MX168335B - Aparato mejorado para la reformacion de combustible - Google Patents

Aparato mejorado para la reformacion de combustible

Info

Publication number
MX168335B
MX168335B MX198347A MX19834783A MX168335B MX 168335 B MX168335 B MX 168335B MX 198347 A MX198347 A MX 198347A MX 19834783 A MX19834783 A MX 19834783A MX 168335 B MX168335 B MX 168335B
Authority
MX
Mexico
Prior art keywords
catalyst
fuel
improved apparatus
reforming fuel
filled
Prior art date
Application number
MX198347A
Other languages
English (en)
Inventor
Miaso Yamamura
Kendichi Hisamatsu
Shozo Kaneko
Akira Hashimoto
Tokushi Maruta
Original Assignee
Mitsubishi Heavy Ind Ltd
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
Priority claimed from JP57140137A external-priority patent/JPS5930705A/ja
Priority claimed from JP20858082A external-priority patent/JPS59102803A/ja
Priority claimed from JP20857982A external-priority patent/JPS59102802A/ja
Priority claimed from JP20931082A external-priority patent/JPS59102804A/ja
Application filed by Mitsubishi Heavy Ind Ltd filed Critical Mitsubishi Heavy Ind Ltd
Publication of MX168335B publication Critical patent/MX168335B/es

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • 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
    • C01B3/32Production 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/06Chemical 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
    • B01J8/062Chemical 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 being installed in a furnace
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • 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)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

La presente invención se refiere a un aparato mejorado para la reformación de combustible, del tipo que incluye una pluralidad de tubos rellenos de catalizador, arreglados para calentarse a temperaturas elevadas, por un calentamiento desde el exterior, para así reformar al combustible a un gas que contiene hidrógeno como coponente principal, dicho combustible pasando através de cada tubo relleno de catalizador, caracterizado porque los tubos rellenos de catalizador se disponen en una capa fluidizada, de material no combustible y se tienen quemadores para calentar el lecho fluidizado.
MX198347A 1982-08-12 1983-08-10 Aparato mejorado para la reformacion de combustible MX168335B (es)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP57140137A JPS5930705A (ja) 1982-08-12 1982-08-12 燃料改質装置
JP20858082A JPS59102803A (ja) 1982-11-30 1982-11-30 燃料改質装置
JP20857982A JPS59102802A (ja) 1982-11-30 1982-11-30 燃料組成変換装置
JP20931082A JPS59102804A (ja) 1982-12-01 1982-12-01 燃料改質装置

Publications (1)

Publication Number Publication Date
MX168335B true MX168335B (es) 1993-05-17

Family

ID=27472285

Family Applications (1)

Application Number Title Priority Date Filing Date
MX198347A MX168335B (es) 1982-08-12 1983-08-10 Aparato mejorado para la reformacion de combustible

Country Status (6)

Country Link
CH (1) CH655495B (es)
DE (1) DE3329435A1 (es)
FR (1) FR2531944A1 (es)
GB (1) GB2126118B (es)
MX (1) MX168335B (es)
NL (1) NL189123C (es)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4557904A (en) * 1984-03-26 1985-12-10 Union Carbide Corporation Integral reactor apparatus
US4861348A (en) * 1986-10-08 1989-08-29 Hitachi, Ltd. Fuel reforming apparatus
GB2201903B (en) * 1987-03-03 1990-11-28 Shell Int Research Apparatus and process suitable for producing hydrogen
US4792436A (en) * 1987-05-08 1988-12-20 Kinetics Technology International Hydrocarbon converter furnace
US4966101A (en) * 1988-05-17 1990-10-30 Ube Industries, Ltd. Fluidized bed apparatus
FR2655350A1 (fr) * 1989-12-01 1991-06-07 Inst Francais Du Petrole Procede de production d'hydrocarbures aromatiques a partir d'une charge d'hydrocarbures aliphatiques dans un reacteur chauffe par un lit fluidise de particules.
DE69016952T2 (de) * 1989-12-01 1995-06-14 Inst Francais Du Petrol Verfahren und Apparat für die Umwandlung von aromatischen Kohlenwasserstoffen aus aliphatischen Kohlenwasserstoffeinsätzen in einem mit fluidisierten Teilchen geheizten Reaktor.
FR2655351B1 (fr) * 1989-12-01 1994-04-29 Inst Francais Du Petrole Dispositif de conversion d'hydrocarbures dans un reacteur chauffe par un lit fluidise de particules et son utilisation.
JP3839846B2 (ja) * 1994-11-17 2006-11-01 株式会社東芝 たて型触媒反応装置
DE19955676B4 (de) * 1999-11-19 2004-06-03 Uhde Gmbh Verfahren zur Herstellung von Synthesegas in Verbindung mit einer Druckwechsel-Adsorptionsanlage
US20030061764A1 (en) * 2001-10-01 2003-04-03 Belhocine Benallal Method and apparatus for steam reforming of hydrocarbons
DE102006046052B3 (de) * 2006-09-28 2008-03-27 Green Vision Holding B.V. Herausschiebbarer Dampfreformer
EP2314543A1 (en) * 2009-10-22 2011-04-27 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for reducing the capacity of a steam reformer and reduced-capacity reformer
EP3296255A1 (de) * 2016-09-14 2018-03-21 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Reformerrohr mit strukturiertem katalysator und verbessertem wärmehaushalt

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE674656A (es) * 1964-12-31 1966-06-30
JPS4930915B1 (es) * 1967-07-15 1974-08-16
US3980452A (en) * 1973-09-14 1976-09-14 Metallgesellschaft Aktiengesellschaft Process for supplying heat to chemical reactions
GB1579577A (en) * 1977-04-14 1980-11-19 Robinson L F Reforming of hydrocarbons
NZ194405A (en) * 1979-08-02 1982-05-25 Dut Pty Ltd Producing liquid hydrocarbon streams by hydrogenation of fossil-based feedstock

Also Published As

Publication number Publication date
GB8321739D0 (en) 1983-09-14
GB2126118B (en) 1986-09-10
NL189123B (nl) 1992-08-17
NL189123C (nl) 1993-01-18
CH655495B (es) 1986-04-30
DE3329435A1 (de) 1984-04-26
GB2126118A (en) 1984-03-21
NL8302824A (nl) 1984-03-01
FR2531944A1 (fr) 1984-02-24
FR2531944B1 (es) 1985-04-19

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