RU2003111161A - Способ частичного окисления метана с использованием плотной керамической мембраны с селективной проницаемостью для кислорода - Google Patents
Способ частичного окисления метана с использованием плотной керамической мембраны с селективной проницаемостью для кислорода Download PDFInfo
- Publication number
- RU2003111161A RU2003111161A RU2003111161/15A RU2003111161A RU2003111161A RU 2003111161 A RU2003111161 A RU 2003111161A RU 2003111161/15 A RU2003111161/15 A RU 2003111161/15A RU 2003111161 A RU2003111161 A RU 2003111161A RU 2003111161 A RU2003111161 A RU 2003111161A
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- Prior art keywords
- methane
- membrane
- partial oxidation
- catalyst
- partial
- Prior art date
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims 34
- 239000012528 membrane Substances 0.000 title claims 15
- 230000003647 oxidation Effects 0.000 title claims 12
- 238000007254 oxidation reaction Methods 0.000 title claims 12
- 239000000919 ceramic Substances 0.000 title claims 7
- 238000000034 method Methods 0.000 title claims 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims 3
- 229910052760 oxygen Inorganic materials 0.000 title claims 3
- 239000001301 oxygen Substances 0.000 title claims 3
- 230000035699 permeability Effects 0.000 title claims 2
- 239000003054 catalyst Substances 0.000 claims 9
- 239000007789 gas Substances 0.000 claims 6
- 229910000510 noble metal Inorganic materials 0.000 claims 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims 2
- 239000000843 powder Substances 0.000 claims 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 239000003245 coal Substances 0.000 claims 1
- 239000003034 coal gas Substances 0.000 claims 1
- 239000000571 coke Substances 0.000 claims 1
- 229910052751 metal Inorganic materials 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 239000003345 natural gas Substances 0.000 claims 1
- 239000003960 organic solvent Substances 0.000 claims 1
- 229910052697 platinum Inorganic materials 0.000 claims 1
- 238000000197 pyrolysis Methods 0.000 claims 1
- 239000002994 raw material Substances 0.000 claims 1
- 229910052703 rhodium Inorganic materials 0.000 claims 1
- 239000010948 rhodium Substances 0.000 claims 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims 1
- 229910052707 ruthenium Inorganic materials 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
Classifications
-
- 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
- C01B3/386—Catalytic partial combustion
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8933—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/8946—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali or alkaline earth metals
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
- B01J35/59—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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/024—Multiple impregnation or coating
- B01J37/0248—Coatings comprising impregnated particles
-
- 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
-
- 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
- C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
- C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
-
- 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
-
- 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
- C01B2203/1064—Platinum group metal 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
-
- 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
- C01B2203/1258—Pre-treatment of the feed
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0046—Nitrogen
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- General Health & Medical Sciences (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Catalysts (AREA)
Claims (6)
1. Способ частичного окисления метана с использованием мембранного реактора, в котором воздух приводят в контакт с одной стороны плотной керамической мембраны с селективной проницаемостью для кислорода, и газовое сырье, которое содержит метан в качестве основного компонента, подают в контакт с другой стороны мембраны таким образом, чтобы провести частичное окисление метана с помощью кислорода, который селективно проходит через керамическую мембрану со стороны воздуха на сторону метана, отличающийся тем, что катализатор частичного окисления метана размещают при двухмерной схеме расположения контакта с указанной мембраной в верхней части сырьевого газового потока и катализатор частичного окисления метана размещают при трехмерной схеме расположения контакта с указанной мембраной в нижней части потока.
2. Способ частичного окисления метана с использованием мембранного реактора по п.1, в котором указанное газовое сырье представляет собой природный газ, газ угольного месторождения, газ от пиролиза угля и/или газ коксовой печи, который содержит метан.
3. Способ частичного окисления метана с использованием мембранного реактора по п.1, где в качестве средства размещения катализатора частичного окисления метана на основе Ni или благородного металла, такого как Ru, на керамической мембране при двухмерной схеме расположения контакта, используют суспензию, полученную из тонкодисперсного порошка катализатора, включающего носитель, который смешивают с органическим растворителем, наносят на керамическую мембрану, которую затем обжигают для спекания катализатора.
