EA201891476A1 - Способ подавления загрязнения металлами устройства для получения синтез-газа - Google Patents

Способ подавления загрязнения металлами устройства для получения синтез-газа

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Publication number
EA201891476A1
EA201891476A1 EA201891476A EA201891476A EA201891476A1 EA 201891476 A1 EA201891476 A1 EA 201891476A1 EA 201891476 A EA201891476 A EA 201891476A EA 201891476 A EA201891476 A EA 201891476A EA 201891476 A1 EA201891476 A1 EA 201891476A1
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Eurasian Patent Office
Prior art keywords
synthesis gas
carbon dioxide
metal
gas
producing
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EA201891476A
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English (en)
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EA035192B1 (ru
Inventor
Сухеи Вакамацу
Фуюки Яги
Томоюки Микурия
Кенити Кавадзуиси
Original Assignee
Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн
Инпекс Корпорейшн
ДжейЭкс НИППОН ОЙЛ ЭНД ЭНЕРДЖИ КОРПОРЕЙШН
Джапан Петролеум Эксплорейшн Ко., Лтд.
Космо Ойл Ко., Лтд.
Ниппон Стил Энд Сумикин Инджиниринг Ко., Лтд.
Тийода Корпорейшн
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Application filed by Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн, Инпекс Корпорейшн, ДжейЭкс НИППОН ОЙЛ ЭНД ЭНЕРДЖИ КОРПОРЕЙШН, Джапан Петролеум Эксплорейшн Ко., Лтд., Космо Ойл Ко., Лтд., Ниппон Стил Энд Сумикин Инджиниринг Ко., Лтд., Тийода Корпорейшн filed Critical Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн
Publication of EA201891476A1 publication Critical patent/EA201891476A1/ru
Publication of EA035192B1 publication Critical patent/EA035192B1/ru

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    • 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
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    • 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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    • C01B3/52—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquids; Regeneration of used liquids
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    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
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    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/002—Removal of contaminants
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    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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    • 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
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    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

Предотвращают загрязнение металлическими компонентами устройства получения синтез-газа (риформер) для использования в способе получения синтез-газа в процессе GTL ("газ-в-жидкость"). Способ подавления загрязнения металлами устройства получения синтез-газа, функционирующего в процессе GTL, включает в себя стадию получения синтез-газа для получения синтез-газа путем взаимодействия друг с другом природного газа и газа, содержащего пар и/или диоксид углерода, для риформинга в устройстве получения синтез-газа, в котором во время отделения и сбора диоксида углерода, содержащегося в синтез-газе, полученном на стадии получения синтез-газа, и рециркуляции отделенного и собранного диоксида углерода в качестве исходного газа для реакции риформинга на стадию получения синтез-газа концентрация никеля в рециркулированном диоксиде углерода составляет не более чем 0,05 ч./млн.об.
EA201891476A 2011-03-31 2012-03-22 Способ подавления загрязнения металлами устройства для получения синтез-газа EA035192B1 (ru)

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JP2011078808A JP5804747B2 (ja) 2011-03-31 2011-03-31 合成ガス製造装置への金属混入抑制方法

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EA201891476A1 true EA201891476A1 (ru) 2019-03-29
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EA201391434A EA031520B1 (ru) 2011-03-31 2012-03-22 Способ подавления загрязнения металлами устройства для получения синтез-газа

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US (2) US9725656B2 (ru)
EP (1) EP2692690A4 (ru)
JP (1) JP5804747B2 (ru)
CN (1) CN103582610B (ru)
AP (1) AP3483A (ru)
AU (1) AU2012235395B2 (ru)
BR (1) BR112013025187B8 (ru)
CA (1) CA2831561C (ru)
EA (2) EA035192B1 (ru)
MY (1) MY175361A (ru)
WO (1) WO2012132337A1 (ru)
ZA (1) ZA201307218B (ru)

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CA3082774A1 (en) * 2017-11-15 2019-05-23 Gas Technology Institute Processes and systems for reforming of methane and light hydrocarbons to liquid hydrocarbon fuels
US11111142B2 (en) 2018-09-18 2021-09-07 Gas Technology Institute Processes and catalysts for reforming of impure methane-containing feeds

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WO2010038391A1 (ja) * 2008-09-30 2010-04-08 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素合成反応装置及び炭化水素合成反応システム、並びに炭化水素合成方法
JP5301330B2 (ja) * 2009-03-27 2013-09-25 独立行政法人石油天然ガス・金属鉱物資源機構 液体炭化水素の合成方法及び液体炭化水素の合成システム
CN102549111B (zh) 2009-08-31 2015-04-01 日本石油天然气·金属矿物资源机构 烃合成反应装置、烃合成反应系统以及烃合成反应方法

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CA2831561A1 (en) 2012-10-04
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EA035192B1 (ru) 2020-05-12
AU2012235395B2 (en) 2015-04-16
US20140018450A1 (en) 2014-01-16
JP2012214529A (ja) 2012-11-08
AP3483A (en) 2015-12-31
EA031520B1 (ru) 2019-01-31
WO2012132337A1 (ja) 2012-10-04
MY175361A (en) 2020-06-22
US20160272895A1 (en) 2016-09-22
CN103582610A (zh) 2014-02-12
AU2012235395A1 (en) 2013-10-31
EP2692690A1 (en) 2014-02-05
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US9884998B2 (en) 2018-02-06
EP2692690A4 (en) 2014-08-27
US9725656B2 (en) 2017-08-08
AP2013007174A0 (en) 2013-10-31
EA201391434A1 (ru) 2014-01-30
BR112013025187B1 (pt) 2022-03-03

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