GB2474164A - Process for increasing hydrogen content of synthesis gas - Google Patents

Process for increasing hydrogen content of synthesis gas Download PDF

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Publication number
GB2474164A
GB2474164A GB1100526A GB201100526A GB2474164A GB 2474164 A GB2474164 A GB 2474164A GB 1100526 A GB1100526 A GB 1100526A GB 201100526 A GB201100526 A GB 201100526A GB 2474164 A GB2474164 A GB 2474164A
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United Kingdom
Prior art keywords
synthesis gas
catalyst
hydrogen content
production
passing
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.)
Granted
Application number
GB1100526A
Other versions
GB2474164B (en
GB201100526D0 (en
Inventor
Peter Edward James Abbott
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
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Filing date
Publication date
Application filed by Johnson Matthey PLC filed Critical Johnson Matthey PLC
Publication of GB201100526D0 publication Critical patent/GB201100526D0/en
Publication of GB2474164A publication Critical patent/GB2474164A/en
Application granted granted Critical
Publication of GB2474164B publication Critical patent/GB2474164B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0242Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical
    • B01J8/025Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical in a cylindrical shaped bed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0285Heating or cooling the reactor
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/16Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/48Production 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/02Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment
    • C10K3/04Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment reducing the carbon monoxide content, e.g. water-gas shift [WGS]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132Tubes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0283Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0435Catalytic purification
    • C01B2203/045Purification by catalytic desulfurisation
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
    • C01B2203/0485Composition of the impurity the impurity being a sulfur compound
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041Composition of the catalyst
    • C01B2203/1047Group VIII metal catalysts
    • C01B2203/1052Nickel or cobalt catalysts

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 co-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.
GB1100526.1A 2008-08-01 2009-07-10 Process for increasing hydrogen content of synthesis gas Expired - Fee Related GB2474164B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0814053.5A GB0814053D0 (en) 2008-08-01 2008-08-01 Process
PCT/GB2009/050820 WO2010013026A1 (en) 2008-08-01 2009-07-10 Process for increasing hydrogen content of synthesis gas

Publications (3)

Publication Number Publication Date
GB201100526D0 GB201100526D0 (en) 2011-03-02
GB2474164A true GB2474164A (en) 2011-04-06
GB2474164B GB2474164B (en) 2013-01-30

Family

ID=39767327

Family Applications (2)

Application Number Title Priority Date Filing Date
GBGB0814053.5A Ceased GB0814053D0 (en) 2008-08-01 2008-08-01 Process
GB1100526.1A Expired - Fee Related GB2474164B (en) 2008-08-01 2009-07-10 Process for increasing hydrogen content of synthesis gas

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GBGB0814053.5A Ceased GB0814053D0 (en) 2008-08-01 2008-08-01 Process

Country Status (6)

Country Link
US (1) US8642667B2 (en)
CN (1) CN102112218B (en)
AU (1) AU2009275643B2 (en)
CA (1) CA2731335C (en)
GB (2) GB0814053D0 (en)
WO (1) WO2010013026A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2496725A (en) * 2011-11-18 2013-05-22 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing sulphur compounds
GB2496726A (en) * 2011-11-18 2013-05-22 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing sulphur compounds
GB2496724A (en) * 2011-11-18 2013-05-22 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing sulphur compounds

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9012523B2 (en) * 2011-12-22 2015-04-21 Kellogg Brown & Root Llc Methanation of a syngas
GB0919385D0 (en) * 2009-11-05 2009-12-23 Johnson Matthey Plc Process
GB201121566D0 (en) 2011-12-15 2012-01-25 Johnson Matthey Plc Process
FR3014862B1 (en) 2013-12-17 2016-01-01 Axens PROCESS FOR THE PURIFICATION OF SYNTHESIS GAS BY WASHING ON AQUEOUS AMINE SOLUTIONS
US9856141B2 (en) * 2016-01-07 2018-01-02 Fluor Technologies Corporation Method for avoiding expensive sour water stripper metallurgy in a gasification plant
WO2020035564A1 (en) 2018-08-17 2020-02-20 Haldor Topsøe A/S Reduction of the content of carbon monoxide in the feed for steam reformers for hydrogen production
CN113795330A (en) * 2019-04-23 2021-12-14 托普索公司 High temperature reactor vessel, apparatus and method
IT202000001912A1 (en) 2020-01-31 2021-07-31 Dondi S P A TOOL HOLDER FOR AGRICULTURAL WORKS.

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3666682A (en) * 1969-11-26 1972-05-30 Texaco Inc Water-gas shift conversion process
EP0278063A2 (en) * 1987-02-09 1988-08-17 Texaco Development Corporation Process for upgrading water used in cooling and cleaning of raw synthesis gas
WO2009019497A2 (en) * 2007-08-03 2009-02-12 Johnson Matthey Plc Process for the generation of a synthesis gas

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3872025A (en) * 1969-10-31 1975-03-18 Bethlehem Steel Corp Production and utilization of synthesis gas
GB8521650D0 (en) * 1985-08-30 1985-10-02 Ici Plc Catalyst
EP2152409B1 (en) * 2007-04-27 2016-06-29 Saudi Basic Industries Corporation Catalytic hydrogenation of carbon dioxide into syngas mixture

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3666682A (en) * 1969-11-26 1972-05-30 Texaco Inc Water-gas shift conversion process
EP0278063A2 (en) * 1987-02-09 1988-08-17 Texaco Development Corporation Process for upgrading water used in cooling and cleaning of raw synthesis gas
WO2009019497A2 (en) * 2007-08-03 2009-02-12 Johnson Matthey Plc Process for the generation of a synthesis gas

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
International Journal of Hydrogen Energy, 2005, vol.30, no.7, Chiesa P. et. al., pages 747-767. *

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2496725A (en) * 2011-11-18 2013-05-22 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing sulphur compounds
GB2496726A (en) * 2011-11-18 2013-05-22 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing sulphur compounds
GB2496724A (en) * 2011-11-18 2013-05-22 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing sulphur compounds
GB2496726B (en) * 2011-11-18 2014-04-16 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing one or more sulphur compounds
GB2496724B (en) * 2011-11-18 2014-08-06 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing one or more sulphur compounds
GB2496725B (en) * 2011-11-18 2014-08-06 Johnson Matthey Plc A process for increasing the hydrogen content of a synthesis gas containing one or more sulphur compounds
US9187323B2 (en) 2011-11-18 2015-11-17 Johnson Matthey Public Limited Company Process for increasing hydrogen content of synthesis gas
US9193590B2 (en) 2011-11-18 2015-11-24 Johnson Matthey Public Limited Company Process for increasing hydrogen content of synthesis gas
US9206044B2 (en) 2011-11-18 2015-12-08 Johnson Matthey Public Limited Company Process for increasing hydrogen content of synthesis gas

Also Published As

Publication number Publication date
US20110137089A1 (en) 2011-06-09
CA2731335A1 (en) 2010-02-04
GB2474164B (en) 2013-01-30
US8642667B2 (en) 2014-02-04
CA2731335C (en) 2015-12-08
GB201100526D0 (en) 2011-03-02
AU2009275643B2 (en) 2014-10-02
CN102112218B (en) 2013-12-04
CN102112218A (en) 2011-06-29
AU2009275643A1 (en) 2010-02-04
GB0814053D0 (en) 2008-09-10
WO2010013026A1 (en) 2010-02-04

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PCNP Patent ceased through non-payment of renewal fee

Effective date: 20160710