4. Способ частичного окисления метана с использованием мембранного реактора по п.1, где в качестве средства размещения катализатора частичного окисления метана на основе Ni или благородного металла, такого как Ru, на керамической мембране при трехмерной схеме расположения контакта, пространство подвода потока в реакторе заполняют порошком катализатора, включающим носитель, в частичном контакте с керамической мембраной.
5. Способ частичного окисления метана по п.3 или 4, где используемый катализатор частичного окисления металла на основе Ni имеет состав, представленный Nix/CaySr1-yTiO3 (х=от 0,1 до 0,3, у=0,8 или 0,0) или Nix/BaTiO3 (х=от 0,1 до 0,3), с рутением, платиной или родием, нанесенными на него в соотношении от 0,1 до 1000 млн-1 по весу указанного катализатора.
6. Способ частичного окисления метана с использованием мембранного реактора по п.1, где пар смешивают в потоке газового сырья, которое содержит метан в качестве основного компонента, при соотношении от 0,25 до 0,5 пара к количеству содержащегося углерода.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000-284647 | 2000-09-20 | ||
| JP2000284647 | 2000-09-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| RU2003111161A true RU2003111161A (ru) | 2004-08-27 |
Family
ID=18768824
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2003111161/15A RU2003111161A (ru) | 2000-09-20 | 2001-09-17 | Способ частичного окисления метана с использованием плотной керамической мембраны с селективной проницаемостью для кислорода |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US7105147B2 (ru) |
| EP (1) | EP1333009A4 (ru) |
| JP (1) | JP4953546B2 (ru) |
| CN (1) | CN1461282A (ru) |
| AU (1) | AU2001286258A1 (ru) |
| CA (1) | CA2422567A1 (ru) |
| NO (1) | NO20031264L (ru) |
| RU (1) | RU2003111161A (ru) |
| WO (1) | WO2002024571A1 (ru) |
| ZA (1) | ZA200303049B (ru) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008077200A1 (fr) * | 2006-12-27 | 2008-07-03 | Milford Group Ventures Limited | Procédé pour augmenter de rendement d'une formation pétrolière productrice |
Families Citing this family (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4916173B2 (ja) * | 2003-12-17 | 2012-04-11 | ダイハツ工業株式会社 | 排ガス浄化用触媒組成物 |
| US7419648B2 (en) * | 2004-07-16 | 2008-09-02 | Shell Oil Company | Process for the production of hydrogen and carbon dioxide |
| EP1795260A1 (fr) * | 2005-12-07 | 2007-06-13 | L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Catalyseur constitué d'un support solide, d'un oxyde, et d'une phase active métallique greffée sur l'oxyde, procédé pour sa préparation et application |
| CN100438978C (zh) * | 2006-12-20 | 2008-12-03 | 中国科学院山西煤炭化学研究所 | 一种天然气部分氧化制备合成气的催化剂及其制备方法 |
| JP2009062258A (ja) * | 2007-03-27 | 2009-03-26 | Tdk Corp | 燃料改質モジュール及び水素発生装置 |
| US20080260631A1 (en) | 2007-04-18 | 2008-10-23 | H2Gen Innovations, Inc. | Hydrogen production process |
| GB201000156D0 (en) * | 2010-01-07 | 2010-02-24 | Gas2 Ltd | Isothermal reactor for partial oxidisation of methane |
| EP2374526A1 (en) | 2010-03-29 | 2011-10-12 | Centre National de la Recherche Scientifique (C.N.R.S) | Solid composite membrane exhibiting both oxygen conductivity and a substrate catalyst interface |
| CN102424360A (zh) * | 2011-09-13 | 2012-04-25 | 昆明理工大学 | 一种载氧膜连续催化甲烷制合成气的方法 |
| WO2013106771A2 (en) | 2012-01-13 | 2013-07-18 | Siluria Technologies, Inc. | Process for separating hydrocarbon compounds |
