GB201121566D0 - Process - Google Patents

Process

Info

Publication number
GB201121566D0
GB201121566D0 GB201121566A GB201121566A GB201121566D0 GB 201121566 D0 GB201121566 D0 GB 201121566D0 GB 201121566 A GB201121566 A GB 201121566A GB 201121566 A GB201121566 A GB 201121566A GB 201121566 D0 GB201121566 D0 GB 201121566D0
Authority
GB
United Kingdom
Prior art keywords
synthesis gas
catalyst
production
passing
heated
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
GB201121566A
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.)
Johnson Matthey PLC
Original Assignee
Johnson Matthey 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 Johnson Matthey PLC filed Critical Johnson Matthey PLC
Priority to GB201121566A priority Critical patent/GB201121566D0/en
Publication of GB201121566D0 publication Critical patent/GB201121566D0/en
Priority to CN201280062037.6A priority patent/CN104066821A/en
Priority to GB1408984.1A priority patent/GB2512758A/en
Priority to PCT/GB2012/052896 priority patent/WO2013088116A1/en
Ceased legal-status Critical Current

Links

Abstract

A process for increasing the hydrogen content of a synthesis gas containing one or more sulphur compounds is described, comprising the steps of (i) heating the synthesis gas and (ii) passing at least part of the heated synthesis gas and steam through a reactor containing a sour shift catalyst, wherein the synthesis gas is heated by passing it through a plurality of tubes disposed within said catalyst in a direction counter-current to the flow of said synthesis gas through the catalyst. The resulting synthesis gas may be passed to one or more additional reactors containing sour shift catalyst to maximise the yield of hydrogen production, or used for methanol production, for the Fischer-Tropsch synthesis of liquid hydrocarbons or for the production of synthetic natural gas.
GB201121566A 2011-12-15 2011-12-15 Process Ceased GB201121566D0 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
GB201121566A GB201121566D0 (en) 2011-12-15 2011-12-15 Process
CN201280062037.6A CN104066821A (en) 2011-12-15 2012-11-22 A water-gas-shift process
GB1408984.1A GB2512758A (en) 2011-12-15 2012-11-22 A water-gas-shift process
PCT/GB2012/052896 WO2013088116A1 (en) 2011-12-15 2012-11-22 A water-gas -shift process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB201121566A GB201121566D0 (en) 2011-12-15 2011-12-15 Process

Publications (1)

Publication Number Publication Date
GB201121566D0 true GB201121566D0 (en) 2012-01-25

Family

ID=45560504

Family Applications (2)

Application Number Title Priority Date Filing Date
GB201121566A Ceased GB201121566D0 (en) 2011-12-15 2011-12-15 Process
GB1408984.1A Withdrawn GB2512758A (en) 2011-12-15 2012-11-22 A water-gas-shift process

Family Applications After (1)

Application Number Title Priority Date Filing Date
GB1408984.1A Withdrawn GB2512758A (en) 2011-12-15 2012-11-22 A water-gas-shift process

Country Status (3)

Country Link
CN (1) CN104066821A (en)
GB (2) GB201121566D0 (en)
WO (1) WO2013088116A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013224037A1 (en) 2013-11-25 2015-05-28 Siemens Aktiengesellschaft Preparation and conditioning of synthesis crude gases
DE102013224039A1 (en) 2013-11-25 2015-05-28 Clariant International Ltd. Treatment of synthesis gases from a gasification facility
CN108977236B (en) * 2018-08-29 2020-09-18 国家能源投资集团有限责任公司 Low-temperature methanol washing system and synthetic gas providing method
DE102018007868A1 (en) * 2018-10-05 2020-04-09 Linde Aktiengesellschaft Method and device for producing gas products using a shift converter
WO2024000371A1 (en) * 2022-06-30 2024-01-04 Bp P.L.C. Integrated fischer-tropsch processes

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB457155A (en) * 1935-12-24 1936-11-23 Non Poisonous Gas Holding Comp An improved heat exchange apparatus for effecting a catalytic reaction
GB498796A (en) * 1938-03-31 1939-01-13 Bamag Meguin Ag Process for washing gases or vapours out of crude water gas
DE8708603U1 (en) * 1987-06-20 1987-08-13 Metallgesellschaft Ag, 6000 Frankfurt, De
DE19832386A1 (en) * 1998-07-18 2000-01-27 Dbb Fuel Cell Engines Gmbh Reforming reactor with catalytic burner unit
US7022306B1 (en) * 2003-03-21 2006-04-04 Uop Llc Process for the production of hydrogen
GB0814053D0 (en) 2008-08-01 2008-09-10 Johnson Matthey Plc Process
CA2739274C (en) * 2010-10-11 2012-04-24 Pioneer Energy, Inc. Compact natural gas steam reformer and reforming method with linear countercurrent heat exchanger

Also Published As

Publication number Publication date
CN104066821A (en) 2014-09-24
GB201408984D0 (en) 2014-07-02
GB2512758A (en) 2014-10-08
WO2013088116A1 (en) 2013-06-20

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Legal Events

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