TW200630158A - Membrane enhanced reactor - Google Patents
Membrane enhanced reactorInfo
- Publication number
- TW200630158A TW200630158A TW094132238A TW94132238A TW200630158A TW 200630158 A TW200630158 A TW 200630158A TW 094132238 A TW094132238 A TW 094132238A TW 94132238 A TW94132238 A TW 94132238A TW 200630158 A TW200630158 A TW 200630158A
- Authority
- TW
- Taiwan
- Prior art keywords
- hydrogen
- intermediate layer
- disclosed
- reactor
- reaction products
- Prior art date
Links
- 239000012528 membrane Substances 0.000 title abstract 2
- 239000001257 hydrogen Substances 0.000 abstract 7
- 229910052739 hydrogen Inorganic materials 0.000 abstract 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 5
- 239000007795 chemical reaction product Substances 0.000 abstract 3
- 239000011230 binding agent Substances 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 2
- 150000002431 hydrogen Chemical class 0.000 abstract 2
- 239000002184 metal Substances 0.000 abstract 2
- 238000000926 separation method Methods 0.000 abstract 2
- 239000000758 substrate Substances 0.000 abstract 2
- 239000002245 particle Substances 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
- 238000000629 steam reforming Methods 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
- B01D71/024—Oxides
- B01D71/025—Aluminium oxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
- B01D63/069—Tubular membrane modules comprising a bundle of tubular membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
- B01D63/062—Tubular membrane modules with membranes on a surface of a support tube
- B01D63/065—Tubular membrane modules with membranes on a surface of a support tube on the outer surface thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0039—Inorganic membrane manufacture
- B01D67/0069—Inorganic membrane manufacture by deposition from the liquid phase, e.g. electrochemical deposition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0081—After-treatment of organic or inorganic membranes
- B01D67/0088—Physical treatment with compounds, e.g. swelling, coating or impregnation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
- B01D71/022—Metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
- B01D71/022—Metals
- B01D71/0223—Group 8, 9 or 10 metals
- B01D71/02231—Palladium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
- B01D71/022—Metals
- B01D71/0223—Group 8, 9 or 10 metals
- B01D71/02232—Nickel
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
- B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
-
- 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
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
- C01B3/501—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion
- C01B3/503—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion characterised by the membrane
- C01B3/505—Membranes containing palladium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/42—Catalysts within the flow path
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/22—Thermal or heat-resistance properties
-
- 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
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0405—Purification by membrane separation
- C01B2203/041—In-situ membrane purification during hydrogen production
-
- 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
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/047—Composition of the impurity the impurity being carbon monoxide
-
- 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
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
-
- 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
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/048—Composition of the impurity the impurity being an organic compound
-
- 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
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/0495—Composition of the impurity the impurity being water
-
- 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
- C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
- C01B2203/86—Carbon dioxide sequestration
-
- 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
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
Abstract
A hydrogen producing reactor is disclosed. The hydrogen producing reactor has a reaction chamber containing a catalyst bed adapted to produce reaction products containing hydrogen from a hydrogen-producing feedstock. The reaction chamber also includes a hydrogen-selective, hydrogen-permeable gas separation module adapted to receive the reaction products from the catalyst bed and to separate a product stream containing hydrogen from the reaction products. The gas separation module comprises a porous substrate, an intermediate layer located at the porous substrate, and a hydrogen-selective membrane overlying the intermediate layer. The intermediate layer comprises particles and a binder metal, where the binder metal is distributed through out the intermediate layer. A steam reforming process is also disclosed using the disclosed reactor.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US61160804P | 2004-09-21 | 2004-09-21 |