| US9670113B2 (en) | 2012-07-09 | 2017-06-06 | Siluria Technologies, Inc. | Natural gas processing and systems |
| CN102744060B (zh) * | 2012-07-23 | 2014-02-19 | 福州大学 | 一种BaTiO3 负载钌氨合成催化剂及其制备方法 |
| AU2013355038B2 (en) | 2012-12-07 | 2017-11-02 | Lummus Technology Llc | Integrated processes and systems for conversion of methane to multiple higher hydrocarbon products |
| EP3074119B1 (en) | 2013-11-27 | 2019-01-09 | Siluria Technologies, Inc. | Reactors and systems for oxidative coupling of methane |
| CN110655437B (zh) | 2014-01-08 | 2022-09-09 | 鲁玛斯技术有限责任公司 | 乙烯成液体的系统和方法 |
| US10377682B2 (en) | 2014-01-09 | 2019-08-13 | Siluria Technologies, Inc. | Reactors and systems for oxidative coupling of methane |
| CA3225180A1 (en) | 2014-01-09 | 2015-07-16 | Lummus Technology Llc | Oxidative coupling of methane implementations for olefin production |
| US9334204B1 (en) | 2015-03-17 | 2016-05-10 | Siluria Technologies, Inc. | Efficient oxidative coupling of methane processes and systems |
| US10793490B2 (en) | 2015-03-17 | 2020-10-06 | Lummus Technology Llc | Oxidative coupling of methane methods and systems |
| US20160289143A1 (en) | 2015-04-01 | 2016-10-06 | Siluria Technologies, Inc. | Advanced oxidative coupling of methane |
| US9328297B1 (en) | 2015-06-16 | 2016-05-03 | Siluria Technologies, Inc. | Ethylene-to-liquids systems and methods |
| WO2017065947A1 (en) | 2015-10-16 | 2017-04-20 | Siluria Technologies, Inc. | Separation methods and systems for oxidative coupling of methane |
| US9944573B2 (en) | 2016-04-13 | 2018-04-17 | Siluria Technologies, Inc. | Oxidative coupling of methane for olefin production |
| US10539324B2 (en) * | 2016-06-09 | 2020-01-21 | King Fahd University Of Petroleum And Minerals | System for combusting a methane stream and a method of combustion |
| CN107537499B (zh) * | 2016-06-29 | 2020-06-09 | 中国石油化工股份有限公司 | 多孔陶瓷负载镍基费托催化剂及其使用方法 |
| US20180169561A1 (en) | 2016-12-19 | 2018-06-21 | Siluria Technologies, Inc. | Methods and systems for performing chemical separations |
| PL3630707T3 (pl) | 2017-05-23 | 2024-02-19 | Lummus Technology Llc | Zintegrowanie sposobów utleniającego sprzęgania metanu |
| EP3649097A4 (en) | 2017-07-07 | 2021-03-24 | Lummus Technology LLC | SYSTEMS AND PROCESSES FOR THE OXIDATIVE COUPLING OF METHANE |
Family Cites Families (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5306411A (en) * | 1989-05-25 | 1994-04-26 | The Standard Oil Company | Solid multi-component membranes, electrochemical reactor components, electrochemical reactors and use of membranes, reactor components, and reactor for oxidation reactions |
| US5360635A (en) | 1992-01-02 | 1994-11-01 | Air Products And Chemicals, Inc. | Method for manufacturing inorganic membranes by organometallic chemical vapor deposition |
| US6033632A (en) * | 1993-12-08 | 2000-03-07 | Eltron Research, Inc. | Solid state oxygen anion and electron mediating membrane and catalytic membrane reactors containing them |
| US6355093B1 (en) * | 1993-12-08 | 2002-03-12 | Eltron Research, Inc | Two component-three dimensional catalysis |
| US5725218A (en) * | 1996-11-15 | 1998-03-10 | The University Of Chicago | High temperature seal for joining ceramics and metal alloys |
| US5846641A (en) | 1997-03-20 | 1998-12-08 | Exxon Research And Engineering Company | Multi-layer membrane composites and their use in hydrocarbon partical oxidation |
