsoe A/S | Process and apparatus for the preparation of synthesis gas |
ES2405587T3 (en) * | 2002-09-26 | 2013-05-31 | Haldor Topsoe A/S | Procedure and apparatus for the preparation of synthesis gas |
EP1413547A1 (en) | 2002-09-26 | 2004-04-28 | Haldor Topsoe A/S | Process for the production of synthesis gas |
CA2410927A1 (en) * | 2002-11-05 | 2004-05-05 | Michel Petitclerc | Electrically heated reactor for reforming in gaseous phase |
EP1445235B1 (en) * | 2003-02-05 | 2012-03-07 | Haldor Topsoe A/S | Process for treatment of synthesis gas |
CA2516355A1 (en) * | 2003-02-24 | 2004-09-10 | Texaco Development Corporation | Diesel steam reforming with co2 fixing |
US7427388B2 (en) * | 2004-03-19 | 2008-09-23 | Air Products And Chemicals, Inc. | Process for improving prereforming and reforming of natural gas containing higher hydrocarbons along with methane |
US7892511B2 (en) | 2004-07-02 | 2011-02-22 | Kellogg Brown & Root Llc | Pseudoisothermal ammonia process |
US7320778B2 (en) * | 2004-07-21 | 2008-01-22 | Catacel Corp. | High-performance catalyst support |
US7472936B2 (en) * | 2005-04-14 | 2009-01-06 | Catacel Corp. | Tool for insertion and removal of a catalytic reactor cartridge |
US20060230613A1 (en) * | 2005-04-14 | 2006-10-19 | Catacel Corporation | Catalytic reactor cartridge |
US7565743B2 (en) * | 2005-04-14 | 2009-07-28 | Catacel Corp. | Method for insertion and removal of a catalytic reactor cartridge |
US7682580B2 (en) * | 2005-05-19 | 2010-03-23 | Catacel Corp. | Catalytic reactor having radial leaves |
US7632322B2 (en) * | 2005-06-07 | 2009-12-15 | Idatech, Llc | Hydrogen-producing fuel processing assemblies, heating assemblies, and methods of operating the same |
US7504048B2 (en) * | 2005-06-14 | 2009-03-17 | Air Products And Chemicals, Inc. | Axial convective reformer |
US7501102B2 (en) * | 2005-07-28 | 2009-03-10 | Catacel Corp. | Reactor having improved heat transfer |
US7588738B2 (en) * | 2005-08-23 | 2009-09-15 | Exxonmobil Chemical Patents Inc. | Series catalyst beds |
JP4724029B2 (en) * | 2006-03-27 | 2011-07-13 | アイシン精機株式会社 | Method for shutting down reformer |
US7629067B2 (en) | 2006-05-22 | 2009-12-08 | Idatech, Llc | Hydrogen-producing fuel processing systems and fuel cell systems with a liquid leak detection system |
US7501078B2 (en) * | 2007-01-10 | 2009-03-10 | Air Products And Chemicals, Inc. | Process for generating synthesis gas using catalyzed structured packing |
US7771585B2 (en) | 2007-03-09 | 2010-08-10 | Southern Company | Method and apparatus for the separation of a gas-solids mixture in a circulating fluidized bed reactor |
US7850944B2 (en) * | 2008-03-17 | 2010-12-14 | Air Products And Chemicals, Inc. | Steam-hydrocarbon reforming method with limited steam export |
US20100147749A1 (en) * | 2008-12-11 | 2010-06-17 | American Air Liquide, Inc. | Multi-Metallic Catalysts For Pre-Reforming Reactions |
US9561476B2 (en) | 2010-12-15 | 2017-02-07 | Praxair Technology, Inc. | Catalyst containing oxygen transport membrane |
CN103011077B (en) * | 2011-09-27 | 2016-04-06 | 中国科学院宁波材料技术与工程研究所 | A kind of catalytically reforming hydrogen producing method and catalytic unit |
