EA200501523A1 - Способ переработки природного газа в жидкие продукты - Google Patents
Способ переработки природного газа в жидкие продуктыInfo
- Publication number
- EA200501523A1 EA200501523A1 EA200501523A EA200501523A EA200501523A1 EA 200501523 A1 EA200501523 A1 EA 200501523A1 EA 200501523 A EA200501523 A EA 200501523A EA 200501523 A EA200501523 A EA 200501523A EA 200501523 A1 EA200501523 A1 EA 200501523A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- sub
- natural gas
- liquid products
- processing natural
- gtl
- Prior art date
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title abstract 4
- 238000000034 method Methods 0.000 title abstract 2
- 239000003345 natural gas Substances 0.000 title abstract 2
- 239000012263 liquid product Substances 0.000 title 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract 4
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0233—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 1 carbon atom or more
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- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
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- 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
- C01B3/48—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 followed by reaction of water vapour with carbon monoxide
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
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- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
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- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
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- F25J1/0032—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
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- F25J1/0228—Coupling of the liquefaction unit to other units or processes, so-called integrated processes
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- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
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- Fats And Perfumes (AREA)
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Abstract
Представлен интегрированный способ производства СПГ и СУ продуктов, в котором поток природного газа, содержащий CO, питающий производственную зону СПГ, вначале предварительно обрабатывается для выделения из него по крайней мере части CO, а полученный в результате поток CO, направляется затем в производственную зону СУ и используется для производства СУ продуктов, которые включают метанол и/или другие производные метанола.Отчет о международном поиске был опубликован 2004.11.25.
Applications Claiming Priority (3)
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US45800503P | 2003-03-27 | 2003-03-27 | |
US10/805,982 US7168265B2 (en) | 2003-03-27 | 2004-03-22 | Integrated processing of natural gas into liquid products |
PCT/US2004/008779 WO2004088225A2 (en) | 2003-03-27 | 2004-03-23 | Integrated processing of natural gas into liquid products |
Publications (2)
Publication Number | Publication Date |
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EA200501523A1 true EA200501523A1 (ru) | 2006-02-24 |
EA008240B1 EA008240B1 (ru) | 2007-04-27 |
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EA200501523A EA008240B1 (ru) | 2003-03-27 | 2004-03-23 | Способ переработки природного газа в жидкие продукты |
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US (1) | US7168265B2 (ru) |
EP (1) | EP1608924B1 (ru) |
AT (1) | ATE362086T1 (ru) |
AU (1) | AU2004225585B2 (ru) |
CA (1) | CA2519118C (ru) |
DE (1) | DE602004006397T2 (ru) |
EA (1) | EA008240B1 (ru) |
EG (1) | EG24329A (ru) |
ES (1) | ES2284038T3 (ru) |
MX (1) | MXPA05010204A (ru) |
NO (1) | NO338860B1 (ru) |
WO (1) | WO2004088225A2 (ru) |
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FR2893627B1 (fr) * | 2005-11-18 | 2007-12-28 | Total Sa | Procede pour l'ajustement du pouvoir calorifique superieur du gaz dans la chaine du gnl. |
US7437889B2 (en) * | 2006-01-11 | 2008-10-21 | Air Products And Chemicals, Inc. | Method and apparatus for producing products from natural gas including helium and liquefied natural gas |
US20090151391A1 (en) * | 2007-12-12 | 2009-06-18 | Conocophillips Company | Lng facility employing a heavies enriching stream |
JP5424566B2 (ja) * | 2008-03-14 | 2014-02-26 | 独立行政法人石油天然ガス・金属鉱物資源機構 | 天然ガスからの液状炭化水素製造プロセスにおける合成ガスの製造方法 |
WO2011059567A1 (en) | 2009-11-12 | 2011-05-19 | Exxonmobil Upstream Research Company | Low emission power generation and hydrocarbon recovery systems and methods |
EP2276559A4 (en) * | 2008-03-28 | 2017-10-18 | Exxonmobil Upstream Research Company | Low emission power generation and hydrocarbon recovery systems and methods |
EP2268897B1 (en) | 2008-03-28 | 2020-11-11 | Exxonmobil Upstream Research Company | Low emission power generation and hydrocarbon recovery system and method |
JP5424569B2 (ja) * | 2008-03-31 | 2014-02-26 | 独立行政法人石油天然ガス・金属鉱物資源機構 | 天然ガスからの液状炭化水素製造プロセスにおける合成ガスの製造方法 |
GB0812699D0 (en) * | 2008-07-11 | 2008-08-20 | Johnson Matthey Plc | Apparatus and process for treating offshore natural gas |
WO2010042266A1 (en) * | 2008-10-07 | 2010-04-15 | Exxonmobil Upstream Research Company | Helium recovery from natural gas integrated with ngl recovery |
CA2737133C (en) | 2008-10-14 | 2017-01-31 | Exxonmobil Upstream Research Company | Methods and systems for controlling the products of combustion |
US9683703B2 (en) * | 2009-08-18 | 2017-06-20 | Charles Edward Matar | Method of storing and transporting light gases |
CN102781819A (zh) * | 2010-03-02 | 2012-11-14 | 独立行政法人石油天然气·金属矿物资源机构 | 合成气体的制造方法 |
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US8454727B2 (en) | 2010-05-28 | 2013-06-04 | Uop Llc | Treatment of natural gas feeds |
US8282707B2 (en) | 2010-06-30 | 2012-10-09 | Uop Llc | Natural gas purification system |
JP5759543B2 (ja) | 2010-07-02 | 2015-08-05 | エクソンモービル アップストリーム リサーチ カンパニー | 排ガス再循環方式及び直接接触型冷却器による化学量論的燃焼 |
US9732675B2 (en) | 2010-07-02 | 2017-08-15 | Exxonmobil Upstream Research Company | Low emission power generation systems and methods |
EA029301B1 (ru) | 2010-07-02 | 2018-03-30 | Эксонмобил Апстрим Рисерч Компани | Интегрированные системы для получения со(варианты) и способ производства электроэнергии |
MY160833A (en) | 2010-07-02 | 2017-03-31 | Exxonmobil Upstream Res Co | Stoichiometric combustion of enriched air with exhaust gas recirculation |
CA2805271A1 (en) * | 2010-07-21 | 2012-01-26 | Synfuels International, Inc. | Methods and systems for storing and transporting gases |
US9115324B2 (en) | 2011-02-10 | 2015-08-25 | Expander Energy Inc. | Enhancement of Fischer-Tropsch process for hydrocarbon fuel formulation |
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EP1608924A2 (en) | 2005-12-28 |
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MXPA05010204A (es) | 2006-02-03 |
US20040248999A1 (en) | 2004-12-09 |
US7168265B2 (en) | 2007-01-30 |
AU2004225585B2 (en) | 2010-02-18 |
ES2284038T3 (es) | 2007-11-01 |
WO2004088225A2 (en) | 2004-10-14 |
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