Publications (1)
Publication Number | Publication Date |
---|---|
TW200630158A true TW200630158A (en) | 2006-09-01 |
Family
ID=35708904
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW094132238A TW200630158A (en) | 2004-09-21 | 2005-09-19 | Membrane enhanced reactor |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1789172A1 (en) |
JP (1) | JP2008513337A (en) |
AU (1) | AU2005287034B2 (en) |
CA (1) | CA2580580A1 (en) |
NO (1) | NO20071532L (en) |
TW (1) | TW200630158A (en) |
WO (1) | WO2006034086A1 (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111905504A (en) * | 2020-07-03 | 2020-11-10 | 王保林 | Industrial waste gas and metal particulate matter processing apparatus in waste gas |
US11322766B2 (en) | 2020-05-28 | 2022-05-03 | Saudi Arabian Oil Company | Direct hydrocarbon metal supported solid oxide fuel cell |
US11492255B2 (en) | 2020-04-03 | 2022-11-08 | Saudi Arabian Oil Company | Steam methane reforming with steam regeneration |
US11492254B2 (en) | 2020-06-18 | 2022-11-08 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
US11578016B1 (en) | 2021-08-12 | 2023-02-14 | Saudi Arabian Oil Company | Olefin production via dry reforming and olefin synthesis in a vessel |
US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
US11617981B1 (en) | 2022-01-03 | 2023-04-04 | Saudi Arabian Oil Company | Method for capturing CO2 with assisted vapor compression |
US11639290B2 (en) | 2020-06-04 | 2023-05-02 | Saudi Arabian Oil Company | Dry reforming of methane with carbon dioxide at elevated pressure |
US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol synthesis in a vessel |
US11787759B2 (en) | 2021-08-12 | 2023-10-17 | Saudi Arabian Oil Company | Dimethyl ether production via dry reforming and dimethyl ether synthesis in a vessel |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7727596B2 (en) * | 2004-07-21 | 2010-06-01 | Worcester Polytechnic Institute | Method for fabricating a composite gas separation module |
US8048199B2 (en) | 2007-02-20 | 2011-11-01 | Shell Oil Company | Method of making a leak stable gas separation membrane system |
US8366805B2 (en) | 2007-04-05 | 2013-02-05 | Worcester Polytechnic Institute | Composite structures with porous anodic oxide layers and methods of fabrication |
JP5147375B2 (en) * | 2007-12-11 | 2013-02-20 | 大日本印刷株式会社 | Reaction membrane, hydrogen production device and fuel cell |
JP5354516B2 (en) * | 2008-08-15 | 2013-11-27 | 日本碍子株式会社 | Hydrogen separator |
US8936883B2 (en) | 2009-03-10 | 2015-01-20 | Powercell Sweden Ab | Arrangement and method for generating hydrogen from hydrocarbon fuel |
CN101920332B (en) * | 2010-04-29 | 2012-05-02 | 西安西工大超晶科技发展有限责任公司 | Method for manufacturing stainless steel/copper composite gradient material heat exchange transition region component |
US8652239B2 (en) | 2010-05-03 | 2014-02-18 | Worcester Polytechnic Institute | High permeance sulfur tolerant Pd/Cu alloy membranes |
CN103298551B (en) | 2010-11-16 | 2017-08-29 | 荷兰能源建设基金中心 | The catalyst produced for hydrogen |
WO2013096183A1 (en) * | 2011-12-19 | 2013-06-27 | Shell Oil Company | A method of making a hydrogen separation composite membrane |
CN103182249B (en) * | 2011-12-30 | 2016-10-05 | 财团法人工业技术研究院 | Method for modifying porous substrate and modified porous substrate |
US20130171442A1 (en) * | 2011-12-30 | 2013-07-04 | Meng-Chang Lin | Method for modifying porous substrate and modified porous substrate |
JP5879161B2 (en) * | 2012-03-09 | 2016-03-08 | 旭化成ケミカルズ株式会社 | Water vapor separation membrane and method for producing the same |
WO2014189744A1 (en) | 2013-05-20 | 2014-11-27 | Shell Oil Company | Two-stage diesel aromatics saturation process utilizing intermediate stripping and base metal catalyst |
CN105013297B (en) * | 2014-04-23 | 2017-12-26 | 中国科学院大连化学物理研究所 | A kind of method with zeolite modified palladium base composite membrane |
EP3686318A1 (en) * | 2019-01-23 | 2020-07-29 | Paul Scherrer Institut | Porous transport layer based on plurality of sintered porous layers |
CN111424306B (en) * | 2020-04-13 | 2021-02-19 | 厦门通富微电子有限公司 | Bubble stripping device and electroplating solution electroplating system |
CN113041970B (en) * | 2021-03-17 | 2021-11-26 | 南京理工大学 | Catalytic membrane type reactor with built-in turbulent flow structure |
DE102022203604A1 (en) | 2022-04-11 | 2023-10-12 | Siemens Energy Global GmbH & Co. KG | Powder, ceramic wall, reaction chamber and process |
