RU2006140327A - Каталитический реактор - Google Patents

Каталитический реактор Download PDF

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Publication number
RU2006140327A
RU2006140327A RU2006140327/12A RU2006140327A RU2006140327A RU 2006140327 A RU2006140327 A RU 2006140327A RU 2006140327/12 A RU2006140327/12 A RU 2006140327/12A RU 2006140327 A RU2006140327 A RU 2006140327A RU 2006140327 A RU2006140327 A RU 2006140327A
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channels
stream
catalytic reactor
reactor according
heat transfer
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RU2006140327/12A
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RU2415701C2 (ru
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Майкл Джозеф БОУЭ (GB)
Майкл Джозеф Боуэ
Дэвид Чарльз Уилль м БЛЭЙКЛИ (GB)
Дэвид Чарльз Уилльям БЛЭЙКЛИ
Клив Дерек ЛИ-ТАФФНЕЛЛ (GB)
Клив Дерек ЛИ-ТАФФНЕЛЛ
Джейсон Эндрю МОД (GB)
Джейсон Эндрю МОД
Дэвид Лесли СИГАЛ (GB)
Дэвид Лесли СИГАЛ
Джон Уилль м СТЭЙРМАНД (GB)
Джон Уилльям СТЭЙРМАНД
Ян Фредерик ЗИММЕРМАН (GB)
Ян Фредерик ЗИММЕРМАН
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КОМПАКТДЖТЛ ПиЭлСи (GB)
КОМПАКТДЖТЛ ПиЭлСи
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    • 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
    • B01J35/56—
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J19/248—Reactors comprising multiple separated flow channels
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    • 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
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production 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
    • C01B3/34—Production 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
    • C01B3/38—Production 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 using catalysts
    • C01B3/384—Production 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 using catalysts the catalyst being continuously externally heated
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    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00117—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
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    • B01J2219/00132—Controlling the temperature using electric heating or cooling elements
    • B01J2219/00135—Electric resistance heaters
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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
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    • B01J2219/2451—Geometry of the reactor
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    • 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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    • B01J2219/2491—Other constructional details
    • B01J2219/2492—Assembling means
    • B01J2219/2493—Means for assembling plates together, e.g. sealing means, screws, bolts
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    • 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
    • B01J2219/2491—Other constructional details
    • B01J2219/2498—Additional structures inserted in the channels, e.g. plates, catalyst holding meshes
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
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    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
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    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
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    • B01J2219/32213—Plurality of essentially parallel sheets
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    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324—Composition or microstructure of the elements
    • B01J2219/32466—Composition or microstructure of the elements comprising catalytically active material
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
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    • B01J2219/32466—Composition or microstructure of the elements comprising catalytically active material
    • B01J2219/32475—Composition or microstructure of the elements comprising catalytically active material involving heat exchange
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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
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    • 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
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    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
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    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/085—Methods of heating the process for making hydrogen or synthesis gas by electric heating
    • 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
    • C01B2203/0866—Methods of heating the process for making hydrogen or synthesis gas by combination of different heating methods
    • 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
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    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Claims (8)

1. Каталитический реактор, включающий множество металлических листов, расположенных в стопке и связанных между собой, причем листы сформированы таким образом, чтобы определить каналы первого потока между смежными листами и каналы второго потока между смежными листами, чередуя каналы первого потока с каналами второго потока в стопке, и так, чтобы обеспечить хороший термический контакт между текучими средами в каналах первого и второго потоков, коллекторы для подачи текучей среды в каналы потоков, причем коллекторы являются такими, что различные текучие среды могут быть поданы в каналы первого и второго потоков, причем внутри каналов первого потока находятся проницаемые металлические теплопередающие слои, причем металлические теплопередающие слои являются удаляемыми и включающими каталитическое покрытие, содержащее катализатор горения, чтобы осуществить горение газовой смеси, текущей в каналах первого потока, отличающийся тем, что катализатор горения в по меньшей мере первой части канала покрыт инертным пористым керамическим слоем для уменьшения скорости реакции.
2. Каталитический реактор по п.1, в котором каналы первого и второго газовых потоков являются менее 8 мм глубиной в направлении, перпендикулярном смежным металлическим листам.
3. Каталитический реактор по п.1, в котором удаляемые металлические теплопроводящие слои находятся в каналах как первого, так и второго потоков, причем каждый такой металлический теплопроводящий слой содержит волнистую металлическую фольгу.
4. Каталитический реактор по п.3, в котором в по меньшей мере одном из каналов шаг волнистой фольги меняется по длине канала.
5. Каталитический реактор по любому из пп. 1-4, в котором направление потока каналов первого потока является поперечным направлению потока каналов второго потока.
6. Каталитический реактор по любому из пп. 1-4 для осуществления конверсии метана с водяным паром, в котором удаляемые металлические теплопередающие слои расположены в каналах как первого, так и второго потоков и удаляемые теплопередающие слои в каналах второго потока включают катализатор конверсии метана с водяным паром.
7. Каталитический реактор по п.5 для осуществления конверсии метана с водяным паром, в котором удаляемые металлические теплопередающие слои расположены в каналах как первого, так и второго потоков и удаляемые теплопередающие слои в каналах второго потока включают катализатор конверсии метана с водяным паром.
8. Способ осуществления конверсии метана с водяным паром, в котором используют каталитический реактор по любому из пп. 1-7.
RU2006140327/05A 2001-07-11 2006-11-15 Каталитический реактор RU2415701C2 (ru)

Applications Claiming Priority (2)

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GB0116894.7 2001-07-11
GBGB0116894.7A GB0116894D0 (en) 2001-07-11 2001-07-11 Catalytic reactor

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RU2415701C2 RU2415701C2 (ru) 2011-04-10

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US (1) US8118889B2 (ru)
EP (2) EP2332642A3 (ru)
JP (1) JP4616554B2 (ru)
KR (1) KR20040024580A (ru)
CN (2) CN100512949C (ru)
AP (1) AP2060A (ru)
AU (1) AU2002314372B2 (ru)
BR (1) BR0210943B1 (ru)
CA (1) CA2451416C (ru)
GB (1) GB0116894D0 (ru)
MX (1) MXPA04000207A (ru)
NO (1) NO333304B1 (ru)
OA (1) OA12566A (ru)
RU (2) RU2296003C2 (ru)
WO (1) WO2003006149A1 (ru)

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US8118889B2 (en) 2012-02-21
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