US9486735B2 (en) | 2011-12-15 | 2016-11-08 | Praxair Technology, Inc. | Composite oxygen transport membrane |
WO2013089895A1 (en) | 2011-12-15 | 2013-06-20 | Praxair Technology, Inc. | Composite oxygen transport membrane |
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 |
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 |
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 |
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 |
EP3055054A2 (en) | 2013-10-07 | 2016-08-17 | Praxair Technology Inc. | Ceramic oxygen transport membrane array reactor and reforming method |
US9573094B2 (en) | 2013-10-08 | 2017-02-21 | Praxair Technology, Inc. | System and method for temperature control in an oxygen transport membrane based reactor |
CA2926757C (en) | 2013-12-02 | 2020-02-25 | Praxair Technology, Inc. | Method and system for producing hydrogen using an oxygen transport membrane based reforming system with secondary reforming |
CN105980666B (en) | 2014-02-12 | 2019-04-09 | 普莱克斯技术有限公司 | For generating the method and system based on oxygen transport membrane reactor of electric power |
US20170021322A1 (en) | 2014-04-02 | 2017-01-26 | Haldor Topsøes A/S | Pseudo-isothermal reactor |
US10822234B2 (en) | 2014-04-16 | 2020-11-03 | 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 |
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 |
KR102154420B1 (en) | 2016-04-01 | 2020-09-10 | 프랙스에어 테크놀로지, 인코포레이티드 | Catalyst-containing oxygen transport membrane |
WO2018208373A1 (en) * | 2017-05-09 | 2018-11-15 | Exxonmobil Chemical Patents Inc. | Linear alpha olefin process using temperature control in oligomerization reactor |
WO2019226435A1 (en) | 2018-05-21 | 2019-11-28 | Praxair Technology, Inc. | Otm syngas panel with gas heated reformer |
EP4247533A1 (en) | 2020-11-19 | 2023-09-27 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Reforming reactor comprising reformer tubes with enlarged outer surface area and structured catalyst |
EP4155259A1 (en) | 2021-09-22 | 2023-03-29 | L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Method for producing synthesis gas with reduced steam export |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1008667A (en) * | 1972-06-30 | 1977-04-19 | Foster Wheeler Corporation | Catalytic steam reforming |
US4079017A (en) * | 1976-11-19 | 1978-03-14 | Pullman Incorporated | Parallel steam reformers to provide low energy process |
EP0049967A1 (en) * | 1980-10-14 | 1982-04-21 | Imperial Chemical Industries Plc | Ammonia production process |
US4844837A (en) * | 1982-09-30 | 1989-07-04 | Engelhard Corporation | Catalytic partial oxidation process |
DE3480192D1 (en) * | 1983-03-25 | 1989-11-23 | Ici Plc | Steam reforming |
GB8308343D0 (en) * | 1983-03-25 | 1983-05-05 | Ici Plc | Steam reforming |
GB8309359D0 (en) * | 1983-04-06 | 1983-05-11 | Ici Plc | Synthesis gas |
DK165946C (en) * | 1985-03-21 | 1993-07-05 | Haldor Topsoe As | REFORMING PROCESS DURING HEAT EXCHANGE AND REACTOR THEREOF |
GB8728882D0 (en) * | 1987-12-10 | 1988-01-27 | Ici Plc | Hydrogen |
EP0334540B1 (en) * | 1988-03-24 | 1993-10-20 | Imperial Chemical Industries Plc | Two-step steam-reforming process |