| US5980840A (en) | 1997-04-25 | 1999-11-09 | Bp Amoco Corporation | Autothermic reactor and process using oxygen ion--conducting dense ceramic membrane |
| US5820654A (en) | 1997-04-29 | 1998-10-13 | Praxair Technology, Inc. | Integrated solid electrolyte ionic conductor separator-cooler |
| US6077323A (en) | 1997-06-06 | 2000-06-20 | Air Products And Chemicals, Inc. | Synthesis gas production by ion transport membranes |
| US5935533A (en) | 1997-10-28 | 1999-08-10 | Bp Amoco Corporation | Membrane reactor hollow tube module with ceramic/metal interfacial zone |
| ES2207785T3 (es) | 1997-12-23 | 2004-06-01 | Air Products And Chemicals, Inc. | Utilizacion de gas de sintesis producido con membranas mixtas conductoras. |
| JP4335356B2 (ja) | 1998-04-14 | 2009-09-30 | 石油資源開発株式会社 | リホーミング用ニッケル系触媒およびこれを用いた合成ガスの製法 |
| US6010614A (en) * | 1998-06-03 | 2000-01-04 | Praxair Technology, Inc. | Temperature control in a ceramic membrane reactor |
| US6153163A (en) | 1998-06-03 | 2000-11-28 | Praxair Technology, Inc. | Ceramic membrane reformer |
| US6139810A (en) | 1998-06-03 | 2000-10-31 | Praxair Technology, Inc. | Tube and shell reactor with oxygen selective ion transport ceramic reaction tubes |
| CN1190356C (zh) * | 1998-07-02 | 2005-02-23 | 霍尔多·托普瑟公司 | 烃原料的自热转化方法 |
| US6458334B1 (en) * | 2000-03-02 | 2002-10-01 | The Boc Group, Inc. | Catalytic partial oxidation of hydrocarbons |
| US6733692B2 (en) * | 2000-04-20 | 2004-05-11 | Conocophillips Company | Rhodium foam catalyst for the partial oxidation of hydrocarbons |
-
2001
- 2001-09-17 RU RU2003111161/15A patent/RU2003111161A/ru not_active Application Discontinuation
- 2001-09-17 WO PCT/JP2001/008036 patent/WO2002024571A1/ja active Application Filing
- 2001-09-17 US US10/363,699 patent/US7105147B2/en not_active Expired - Fee Related
- 2001-09-17 CN CN01815998A patent/CN1461282A/zh active Pending
- 2001-09-17 JP JP2002528594A patent/JP4953546B2/ja not_active Expired - Fee Related
- 2001-09-17 CA CA002422567A patent/CA2422567A1/en not_active Abandoned
- 2001-09-17 EP EP01965672A patent/EP1333009A4/en not_active Ceased
- 2001-09-17 AU AU2001286258A patent/AU2001286258A1/en not_active Abandoned
-
2003
- 2003-03-19 NO NO20031264A patent/NO20031264L/no not_active Application Discontinuation
- 2003-09-17 ZA ZA200303049A patent/ZA200303049B/en unknown
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008077200A1 (fr) * | 2006-12-27 | 2008-07-03 | Milford Group Ventures Limited | Procédé pour augmenter de rendement d'une formation pétrolière productrice |
| EA012979B1 (ru) * | 2006-12-27 | 2010-02-26 | Милфорд Груп Венчурс Лимитед | Способ повышения нефтеотдачи продуктивного пласта |
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| Publication number | Publication date |
|---|---|
| WO2002024571A1 (fr) | 2002-03-28 |
| JP4953546B2 (ja) | 2012-06-13 |
| AU2001286258A1 (en) | 2002-04-02 |
| EP1333009A1 (en) | 2003-08-06 |
| US20040101472A1 (en) | 2004-05-27 |
| NO20031264D0 (no) | 2003-03-19 |
| ZA200303049B (en) | 2004-04-19 |
| CN1461282A (zh) | 2003-12-10 |
| CA2422567A1 (en) | 2003-03-18 |
| JPWO2002024571A1 (ja) | 2004-01-29 |
| EP1333009A4 (en) | 2004-08-04 |
| NO20031264L (no) | 2003-05-19 |
| US7105147B2 (en) | 2006-09-12 |
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