RU2008141283A - LIQUID FUEL SYNTHESIS SYSTEM - Google Patents

LIQUID FUEL SYNTHESIS SYSTEM Download PDF

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Publication number
RU2008141283A
RU2008141283A RU2008141283/04A RU2008141283A RU2008141283A RU 2008141283 A RU2008141283 A RU 2008141283A RU 2008141283/04 A RU2008141283/04 A RU 2008141283/04A RU 2008141283 A RU2008141283 A RU 2008141283A RU 2008141283 A RU2008141283 A RU 2008141283A
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RU
Russia
Prior art keywords
quality
processing
liquid hydrocarbons
liquid
gas
Prior art date
Application number
RU2008141283/04A
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Russian (ru)
Other versions
RU2418840C2 (en
Inventor
Ясухиро ОНИСИ (JP)
Ясухиро Ониси
Осаму ВАКАМУРА (JP)
Осаму Вакамура
Кенитиро ФУДЗИМОТО (JP)
Кенитиро ФУДЗИМОТО
Original Assignee
Ниппон Стил Инджиниринг Ко., Лтд. (Jp)
Ниппон Стил Инджиниринг Ко., Лтд.
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Application filed by Ниппон Стил Инджиниринг Ко., Лтд. (Jp), Ниппон Стил Инджиниринг Ко., Лтд. filed Critical Ниппон Стил Инджиниринг Ко., Лтд. (Jp)
Publication of RU2008141283A publication Critical patent/RU2008141283A/en
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Publication of RU2418840C2 publication Critical patent/RU2418840C2/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34—Apparatus, reactors
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • C10G2/344—Apparatus, reactors with moving solid catalysts according to the "fluidised-bed" technique
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing

Abstract

1. Система синтеза жидкого топлива, включающая: ! реформинг-аппарат, который преобразует углеводородный сырьевой материал для получения синтез-газа, содержащего газообразный монооксид углерода и газообразный водород в качестве основных компонентов; ! реактор, который синтезирует жидкие углеводороды из газообразного монооксида углерода и газообразного водорода, содержащихся в синтез-газе; ! устройство для повышающей качество обработки, которое осуществляет заданную повышающую качество обработку жидких углеводородов, синтезированных в реакторе; и ! нагревательное устройство, которое нагревает жидкие углеводороды, вводимые в устройство для повышающей качество обработки, с использованием газа, выводимого из реформинг-аппарата, в качестве источника тепла. ! 2. Система синтеза жидкого топлива по п.1, в которой ! устройство для повышающей качество обработки представляет собой ректификационную колонну, которая производит фракционную разгонку жидких углеводородов на множество видов жидких топлив, имеющих различные температуры кипения, и/или реактор для гидрирования, который производит гидрирование жидких углеводородов. 1. The system of synthesis of liquid fuel, including:! a reforming apparatus that converts a hydrocarbon raw material to produce synthesis gas containing carbon monoxide gas and hydrogen gas as main components; ! a reactor that synthesizes liquid hydrocarbons from gaseous carbon monoxide and gaseous hydrogen contained in the synthesis gas; ! a device for improving the quality of processing, which performs the specified improving the quality of the processing of liquid hydrocarbons synthesized in the reactor; and! a heating device that heats the liquid hydrocarbons introduced into the device to improve the quality of processing, using gas removed from the reforming apparatus as a heat source. ! 2. The system for the synthesis of liquid fuel according to claim 1, in which! a device for improving the quality of processing is a distillation column, which produces fractional distillation of liquid hydrocarbons into many types of liquid fuels having different boiling points, and / or a hydrogenation reactor that produces hydrogenation of liquid hydrocarbons.

Claims (2)

