NO20075105L - Dampreformering - Google Patents

Dampreformering

Info

Publication number
NO20075105L
NO20075105L NO20075105A NO20075105A NO20075105L NO 20075105 L NO20075105 L NO 20075105L NO 20075105 A NO20075105 A NO 20075105A NO 20075105 A NO20075105 A NO 20075105A NO 20075105 L NO20075105 L NO 20075105L
Authority
NO
Norway
Prior art keywords
heat exchange
steam reforming
catalyst
tubes
zone
Prior art date
Application number
NO20075105A
Other languages
English (en)
Other versions
NO344874B1 (no
Inventor
Martin Fowles
Stuart Ballentyne Brady
Peter William Farnell
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
Publication of NO20075105L publication Critical patent/NO20075105L/no
Publication of NO344874B1 publication Critical patent/NO344874B1/no

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/14—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by endowing the walls of conduits with zones of different degrees of conduction of heat
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical 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
    • B01J8/06—Chemical 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 in tube reactors; the solid particles being arranged in tubes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical 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
    • B01J8/06—Chemical 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 in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
    • C01B3/34—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts with external heating of the catalyst
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/106—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
    • F28D7/1607—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with particular pattern of flow of the heat exchange media, e.g. change of flow direction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212—Plates; Jackets; Cylinders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212—Plates; Jackets; Cylinders
    • B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00477—Controlling the temperature by thermal insulation means
    • B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00504—Controlling the temperature by means of a burner
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/0838—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel
    • C01B2203/0844—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel the non-combustive exothermic reaction being another reforming reaction as defined in groups C01B2203/02 - C01B2203/0294
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1005—Arrangement or shape of catalyst
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041—Composition of the catalyst
    • C01B2203/1047—Group VIII metal catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041—Composition of the catalyst
    • C01B2203/1047—Group VIII metal catalysts
    • C01B2203/1052—Nickel or cobalt catalysts
    • C01B2203/1058—Nickel catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1235—Hydrocarbons
    • C01B2203/1241—Natural gas or methane
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/14—Details of the flowsheet
    • C01B2203/142—At least two reforming, decomposition or partial oxidation steps in series
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
    • F28F2265/26—Safety or protection arrangements; Arrangements for preventing malfunction for allowing differential expansion between elements

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Et apparat for dampreformering av hydrokarboner er beskrevet, omfattende en varmevekslingsreformer hvori det er anbrakt et flertall vertikale katalysatorfylte rør, hvorigjennom en gassblanding omfattende hydrokarbon og vanndamp kan føres, og hvortil varme kan overføres ved hjelp av et varmevekslingsmedium som strømmer omkring de utvendige røroverflater, hvori varmevekslingstilpasningsanordninger er anordnet inne i reformeren slik at rørene har en sone med lavere varmeveksling som strekker seg fra bunnen av katalysatoren opp til 25 % av katalysatordybden med ikke noen varmevekslingsøkende anordninger anordnet i den nevnte sone. En prosess for dampreformering av hydrokarboner ved bruk av nevnte apparat er også beskrevet.
NO20075105A 2005-04-11 2007-10-09 Apparat og fremgangsmåte for dampreformering av hydrokarboner NO344874B1 (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0507269.9A GB0507269D0 (en) 2005-04-11 2005-04-11 Steam reforming
PCT/GB2006/050068 WO2006109095A1 (en) 2005-04-11 2006-03-27 Steam reforming

Publications (2)

Publication Number Publication Date
NO20075105L true NO20075105L (no) 2008-01-09
NO344874B1 NO344874B1 (no) 2020-06-08

Family

ID=34610914

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20075105A NO344874B1 (no) 2005-04-11 2007-10-09 Apparat og fremgangsmåte for dampreformering av hydrokarboner

Country Status (12)

Country Link
US (1) US7731935B2 (no)
CN (1) CN100563810C (no)
AU (1) AU2006235745B2 (no)
BR (1) BRPI0610674B1 (no)
EA (1) EA011577B1 (no)
EG (1) EG25126A (no)
GB (1) GB0507269D0 (no)
MY (1) MY143525A (no)
NO (1) NO344874B1 (no)
NZ (1) NZ562068A (no)
WO (1) WO2006109095A1 (no)
ZA (1) ZA200708615B (no)