Family Cites Families (19)
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US5139541A (en) * | 1990-08-10 | 1992-08-18 | Bend Research, Inc. | Hydrogen-permeable composite metal membrane |
US5393325A (en) * | 1990-08-10 | 1995-02-28 | Bend Research, Inc. | Composite hydrogen separation metal membrane |
US5217506A (en) * | 1990-08-10 | 1993-06-08 | Bend Research, Inc. | Hydrogen-permeable composite metal membrane and uses thereof |
US5498278A (en) * | 1990-08-10 | 1996-03-12 | Bend Research, Inc. | Composite hydrogen separation element and module |
JPH04346824A (en) * | 1991-05-21 | 1992-12-02 | Mitsubishi Heavy Ind Ltd | Hydrogen separating membrane |
JPH0585702A (en) * | 1991-09-30 | 1993-04-06 | Mitsubishi Heavy Ind Ltd | Production of hydrogen separation membrane |
JP3117276B2 (en) * | 1992-04-09 | 2000-12-11 | 三菱重工業株式会社 | Hydrogen separation membrane |
JP3621785B2 (en) * | 1996-07-12 | 2005-02-16 | トヨタ自動車株式会社 | Hydrogen separation structure |
US6152987A (en) * | 1997-12-15 | 2000-11-28 | Worcester Polytechnic Institute | Hydrogen gas-extraction module and method of fabrication |
JP2001286742A (en) * | 2000-04-10 | 2001-10-16 | Mitsubishi Heavy Ind Ltd | Hydrogen separation membrane |
JP2002219341A (en) * | 2001-01-30 | 2002-08-06 | Kobe Steel Ltd | Supporting base for hydrogen-permselective membrane and hydrogen-permselective member |
FR2820988B1 (en) * | 2001-02-19 | 2003-04-25 | Cie D Etudes Des Technologies | COMPOSITE STRUCTURES OF SELECTIVELY HYDROGEN PERMEABLE MEMBRANES AND COMBUSTIBLE GAS PROCESSORS USING THE SAME |
US6916454B2 (en) * | 2001-03-30 | 2005-07-12 | Siemens Westinghouse Power Corporation | Metal gas separation membrane |
DE10135390A1 (en) * | 2001-07-25 | 2003-02-20 | Fraunhofer Ges Forschung | Metallic solution-diffusion membrane, used for separating and purifying hydrogen for use in the electronics, metals and chemical industry, consists of a macroporous base body with a thin metallic membrane layer |
US7001446B2 (en) * | 2002-03-05 | 2006-02-21 | Eltron Research, Inc. | Dense, layered membranes for hydrogen separation |
AU2003220048A1 (en) * | 2002-03-05 | 2003-09-22 | Eltron Research, Inc. | Hydrogen transport membranes |
CA2497441C (en) * | 2002-09-05 | 2013-11-19 | Shell Internationale Research Maatschappij B.V. | Apparatus and process for production of high purity hydrogen |
WO2004085034A2 (en) * | 2003-03-21 | 2004-10-07 | Worcester Polytechnic Institute | Composite gas separations modules having intermediate metal layers |
US7255726B2 (en) * | 2003-05-02 | 2007-08-14 | Worcester Polytechnic Institute | Composite gas separation modules having high Tamman temperature intermediate layers |
-
2005
- 2005-09-19 JP JP2007532531A patent/JP2008513337A/en active Pending
- 2005-09-19 EP EP05808744A patent/EP1789172A1/en not_active Withdrawn
- 2005-09-19 CA CA002580580A patent/CA2580580A1/en not_active Abandoned
- 2005-09-19 AU AU2005287034A patent/AU2005287034B2/en not_active Ceased
- 2005-09-19 TW TW094132238A patent/TW200630158A/en unknown
- 2005-09-19 WO PCT/US2005/033267 patent/WO2006034086A1/en active Application Filing
-
2007
- 2007-03-23 NO NO20071532A patent/NO20071532L/en not_active Application Discontinuation
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11492255B2 (en) | 2020-04-03 | 2022-11-08 | Saudi Arabian Oil Company | Steam methane reforming with steam regeneration |
US11322766B2 (en) | 2020-05-28 | 2022-05-03 | Saudi Arabian Oil Company | Direct hydrocarbon metal supported solid oxide fuel cell |
US11639290B2 (en) | 2020-06-04 | 2023-05-02 | Saudi Arabian Oil Company | Dry reforming of methane with carbon dioxide at elevated pressure |
US11492254B2 (en) | 2020-06-18 | 2022-11-08 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
CN111905504A (en) * | 2020-07-03 | 2020-11-10 | 王保林 | Industrial waste gas and metal particulate matter processing apparatus in waste gas |
US11578016B1 (en) | 2021-08-12 | 2023-02-14 | Saudi Arabian Oil Company | Olefin production via dry reforming and olefin synthesis in a vessel |
US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol synthesis in a vessel |
US11787759B2 (en) | 2021-08-12 | 2023-10-17 | Saudi Arabian Oil Company | Dimethyl ether production via dry reforming and dimethyl ether synthesis in a vessel |
US11617981B1 (en) | 2022-01-03 | 2023-04-04 | Saudi Arabian Oil Company | Method for capturing CO2 with assisted vapor compression |
Also Published As
Publication number | Publication date |
---|---|
NO20071532L (en) | 2007-06-20 |
WO2006034086A1 (en) | 2006-03-30 |
AU2005287034A1 (en) | 2006-03-30 |
CA2580580A1 (en) | 2006-03-30 |
JP2008513337A (en) | 2008-05-01 |
EP1789172A1 (en) | 2007-05-30 |
AU2005287034B2 (en) | 2009-06-11 |
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