NO20055174L - Fremgangsmate og apparat for hurtig oppvarming av brenselnyformingsreaktanter - Google Patents

Fremgangsmate og apparat for hurtig oppvarming av brenselnyformingsreaktanter

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Publication number
NO20055174L
NO20055174L NO20055174A NO20055174A NO20055174L NO 20055174 L NO20055174 L NO 20055174L NO 20055174 A NO20055174 A NO 20055174A NO 20055174 A NO20055174 A NO 20055174A NO 20055174 L NO20055174 L NO 20055174L
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Norway
Prior art keywords
combustion
heat
section
heat regeneration
combustion chamber
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NO20055174A
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English (en)
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NO20055174D0 (no
Inventor
Kevin H Nguyen
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Texaco Development Corp
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Publication of NO20055174D0 publication Critical patent/NO20055174D0/no
Publication of NO20055174L publication Critical patent/NO20055174L/no

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    • 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
    • C01B3/48—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 followed by reaction of water vapour with carbon monoxide
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    • 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
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    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/2485—Monolithic reactors
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/22—Production of hydrogen; Production of gaseous mixtures containing hydrogen by decomposition of gaseous or liquid organic compounds
    • C01B3/24—Production of hydrogen; Production of gaseous mixtures containing hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
    • C01B3/26—Production of hydrogen; Production of gaseous mixtures containing hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using catalysts
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    • 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
    • C01B3/382—Processes with two or more reaction steps, of which at least one is catalytic, e.g. steam reforming and partial oxidation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C13/00—Apparatus in which combustion takes place in the presence of catalytic material
    • F23C13/02—Apparatus in which combustion takes place in the presence of catalytic material characterised by arrangements for starting the operation, e.g. for heating the catalytic material to operating temperature
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    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00083—Coils
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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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00157—Controlling the temperature by means of a burner
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    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
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    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
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    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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    • 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)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Fuel Cell (AREA)

Abstract

Apparat for rask oppvarming av en eller flere reaktanter for bruk i en brensekeformer. Apparatet omfatter en forbrermingsseksjon med en yttervegg som omslutter et forbrermingskammer og en katalysator anbrakt i forbrermingskammeret. Katalysatoren tilveiebringer en ikke-diffusert sfrørrmingsbane gjermom forbrermingskammeret for forbrerming av gasser og generering av varme og passasje av slike gasser og varme fra forbrermingskanmieret. En varmegjenvirmingsseksjon står i fluidforbindelse med forbrermingsseksjonen og har en yttervegg som danner et varmegjenvirmingskanmier. Minst et varmevekslingselement er anbrakt i varmegjenvirmingskanmieret med et irmløp for å motta en brenselreformeringsreaktant og et utløp for å føre oppvarmet reaktant ut av varmegjenvirmingsseksjonen. Forbrermingsseksjonen er forhøyet i forhold til varmegjenvirmingsseksjonen, slik at oppvarmede forbrermingsgasser blir flyttet ned i varmegjenvirmingsseksjonen. Forbrermings- og varmegjenvirmingsseksjonene har yttervegger som er kontinuerlige med hverandre for å danne et hus som fortrinnsvis er sylindriske. Huset har en irmvendig diameter på mindre erm 10 tommer eller har altemativt en lengde og en diameter i et forhold mellom omfrent 7:1 og omfrent 4:1. Fremgangsmåte for rask oppstart av brenselprosessoren ved hjelp av en slik prereformer er også tilveiebrakt og integrerte brenselprosessorer omfatter en brenselreformer og den beskrevne prereformer.
NO20055174A 2003-04-04 2005-11-03 Fremgangsmate og apparat for hurtig oppvarming av brenselnyformingsreaktanter NO20055174L (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/408,080 US7235217B2 (en) 2003-04-04 2003-04-04 Method and apparatus for rapid heating of fuel reforming reactants
PCT/US2004/009786 WO2004090075A2 (en) 2003-04-04 2004-03-30 Method and apparatus for rapid heating of fuel reforming reactants

Publications (2)

Publication Number Publication Date
NO20055174D0 NO20055174D0 (no) 2005-11-03
NO20055174L true NO20055174L (no) 2006-01-03

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NO20055174A NO20055174L (no) 2003-04-04 2005-11-03 Fremgangsmate og apparat for hurtig oppvarming av brenselnyformingsreaktanter

Country Status (13)

Country Link
US (1) US7235217B2 (no)
EP (1) EP1611221A4 (no)
JP (1) JP5015590B2 (no)
KR (1) KR101118825B1 (no)
CN (1) CN100519707C (no)
AU (1) AU2004227329B2 (no)
BR (1) BRPI0409144A (no)
CA (1) CA2521292C (no)
MX (1) MXPA05010579A (no)
MY (1) MY138396A (no)
NO (1) NO20055174L (no)
TW (1) TWI392543B (no)
WO (1) WO2004090075A2 (no)

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JP2006523603A (ja) 2006-10-19
AU2004227329A1 (en) 2004-10-21
AU2004227329B2 (en) 2010-10-07
NO20055174D0 (no) 2005-11-03
BRPI0409144A (pt) 2006-03-28
JP5015590B2 (ja) 2012-08-29
CN100519707C (zh) 2009-07-29
TWI392543B (zh) 2013-04-11
CA2521292A1 (en) 2004-10-21
MY138396A (en) 2009-05-29
WO2004090075A2 (en) 2004-10-21
US20040194384A1 (en) 2004-10-07
HK1090661A1 (zh) 2006-12-29
CA2521292C (en) 2012-01-03
CN1791663A (zh) 2006-06-21
WO2004090075A3 (en) 2005-01-27
MXPA05010579A (es) 2005-11-23
US7235217B2 (en) 2007-06-26
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