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2924423B1 (fr) * 2007-12-03 2010-11-26 Air Liquide Procede de production de gaz de synthese par reformage a la vapeur
CN101825271B (zh) * 2009-03-06 2016-04-13 中国石油化工股份有限公司 一种多液相平行分布的换热器
US20100278700A1 (en) * 2009-03-30 2010-11-04 Lawrence Clawson Steam reformer with passive heat flux control elements
JP2011107925A (ja) * 2009-11-17 2011-06-02 Ubiquitous Corp プログラム、制御方法、並びに制御装置
JP5506418B2 (ja) * 2010-01-15 2014-05-28 株式会社ユビキタス プログラム、制御方法、並びに制御装置
US8287763B2 (en) 2010-10-28 2012-10-16 Air Products And Chemicals, Inc. Steam-hydrocarbon reforming with limited steam export
FR2979257B1 (fr) * 2011-08-26 2013-08-16 Ifp Energies Now Reacteur echangeur pour la production d'hydrogene avec faisceau de generation vapeur integre
KR101422630B1 (ko) 2011-12-30 2014-07-23 두산중공업 주식회사 열교환형 선개질기
US10961122B2 (en) * 2012-02-06 2021-03-30 Helbio S.A. Heat integrated reformer with catalytic combustion for hydrogen production
DE102013020856A1 (de) * 2013-12-12 2015-06-18 Linde Aktiengesellschaft Reformerrohr und Einrichtung sowie Verfahren zur Herstellung eines Synthesegases
GB201403787D0 (en) * 2014-03-04 2014-04-16 Johnson Matthey Plc Steam reforming
DE102015219305A1 (de) * 2015-10-06 2017-04-06 Hydrogenious Technologies Gmbh Reaktor-Vorrichtung zum Dehydrieren eines Trägermediums
CN107356140A (zh) * 2016-01-08 2017-11-17 申清章 一种换热速度快的化工用快速换热快速清洗装置
US11213794B2 (en) 2016-06-10 2022-01-04 Haldor Topsøe A/S CO rich synthesis gas production
US9943818B2 (en) 2016-06-20 2018-04-17 Air Products And Chemicals, Inc. Steam-hydrocarbon reforming reactor
CN106422994B (zh) * 2016-10-21 2022-10-18 北京沃特尔水技术股份有限公司 一种制备碳铵类汲取液的方法及设备
CA3042969A1 (en) 2016-11-09 2018-05-17 8 Rivers Capital, Llc Systems and methods for power production with integrated production of hydrogen
JP7297775B2 (ja) 2017-11-09 2023-06-26 ８ リバーズ キャピタル，エルエルシー 水素および二酸化炭素の生成および分離のためのシステムおよび方法
EP3530612A1 (de) 2018-02-22 2019-08-28 Linde Aktiengesellschaft Verfahren und anlage zur bereitstellung eines überwiegend oder ausschliesslich wasserstoff enthaltenden gasprodukts
JP7218155B2 (ja) * 2018-11-07 2023-02-06 三菱重工業株式会社 改質装置、改質ガスの製造方法、及び改質システム
GB201908449D0 (en) 2019-06-12 2019-07-24 Johnson Matthey Davy Technologies Ltd Process for synthesising methanol
KR20220020842A (ko) 2019-06-13 2022-02-21 8 리버스 캐피탈, 엘엘씨 추가 생성물들의 공동 발생을 구비하는 동력 생산
GB202102787D0 (en) * 2021-02-26 2021-04-14 Johnson Matthey Plc Heat exchange reactor seal apparatus
AU2022394811A1 (en) 2021-11-18 2024-06-27 8 Rivers Capital, Llc Apparatus for hydrogen production
US11781076B2 (en) * 2022-03-01 2023-10-10 Chevron U.S.A. Inc. Multi-tube reactor systems and processes for no-oxidative conversion of methane
WO2025078974A2 (en) 2023-10-09 2025-04-17 8 Rivers Capital, Llc Systems and methods for producing hydrogen with integrated capture of carbon dioxide
GB202416059D0 (en) 2024-10-31 2024-12-18 Johnson Matthey Plc Plant for the production of synthesis gas

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0194067A2 (en) * 1985-03-05 1986-09-10 Imperial Chemical Industries Plc Steam reforming hydrocarbons
US5362454A (en) * 1993-06-28 1994-11-08 The M. W. Kellogg Company High temperature heat exchanger

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2700598A (en) * 1946-10-31 1955-01-25 Standard Oil Dev Co Process for reforming hydrocarbons
US3765851A (en) * 1970-12-14 1973-10-16 Chervon Res Co Gas production
US4127389A (en) 1977-04-04 1978-11-28 Pullman Incorporated Exchanger reactor
US5023276A (en) * 1982-09-30 1991-06-11 Engelhard Corporation Preparation of normally liquid hydrocarbons and a synthesis gas to make the same, from a normally gaseous hydrocarbon feed
GB9516125D0 (en) 1995-08-07 1995-10-04 Ici Plc Heat exchange apparatus and process
US6855272B2 (en) * 2001-07-18 2005-02-15 Kellogg Brown & Root, Inc. Low pressure drop reforming exchanger

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0194067A2 (en) * 1985-03-05 1986-09-10 Imperial Chemical Industries Plc Steam reforming hydrocarbons
US5362454A (en) * 1993-06-28 1994-11-08 The M. W. Kellogg Company High temperature heat exchanger

Also Published As

Publication number Publication date
AU2006235745B2 (en) 2010-09-23
MY143525A (en) 2011-05-31
CN101155630A (zh) 2008-04-02
US7731935B2 (en) 2010-06-08
NZ562068A (en) 2010-07-30
CN100563810C (zh) 2009-12-02
BRPI0610674A2 (pt) 2010-07-20
ZA200708615B (en) 2008-10-29
EG25126A (en) 2011-09-18
US20090123348A1 (en) 2009-05-14
AU2006235745A1 (en) 2006-10-19
BRPI0610674B1 (pt) 2015-07-21
WO2006109095A1 (en) 2006-10-19
EA200702219A1 (ru) 2008-02-28
GB0507269D0 (en) 2005-05-18
EA011577B1 (ru) 2009-04-28
NO344874B1 (no) 2020-06-08

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