NO20073625L - Katalytisk reaktor - Google Patents

Katalytisk reaktor

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Publication number
NO20073625L
NO20073625L NO20073625A NO20073625A NO20073625L NO 20073625 L NO20073625 L NO 20073625L NO 20073625 A NO20073625 A NO 20073625A NO 20073625 A NO20073625 A NO 20073625A NO 20073625 L NO20073625 L NO 20073625L
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NO
Norway
Prior art keywords
pressure
module
reactor
gas stream
gas
Prior art date
Application number
NO20073625A
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English (en)
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Michael Joseph Bowe
John Vitucci
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Compactgtl Plc
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Publication date
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Publication of NO20073625L publication Critical patent/NO20073625L/no

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/248Reactors comprising multiple separated flow channels
    • B01J19/249Plate-type reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • 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
    • C01B3/22Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
    • C01B3/24Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
    • C01B3/26Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using catalysts
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    • 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
    • C01B3/38Production 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
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    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
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    • 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
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    • C01B3/382Multi-step processes
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    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
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    • 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
    • C01B3/38Production 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
    • C01B3/384Production 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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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
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    • B01J2219/2461Heat exchange aspects
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    • B01J2219/2464Independent temperature control in various sections of the reactor
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    • B01J2219/2465Two reactions in indirect heat exchange with each other
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    • B01J2219/2471Feeding means for the catalyst
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    • B01J2219/2479Catalysts coated on the surface of plates or inserts
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    • B01J2219/2493Means for assembling plates together, e.g. sealing means, screws, bolts
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Abstract

En kompakt katalytisk reaktor (20) for reformering som omfatter en reaktormodul (70) for å definere et mangfold av første og andre strømningskanaler anordnet alternerende, for føring av første og andre gasstrømmer, og en fjernbar gasspermeabel katalysatorstruktur (80) med et substrat f.eks. av metallfolie er tilveiebrakt i hver strømningskanal hvori en kjemisk reaksjon skal foregå. Reaktoren er for bruk med en første gasstrøm hvis trykk er over omgivelsestrykk og er ikke mindre enn det av den andre gasstrømmen. Reaktormodulen (70) kan være dannet av en stabel av plater (72, 74, 75). Modulen (70) er innelukket i en trykktank (90), idet trykket i trykktanken er anordnet til å være ved et trykk som hovedsakelig er det av den første gasstrømmen. Følgelig er ingen deler av modulen (70) under spenning. Dette forenkler utformingen av reaktormodulen, og øker andelen av dens volum som okkuperes av katalysatoren.
NO20073625A 2005-01-15 2007-07-13 Katalytisk reaktor NO20073625L (no)

Applications Claiming Priority (2)

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GBGB0500838.8A GB0500838D0 (en) 2005-01-15 2005-01-15 Catalytic reactor
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JP2008526501A (ja) 2008-07-24
BRPI0519810A2 (pt) 2009-03-17
EP1858637A1 (en) 2007-11-28
EA200701517A1 (ru) 2007-12-28
CA2592939A1 (en) 2006-07-20
WO2006075130A1 (en) 2006-07-20
GB0500838D0 (en) 2005-02-23
CN101128260A (zh) 2008-02-20
TW200631653A (en) 2006-09-16
EA010780B1 (ru) 2008-10-30
MX2007008530A (es) 2007-09-06
KR20070100737A (ko) 2007-10-11
AU2005324800A1 (en) 2006-07-20

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