RU2003128598A - Способ и устройство для получения синтез-газа - Google Patents
Способ и устройство для получения синтез-газа Download PDFInfo
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- RU2003128598A RU2003128598A RU2003128598/15A RU2003128598A RU2003128598A RU 2003128598 A RU2003128598 A RU 2003128598A RU 2003128598/15 A RU2003128598/15 A RU 2003128598/15A RU 2003128598 A RU2003128598 A RU 2003128598A RU 2003128598 A RU2003128598 A RU 2003128598A
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- Prior art keywords
- reforming
- heated
- reforming unit
- catalyst
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- 238000000034 method Methods 0.000 title claims 9
- 230000015572 biosynthetic process Effects 0.000 title claims 3
- 238000003786 synthesis reaction Methods 0.000 title claims 3
- 238000002407 reforming Methods 0.000 claims 15
- 239000003054 catalyst Substances 0.000 claims 10
- 238000006243 chemical reaction Methods 0.000 claims 8
- 239000007789 gas Substances 0.000 claims 7
- 238000000629 steam reforming Methods 0.000 claims 7
- 239000000203 mixture Substances 0.000 claims 6
- 239000002912 waste gas Substances 0.000 claims 6
- 239000002918 waste heat Substances 0.000 claims 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 6
- 239000004215 Carbon black (E152) Substances 0.000 claims 5
- 229930195733 hydrocarbon Natural products 0.000 claims 5
- 150000002430 hydrocarbons Chemical class 0.000 claims 5
- 238000010438 heat treatment Methods 0.000 claims 4
- 239000007787 solid Substances 0.000 claims 4
- 230000003197 catalytic effect Effects 0.000 claims 3
- 239000008187 granular material Substances 0.000 claims 3
- 239000011541 reaction mixture Substances 0.000 claims 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 2
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 1
- 239000001569 carbon dioxide Substances 0.000 claims 1
- 238000001833 catalytic reforming Methods 0.000 claims 1
- 239000011949 solid catalyst Substances 0.000 claims 1
- 239000002699 waste material Substances 0.000 claims 1
Classifications
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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
- C01B3/382—Multi-step processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/08—Production of synthetic natural gas
-
- 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
- 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
- C01B2203/08—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
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1005—Arrangement or shape of catalyst
- C01B2203/1011—Packed bed of catalytic structures, e.g. particles, packing elements
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1005—Arrangement or shape of catalyst
- C01B2203/1035—Catalyst coated on equipment surfaces, e.g. reactor walls
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Claims (9)
1. Способ получения синтез-газа каталитическим реформингом с водяным паром и/или CO2 углеводородного сырья, включающий следующие стадии:
(а) нагревание реакционной смеси углеводорода и водяного пара и/или CO2 в нагретой водяным паром реформинг-установке, объединенной с секцией отходящего газа, содержащего бросовое тепло, трубчатой реформинг-установки с огневым обогревом, в которой происходит реформинг реакционной смеси при контакте с твердым катализатором реформинга,
(б) подача частично подвергнутой реформингу с водяным паром смеси в трубчатую реформинг-установку с огневым обогревом и затем реформинг этой смеси до желаемых состава и температуры, при этом реформинг-установка с нагретым водяным паром включает трубную систему, содержащую реакционные секции с твердым катализатором реформинга, включающим гранулы катализатора и/или каталитические структурированные элементы, причем трубная система является частью трубной системы для перерабатываемого газа, объединенной с секцией отходящего газа, содержащего бросовое тепло.
2. Способ по п.1, где реформинг-установка с нагретым водяным паром включает секции нагрева с твердым катализатором реформинга или без него и адиабатические реакционные секции, содержащие каталитические структурированные элементы, покрытые слоем катализатора реформинга с водяным паром, причем обе секции являются частью трубной системы для перерабатываемого газа, объединенной с секцией отходящего газа, содержащего бросовое тепло.
3. Способ по п.1, где реформинг-установка с нагретым водяным паром включает нагреваемые реакционные секции с гранулами катализатора, причем нагреваемые секции являются частью трубной системы для перерабатываемого газа, объединенной с секцией отходящего газа, содержащего бросовое тепло.