1. Система синтеза жидкого топлива, включающая:1. The system of synthesis of liquid fuel, including: реформинг-аппарат, который преобразует углеводородный сырьевой материал для получения синтез-газа, содержащего газообразный монооксид углерода и газообразный водород в качестве основных компонентов;a reforming apparatus that converts a hydrocarbon raw material to produce synthesis gas containing carbon monoxide gas and hydrogen gas as main components; реактор, который синтезирует жидкие углеводороды из газообразного монооксида углерода и газообразного водорода, содержащихся в синтез-газе;a reactor that synthesizes liquid hydrocarbons from gaseous carbon monoxide and gaseous hydrogen contained in the synthesis gas; устройство для повышающей качество обработки, которое осуществляет заданную повышающую качество обработку жидких углеводородов, синтезированных в реакторе; иa device for improving the quality of processing, which performs the specified improving the quality of the processing of liquid hydrocarbons synthesized in the reactor; and нагревательное устройство, которое нагревает жидкие углеводороды, вводимые в устройство для повышающей качество обработки, с использованием газа, выводимого из реформинг-аппарата, в качестве источника тепла.a heating device that heats the liquid hydrocarbons introduced into the device to improve the quality of processing, using gas removed from the reforming apparatus as a heat source. 2. Система синтеза жидкого топлива по п.1, в которой2. The system for the synthesis of liquid fuel according to claim 1, in which устройство для повышающей качество обработки представляет собой ректификационную колонну, которая производит фракционную разгонку жидких углеводородов на множество видов жидких топлив, имеющих различные температуры кипения, и/или реактор для гидрирования, который производит гидрирование жидких углеводородов. a device for improving the quality of processing is a distillation column, which produces fractional distillation of liquid hydrocarbons into many types of liquid fuels having different boiling points, and / or a hydrogenation reactor that produces hydrogenation of liquid hydrocarbons.
RU2008141283/04A 2006-03-30 2007-03-29 System of liquid fuel synthesis RU2418840C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2006095516 2006-03-30
JP2006-095516 2006-03-30

Publications (2)

Publication Number Publication Date
RU2008141283A true RU2008141283A (en) 2010-04-27
RU2418840C2 RU2418840C2 (en) 2011-05-20

Family

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Application Number Title Priority Date Filing Date
RU2008141283/04A RU2418840C2 (en) 2006-03-30 2007-03-29 System of liquid fuel synthesis

Country Status (7)

Country Link
JP (1) JP5107234B2 (en)
CN (1) CN101432391A (en)
AU (1) AU2007232922B2 (en)
MY (1) MY149298A (en)
RU (1) RU2418840C2 (en)
WO (1) WO2007114274A1 (en)
ZA (1) ZA200808242B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5174411B2 (en) * 2007-09-28 2013-04-03 独立行政法人石油天然ガス・金属鉱物資源機構 Effective heat utilization method of tube reformer
JP5424566B2 (en) * 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 Method for producing synthesis gas in liquid hydrocarbon production process from natural gas
JP5424569B2 (en) * 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 Method for producing synthesis gas in liquid hydrocarbon production process from natural gas
JP5173531B2 (en) 2008-03-31 2013-04-03 独立行政法人石油天然ガス・金属鉱物資源機構 Method of operating a syngas reformer in a GTL plant
JP5364329B2 (en) * 2008-09-30 2013-12-11 独立行政法人石油天然ガス・金属鉱物資源機構 Liquid fuel mixing system, liquid fuel synthesizing system, and liquid fuel mixing method
CA2804389C (en) * 2010-07-09 2017-01-17 Eco Technol Pty Ltd Syngas production through the use of membrane technologies
JP5804747B2 (en) * 2011-03-31 2015-11-04 独立行政法人石油天然ガス・金属鉱物資源機構 Method for suppressing metal contamination in syngas production equipment
WO2023085960A1 (en) * 2021-11-10 2023-05-19 Qatar Foundation For Education, Science And Community Development Retrofitting gas to liquids processing utilizing cargen technology

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6043288A (en) * 1998-02-13 2000-03-28 Exxon Research And Engineering Co. Gas conversion using synthesis gas produced hydrogen for catalyst rejuvenation and hydrocarbon conversion
WO2002070628A2 (en) * 2001-03-05 2002-09-12 Shell Internationale Research Maatschappij B.V. Process for the preparation of middle distillates
US6709569B2 (en) * 2001-12-21 2004-03-23 Chevron U.S.A. Inc. Methods for pre-conditioning fischer-tropsch light products preceding upgrading

Also Published As

Publication number Publication date
JP5107234B2 (en) 2012-12-26
AU2007232922B2 (en) 2010-12-09
MY149298A (en) 2013-08-30
AU2007232922A1 (en) 2007-10-11
WO2007114274A1 (en) 2007-10-11
CN101432391A (en) 2009-05-13
ZA200808242B (en) 2010-01-27
RU2418840C2 (en) 2011-05-20
JPWO2007114274A1 (en) 2009-08-13

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Effective date: 20140330