JP2607644B2 (en) * | 1988-10-27 | 1997-05-07 | 三菱重工業株式会社 | Methanol reforming method |
GB9000389D0 (en) * | 1990-01-08 | 1990-03-07 | Ici Plc | Steam reforming |
DK167864B1 (en) * | 1990-02-02 | 1993-12-27 | Topsoe Haldor As | PROCEDURE AND REACTOR SYSTEM FOR REFORMING CARBON HYDROIDS DURING HEAT EXCHANGE |
ATE156778T1 (en) * | 1991-07-09 | 1997-08-15 | Ici Plc | SYNTHESIS GAS GENERATION |
US5429809A (en) * | 1991-09-23 | 1995-07-04 | Haldor Topsoe A/S | Process and reactor for carrying out non-adiabatic catalytic reactions |
JPH05155602A (en) * | 1991-12-09 | 1993-06-22 | Sekiyu Sangyo Kasseika Center | Thin type steam reforming reactor |
JPH05186203A (en) * | 1992-01-07 | 1993-07-27 | Toshiba Corp | Catalytic element for steam reforming |
FR2696168B1 (en) * | 1992-09-25 | 1994-12-09 | Inst Francais Du Petrole | Process and device for the production of synthesis gas and associated use. |
JPH06219705A (en) * | 1993-01-22 | 1994-08-09 | Mitsubishi Electric Corp | Fuel reformer |
MY131526A (en) * | 1993-12-27 | 2007-08-30 | Shell Int Research | A process for the preparation of carbon monoxide and/or hydrogen |
-
1998
- 1998-01-16 DK DK98100669T patent/DK0855366T3/en active
- 1998-01-16 EP EP98100669A patent/EP0855366B1/en not_active Expired - Lifetime
- 1998-01-16 DE DE69800734T patent/DE69800734T2/en not_active Expired - Lifetime
- 1998-01-16 AT AT98100669T patent/ATE200884T1/en active
- 1998-01-16 ES ES98100669T patent/ES2158621T3/en not_active Expired - Lifetime
- 1998-01-17 TW TW087100593A patent/TW482741B/en not_active IP Right Cessation
- 1998-01-21 UA UA98010355A patent/UA61888C2/en unknown
- 1998-01-21 JP JP00985598A patent/JP4521735B2/en not_active Expired - Fee Related
- 1998-01-21 NO NO19980274A patent/NO318107B1/en not_active IP Right Cessation
- 1998-01-21 RU RU98102132/15A patent/RU2218301C2/en not_active IP Right Cessation
- 1998-01-21 CA CA002227598A patent/CA2227598C/en not_active Expired - Fee Related
- 1998-01-21 NZ NZ329613A patent/NZ329613A/en not_active IP Right Cessation
- 1998-01-21 AU AU52158/98A patent/AU728728C/en not_active Ceased
- 1998-01-22 KR KR1019980001842A patent/KR100547540B1/en not_active IP Right Cessation
- 1998-01-22 US US09/010,529 patent/US5932141A/en not_active Expired - Lifetime
- 1998-01-22 CN CNB981056520A patent/CN1269724C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
ATE200884T1 (en) | 2001-05-15 |
NZ329613A (en) | 1998-11-25 |
NO980274L (en) | 1998-07-23 |
DE69800734T2 (en) | 2001-08-09 |
KR19980070692A (en) | 1998-10-26 |
NO318107B1 (en) | 2005-01-31 |
CN1269724C (en) | 2006-08-16 |
ES2158621T3 (en) | 2001-09-01 |
NO980274D0 (en) | 1998-01-21 |
TW482741B (en) | 2002-04-11 |
AU728728C (en) | 2001-08-30 |
AU728728B2 (en) | 2001-01-18 |
DE69800734D1 (en) | 2001-06-07 |
US5932141A (en) | 1999-08-03 |
AU5215898A (en) | 1998-07-30 |
JPH10297904A (en) | 1998-11-10 |
DK0855366T3 (en) | 2001-08-13 |
CN1196330A (en) | 1998-10-21 |
RU2218301C2 (en) | 2003-12-10 |
EP0855366B1 (en) | 2001-05-02 |
JP4521735B2 (en) | 2010-08-11 |
UA61888C2 (en) | 2003-12-15 |
CA2227598C (en) | 2007-09-11 |
KR100547540B1 (en) | 2006-03-23 |
EP0855366A1 (en) | 1998-07-29 |
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