4. Способ по п.2 или 3, где реакционную смесь углеводорода и водяного пара и/или CO2 подвергают предварительному реформингу перед стадией нагревания (а).
5. Способ по пп.1, 2 или 3, где структурированный элемент представляет собой монолит или складчатую структуру.
6. Способ по п.2, где водяной пар и/или диоксид углерода добавляют в адиабатические реакционные секции.
7. Способ по пп.1, 2, 3 или 4, где реакционные секции также содержат катализатор реформинга с водяным паром, прикрепленный к стенке
трубы, или катализатор, прикрепленный к структурам, прикрепленным к стенке трубы.
8. Устройство для получения синтез-газа по п.1, включающее следующее:
(а) установку адиабатического предварительного реформинга для необязательного предварительного реформинга смеси углеводорода и водяного пара и/или СО2,
(б) трубчатую реформинг-установку с огневым обогревом с секцией отходящего газа, содержащего бросовое тепло, для нагревания смеси углеводорода и водяного пара и/или CO2 или смеси, подвергнутой предварительному реформингу,
(в) реформинг-установку с нагретым водяным паром, объединенную с секцией отходящего газа, содержащего бросовое тепло, трубчатой реформинг-установки с огневым обогревом, где реформинг-установка с нагретым водяным паром включает трубную систему, содержащую реакционные секции с твердым катализатором реформинга, включающим гранулы катализатора и/или каталитические структурированные элементы, причем трубная система является частью трубной системы для перерабатываемого газа, объединенной с секцией отходящего газа, содержащего бросовое тепло.
9. Устройство по п.8, где твердый катализатор помещают в нагреваемые реакционные секции и/или в адиабатические реакционные секции реформинг-установки с нагретым водяным паром.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DKPA200201431 | 2002-09-26 | ||
| DKPA200201431 | 2002-09-26 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| RU2003128598A true RU2003128598A (ru) | 2005-03-27 |
| RU2354608C2 RU2354608C2 (ru) | 2009-05-10 |
Family
ID=29414638
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2003128598/04A RU2354608C2 (ru) | 2002-09-26 | 2003-09-25 | Способ и устройство для получения синтез-газа |
Country Status (11)
| Country | Link |
|---|---|
| US (2) | US7094363B2 (ru) |
| EP (1) | EP1403215B1 (ru) |
| JP (1) | JP4959105B2 (ru) |
| KR (1) | KR101044621B1 (ru) |
| CN (1) | CN1328153C (ru) |
| AU (1) | AU2003248394B2 (ru) |
| CA (1) | CA2442493C (ru) |
| ES (1) | ES2405587T3 (ru) |
| NO (1) | NO336969B1 (ru) |
| RU (1) | RU2354608C2 (ru) |
| ZA (1) | ZA200307449B (ru) |
Families Citing this family (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8177868B2 (en) | 2002-01-04 | 2012-05-15 | Meggitt (Uk) Limited | Reforming apparatus and method |
| US7967878B2 (en) | 2002-01-04 | 2011-06-28 | Meggitt (Uk) Limited | Reformer apparatus and method |
| US7377951B2 (en) * | 2005-04-15 | 2008-05-27 | Air Products And Chemicals, Inc. | Process to utilize low-temperature waste heat for the preparation of synthesis gas |
| US7504048B2 (en) * | 2005-06-14 | 2009-03-17 | Air Products And Chemicals, Inc. | Axial convective reformer |
| ATE549305T1 (de) * | 2006-01-23 | 2012-03-15 | Saudi Basic Ind Corp Inc | Verfahren zur herstellung von ethylen aus naturgas mit wärmeintegration |
| US7740751B2 (en) | 2006-11-09 | 2010-06-22 | Uop Llc | Process for heating a stream for a hydrocarbon conversion process |
