NO20084685L - Katalytisk reaktor omfattende forst og sekundaere stromningskanaler anordnet alternerende - Google Patents

Katalytisk reaktor omfattende forst og sekundaere stromningskanaler anordnet alternerende

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Publication number
NO20084685L
NO20084685L NO20084685A NO20084685A NO20084685L NO 20084685 L NO20084685 L NO 20084685L NO 20084685 A NO20084685 A NO 20084685A NO 20084685 A NO20084685 A NO 20084685A NO 20084685 L NO20084685 L NO 20084685L
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NO
Norway
Prior art keywords
flow channels
arranged alternately
reactants
insertion element
channels arranged
Prior art date
Application number
NO20084685A
Other languages
English (en)
Inventor
Michael Joseph Bowe
David James West
Robert Peat
Robert Frew Gillespie
Steven Brabon
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
Publication of NO20084685L publication Critical patent/NO20084685L/no

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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/249—Plate-type reactors
    • 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
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    • B01J19/24—Stationary reactors without moving elements inside
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00259—Preventing runaway of the chemical reaction
    • B01J2219/00265—Preventing flame propagation
    • 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
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    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2453—Plates arranged in parallel
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2456—Geometry of the plates
    • B01J2219/2458—Flat plates, i.e. plates which are not corrugated or otherwise structured, e.g. plates with cylindrical shape
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    • B01J2219/245—Plate-type reactors
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    • B01J2219/2459—Corrugated plates
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    • B01J2219/24—Stationary reactors without moving elements inside
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    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2456—Geometry of the plates
    • B01J2219/246—Perforated plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
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    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
    • B01J2219/2464—Independent temperature control in various sections of the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2465—Two reactions in indirect heat exchange with each other
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
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    • B01J2219/2469—Feeding means
    • B01J2219/247—Feeding means for the reactants
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2469—Feeding means
    • B01J2219/2471—Feeding means for the catalyst
    • B01J2219/2472—Feeding means for the catalyst the catalyst being exchangeable on inserts other than plates, e.g. in bags
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2474—Mixing means, e.g. fins or baffles attached to the plates
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
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    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts
    • B01J2219/2479—Catalysts coated on the surface of plates or inserts
    • 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
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    • B01J2219/245—Plate-type reactors
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    • B01J2219/2477—Construction materials of the catalysts
    • B01J2219/2482—Catalytically active foils; Plates having catalytically activity on their own
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
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    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
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    • B01J2219/2485—Metals or alloys
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    • B01J2219/245—Plate-type reactors
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    • B01J2219/245—Plate-type reactors
    • B01J2219/2491—Other constructional details
    • B01J2219/2498—Additional structures inserted in the channels, e.g. plates, catalyst holding meshes
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    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
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    • 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
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    • 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
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • C01B2203/0822—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel the fuel containing hydrogen
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    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
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    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1005—Arrangement or shape of catalyst
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Catalysts (AREA)

Abstract

En kompakt katalytisk reaktor definerer et mangfold av første og andre strømningskanaler anordnet alternerende, idet de første strømningskanaler ikke er mer enn 10 mm dype og tilveiebringer strømningslinjer for brennbare reaktanter, og inneholdende en katalysatorstruktur (20) for å katalysere forbrenning av reaktantene, og som har minst ett innløp for minst en av reaktantene. Den første strømningskanalen inkluderer også et innføringselement (40 eller 60) i umiddelbar nærhet av hvert innløp, idet dette innføringselementet ikke er katalytisk overfor forbrenningsreaksjonen: innføringselementet kan definere gap som er smalere enn den maksimale gapstørrelse for hindring av flammespredning. Denne reaktoren er anvendelig i et damp-metan-reformeringsanlegg.
NO20084685A 2006-05-08 2008-11-06 Katalytisk reaktor omfattende forst og sekundaere stromningskanaler anordnet alternerende NO20084685L (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0608927.0A GB0608927D0 (en) 2006-05-08 2006-05-08 Catalytic Reactor
PCT/GB2007/050200 WO2007129108A1 (en) 2006-05-08 2007-04-19 Catalytic reactor comprising first and secondary flow channels arranged alternately

Publications (1)

Publication Number Publication Date
NO20084685L true NO20084685L (no) 2009-01-27

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NO20084685A NO20084685L (no) 2006-05-08 2008-11-06 Katalytisk reaktor omfattende forst og sekundaere stromningskanaler anordnet alternerende

Country Status (15)

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US (1) US7897119B2 (no)
EP (1) EP2015865B1 (no)
JP (1) JP5362553B2 (no)
KR (1) KR20090018606A (no)
CN (2) CN101437607B (no)
AU (1) AU2007246839B2 (no)
BR (1) BRPI0711441B1 (no)
CA (1) CA2648501C (no)
DK (1) DK2015865T3 (no)
EA (1) EA014205B1 (no)
GB (1) GB0608927D0 (no)
MX (1) MX2008014021A (no)
NO (1) NO20084685L (no)
TW (1) TW200744750A (no)
WO (1) WO2007129108A1 (no)

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JP5581028B2 (ja) 2009-09-16 2014-08-27 住友精密工業株式会社 触媒反応器
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US10961122B2 (en) * 2012-02-06 2021-03-30 Helbio S.A. Heat integrated reformer with catalytic combustion for hydrogen production
CA3137624C (en) 2012-03-08 2023-06-20 Helbio Societe Anonyme Hydrogen And Energy Production Systems Catalytically heated fuel processor with replaceable structured supports bearing catalyst for fuel cell
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JP2015014499A (ja) * 2013-07-04 2015-01-22 ダイハツ工業株式会社 水素−酸素結合装置
CN105873854B (zh) * 2013-11-06 2019-02-05 瓦特燃料电池公司 使用钙钛矿作为其结构组分的重整器
FR3027663B1 (fr) * 2014-10-27 2019-05-03 Commissariat A L'energie Atomique Et Aux Energies Alternatives Reacteur echangeur comportant des moyens de modification de la distribution de fluide caloporteur
CN106892402A (zh) * 2015-12-18 2017-06-27 中国科学院大连化学物理研究所 一种波纹板式微通道甲醇蒸汽重整制氢反应器
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CN108180063B (zh) * 2017-11-24 2019-01-01 浙江大学 面向国六柴油机的折叠式后处理空间布置装置
JP7707478B2 (ja) * 2020-05-12 2025-07-15 ソレマルテック エス.エー. 作業デバイス
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DK2015865T3 (da) 2012-02-27
CN101437608A (zh) 2009-05-20
JP5362553B2 (ja) 2013-12-11
MX2008014021A (es) 2008-11-14
BRPI0711441B1 (pt) 2016-06-07
KR20090018606A (ko) 2009-02-20
AU2007246839B2 (en) 2011-10-20
EP2015865A1 (en) 2009-01-21
CA2648501A1 (en) 2007-11-15
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US20070258872A1 (en) 2007-11-08
CA2648501C (en) 2013-10-29
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GB0608927D0 (en) 2006-06-14
EA200870512A1 (ru) 2009-04-28
JP2009536143A (ja) 2009-10-08
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US7897119B2 (en) 2011-03-01
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