GB201118465D0 - Gas-to-liquid technology - Google Patents

Gas-to-liquid technology

Info

Publication number
GB201118465D0
GB201118465D0 GB201118465A GB201118465A GB201118465D0 GB 201118465 D0 GB201118465 D0 GB 201118465D0 GB 201118465 A GB201118465 A GB 201118465A GB 201118465 A GB201118465 A GB 201118465A GB 201118465 D0 GB201118465 D0 GB 201118465D0
Authority
GB
United Kingdom
Prior art keywords
gas
hydrogen
reactor
plant
synthesis
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
GB201118465A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CompactGTL PLC
Original Assignee
CompactGTL PLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CompactGTL PLC filed Critical CompactGTL PLC
Priority to GB201118465A priority Critical patent/GB201118465D0/en
Publication of GB201118465D0 publication Critical patent/GB201118465D0/en
Application status is Ceased legal-status Critical

Links

Abstract

A gas-to-liquids plant (10) for treating natural gas (5) includes a synthesis-gas-producing catalytic reactor (30) to produce a synthesis gas containing hydrogen and carbon monoxide, and a Fischer-Tropsch synthesis reactor (55) for generating hydrocarbons, and producing a tail gas, and also means (52) to generate a hydrogen-rich gas stream (34) from the synthesis gas or from the tail gas. The plant (10) also incorporates a hydrogen- desulphurisation reactor (87, 90) and means (86) to supply both the natural gas and the hydrogen-rich gas stream to the hydrogen-desulphurisation reactor during normal operation. The plant (10) also may comprise a hydrogen production module (92, 95) for use at start-up of the plant. The reactor (30) may comprise a partly-sacrificial catalyst bed.
GB201118465A 2011-10-26 2011-10-26 Gas-to-liquid technology Ceased GB201118465D0 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB201118465A GB201118465D0 (en) 2011-10-26 2011-10-26 Gas-to-liquid technology

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB201118465A GB201118465D0 (en) 2011-10-26 2011-10-26 Gas-to-liquid technology
PCT/GB2012/052614 WO2013061040A2 (en) 2011-10-26 2012-10-22 Gas-to-liquid technology
TW101139046A TW201333181A (en) 2011-10-26 2012-10-23 Gas-to-liquid technology

Publications (1)

Publication Number Publication Date
GB201118465D0 true GB201118465D0 (en) 2011-12-07

Family

ID=45373422

Family Applications (1)

Application Number Title Priority Date Filing Date
GB201118465A Ceased GB201118465D0 (en) 2011-10-26 2011-10-26 Gas-to-liquid technology

Country Status (3)

Country Link
GB (1) GB201118465D0 (en)
TW (1) TW201333181A (en)
WO (1) WO2013061040A2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013104893A1 (en) * 2013-05-13 2014-11-13 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude A method for starting a prereforming
US9683176B2 (en) * 2015-10-16 2017-06-20 Haldor Topsøe A/S Process for conversion of natural gas to liquid hydrocarbons and a plant for carrying out the process
US10294102B2 (en) * 2016-12-15 2019-05-21 Praxair Technology, Inc. Method of catalyst reduction in a hydrogen plant

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NO311081B1 (en) * 1999-12-09 2001-10-08 Norske Stats Oljeselskap Optimized FT synthesis by reforming and recirculation of tail gas from the FT synthesis
EP1905508A3 (en) 2000-01-11 2012-09-05 CompactGTL plc Catalytic reactor
WO2003048034A1 (en) 2001-12-05 2003-06-12 Gtl Microsystems Ag Process an apparatus for steam-methane reforming
US7033552B2 (en) * 2002-01-31 2006-04-25 Chevron U.S.A. Inc. Upgrading Fischer-Tropsch and petroleum-derived naphthas and distillates
AU2002351515A1 (en) * 2002-12-13 2004-07-09 Petrosa (The Petroleum Oil & Gas Corporation Of Sa (Pty) Ltd A method for oil recovery from an oil field
GB0500838D0 (en) * 2005-01-15 2005-02-23 Accentus Plc Catalytic reactor
GB0608277D0 (en) * 2006-04-27 2006-06-07 Accentus Plc Process for preparing liquid hydrocarbons
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 the liquid hydrocarbon production process from natural gas
EA201290112A1 (en) * 2009-08-31 2012-06-29 Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн Method for obtaining a suspension, a device for obtaining a suspension, a reactor for the synthesis of hydrocarbons and a reaction system for the synthesis of hydrocarbons

Also Published As

Publication number Publication date
TW201333181A (en) 2013-08-16
WO2013061040A2 (en) 2013-05-02
WO2013061040A3 (en) 2013-06-20

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Legal Events

Date Code Title Description
AT Applications terminated before publication under section 16(1)