| US20080110801A1 (en) * | 2006-11-09 | 2008-05-15 | Leon Yuan | Process For Heating A Hydrocarbon Stream Entering A Reaction Zone With A Heater Convection Section |
| US7501078B2 (en) | 2007-01-10 | 2009-03-10 | Air Products And Chemicals, Inc. | Process for generating synthesis gas using catalyzed structured packing |
| US7862633B2 (en) * | 2007-04-13 | 2011-01-04 | Battelle Memorial Institute | Method and system for introducing fuel oil into a steam reformer with reduced carbon deposition |
| US20080260631A1 (en) | 2007-04-18 | 2008-10-23 | H2Gen Innovations, Inc. | Hydrogen production process |
| US7906559B2 (en) * | 2007-06-21 | 2011-03-15 | University Of Southern California | Conversion of carbon dioxide to methanol and/or dimethyl ether using bi-reforming of methane or natural gas |
| US7790059B2 (en) * | 2007-10-18 | 2010-09-07 | Air Products And Chemicals, Inc. | Staged hydrocarbon/steam reformer apparatus and method |
| US8282814B2 (en) * | 2009-03-31 | 2012-10-09 | Uop Llc | Fired heater for a hydrocarbon conversion process |
| EP2419375B1 (en) * | 2009-04-15 | 2016-04-06 | Air Products and Chemicals, Inc. | Process for producing a hydrogen-containing product gas |
| WO2012112065A1 (ru) | 2011-02-18 | 2012-08-23 | "Крено Инвест Са" | Способ и устройство для получения синтез - газа |
| DE102012019382A1 (de) * | 2012-10-02 | 2014-04-03 | Linde Aktiengesellschaft | Anlage und Verfahren zur Herstellung von Synthesegas |
| RU2736976C2 (ru) | 2016-06-10 | 2020-11-23 | Хальдор Топсёэ А/С | Получение со-обогащенного синтез-газа |
| US10537867B2 (en) | 2018-01-04 | 2020-01-21 | Chevron Phillips Chemical Company Lp | Optimized reactor configuration for optimal performance of the aromax catalyst for aromatics synthesis |
| US10633603B2 (en) | 2018-01-04 | 2020-04-28 | Chevron Phillips Chemical Company Lp | Optimized reactor configuration for optimal performance of the aromax catalyst for aromatics synthesis |
| RU2677142C1 (ru) * | 2018-05-04 | 2019-01-15 | Андрей Владиславович Курочкин | Устройство нагрева реакционной зоны каталитического реактора |
| RU2677146C1 (ru) * | 2018-05-04 | 2019-01-15 | Андрей Владиславович Курочкин | Установка для получения синтез-газа с каталитическим нагревателем |
| GB201813431D0 (en) | 2018-08-17 | 2018-10-03 | Weedon Geoffrey Gerald | Process & apparatus for steam reforming |
| CN119947980A (zh) | 2022-10-03 | 2025-05-06 | 埃克森美孚技术与工程公司 | 高温逆流反应器中的氢气生成 |
| WO2024196340A1 (en) * | 2023-03-17 | 2024-09-26 | Jbk Extractions Llc | Systems and methods for making syngas |
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| RU2047354C1 (ru) * | 1992-07-08 | 1995-11-10 | Остроушко Александр Александрович | Способ изготовления катализатора |
| DK169614B1 (da) | 1992-08-13 | 1994-12-27 | Topsoe Haldor As | Fremgangsmåde og reaktor til fremstilling af hydrogen- og carbonmonoxidrige gasser |
| FR2696168B1 (fr) * | 1992-09-25 | 1994-12-09 | Inst Francais Du Petrole | Procédé et dispositif de fabrication de gaz de synthèse et utilisation associée. |
| MY131526A (en) * | 1993-12-27 | 2007-08-30 | Shell Int Research | A process for the preparation of carbon monoxide and/or hydrogen |
| DE19503082A1 (de) * | 1995-02-01 | 1996-08-08 | Univ Ludwigs Albert | Gegenstand und Verfahren zur bevorzugt transienten Expression und möglichen Translation spezifischer RNA im cytoplasmatischen Bereich höherer eukaryontischer Zellen |
| DE19534433C1 (de) | 1995-09-16 | 1996-10-10 | Daimler Benz Ag | Katalysatorschichtstruktur für einen Methanolreformierungsreaktor und Verfahren zu ihrer Herstellung |
| EP0855366B1 (en) * | 1997-01-22 | 2001-05-02 | Haldor Topsoe A/S | Synthesis gas production by steam reforming using catalyzed hardware |
| US6048472A (en) * | 1997-12-23 | 2000-04-11 | Air Products And Chemicals, Inc. | Production of synthesis gas by mixed conducting membranes |
| DK173496B1 (da) | 1998-07-16 | 2001-01-02 | Topsoe Haldor As | Fremgangsmåde til fremstilling af syntesegas ved vanddampreformering under anvendelse af en katalyseret metaloverflade |
| GB9817526D0 (en) | 1998-08-13 | 1998-10-07 | Ici Plc | Steam reforming |
| DK173897B1 (da) * | 1998-09-25 | 2002-02-04 | Topsoe Haldor As | Fremgangsmåde til autotermisk reforming af et carbonhydridfødemateriale indeholdende højere carbonhydrider |
| US6277894B1 (en) | 1999-03-30 | 2001-08-21 | Syntroleum Corporation | System and method for converting light hydrocarbons into heavier hydrocarbons with a plurality of synthesis gas subsystems |
| ES2375102T3 (es) * | 1999-07-15 | 2012-02-24 | Haldor Topsoe A/S | Procedimiento para el reformado con vapor catalítico de un material de alimentación hidrocarbonado. |
| US20010051662A1 (en) * | 2000-02-15 | 2001-12-13 | Arcuri Kym B. | System and method for preparing a synthesis gas stream and converting hydrocarbons |
| US6444712B1 (en) * | 2000-09-28 | 2002-09-03 | Exxonmobil Chemical Patents, Inc. | Methanol, olefin, and hydrocarbon synthesis process |
| US20020165417A1 (en) | 2001-03-14 | 2002-11-07 | Toyo Engineering Corporation | Process for producing synthesis gas |
| RU2196761C2 (ru) * | 2001-05-03 | 2003-01-20 | Институт нефтехимического синтеза им. А.В.Топчиева РАН | Способ получения бензина из углеводородного газового сырья |
-
2003
- 2003-09-11 EP EP03020672A patent/EP1403215B1/en not_active Expired - Lifetime
- 2003-09-11 ES ES03020672T patent/ES2405587T3/es not_active Expired - Lifetime
- 2003-09-24 US US10/668,295 patent/US7094363B2/en not_active Expired - Lifetime
- 2003-09-25 CA CA2442493A patent/CA2442493C/en not_active Expired - Fee Related
- 2003-09-25 JP JP2003334056A patent/JP4959105B2/ja not_active Expired - Fee Related
- 2003-09-25 NO NO20034283A patent/NO336969B1/no not_active IP Right Cessation
- 2003-09-25 AU AU2003248394A patent/AU2003248394B2/en not_active Ceased
- 2003-09-25 RU RU2003128598/04A patent/RU2354608C2/ru active
- 2003-09-25 ZA ZA200307449A patent/ZA200307449B/xx unknown
- 2003-09-26 CN CNB031648223A patent/CN1328153C/zh not_active Expired - Fee Related
- 2003-09-26 KR KR1020030066966A patent/KR101044621B1/ko not_active Expired - Lifetime
-
2006
- 2006-02-23 US US11/359,466 patent/US7547332B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| RU2354608C2 (ru) | 2009-05-10 |
| NO336969B1 (no) | 2015-12-07 |
| AU2003248394B2 (en) | 2010-03-11 |
| CN1328153C (zh) | 2007-07-25 |
| AU2003248394A1 (en) | 2004-04-22 |
| NO20034283D0 (no) | 2003-09-25 |
| CA2442493A1 (en) | 2004-03-26 |
| NO20034283L (no) | 2004-03-29 |
| ES2405587T3 (es) | 2013-05-31 |
| US20040065014A1 (en) | 2004-04-08 |
| US7094363B2 (en) | 2006-08-22 |
| ZA200307449B (en) | 2004-07-06 |
| EP1403215B1 (en) | 2013-03-13 |
| EP1403215A1 (en) | 2004-03-31 |
| JP4959105B2 (ja) | 2012-06-20 |
| CN1496956A (zh) | 2004-05-19 |
| KR20040027456A (ko) | 2004-04-01 |
| KR101044621B1 (ko) | 2011-06-29 |
| US20060143984A1 (en) | 2006-07-06 |
| US7547332B2 (en) | 2009-06-16 |
| CA2442493C (en) | 2011-05-03 |
| JP2004269345A (ja) | 2004-09-30 |
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