AR245488A1 - Procedimiento para la reformacion de hidrocarburos por vapor y reactor para llevarlo a cabo. - Google Patents

Procedimiento para la reformacion de hidrocarburos por vapor y reactor para llevarlo a cabo.

Info

Publication number
AR245488A1
AR245488A1 AR86303430A AR30343086A AR245488A1 AR 245488 A1 AR245488 A1 AR 245488A1 AR 86303430 A AR86303430 A AR 86303430A AR 30343086 A AR30343086 A AR 30343086A AR 245488 A1 AR245488 A1 AR 245488A1
Authority
AR
Argentina
Prior art keywords
gas
steam
catalyst
hot combustion
reformation
Prior art date
Application number
AR86303430A
Other languages
English (en)
Original Assignee
Haldor Topsoe As
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=8102918&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=AR245488(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Haldor Topsoe As filed Critical Haldor Topsoe As
Application granted granted Critical
Publication of AR245488A1 publication Critical patent/AR245488A1/es

Links

Classifications

    • 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
    • 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
    • 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
    • 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
    • B01J8/04—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 the fluid passing successively through two or more beds
    • B01J8/0446—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0461—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds
    • B01J8/0465—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds the beds being concentric
    • 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
    • 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
    • B01J8/04—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 the fluid passing successively through two or more beds
    • B01J8/0492—Feeding reactive fluids
    • 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
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • 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
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • C01B2203/0816—Heating by flames
    • 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
    • C01B2203/0838—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel
    • C01B2203/0844—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel the non-combustive exothermic reaction being another reforming reaction as defined in groups C01B2203/02 - C01B2203/0294
    • 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

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)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

UN PROCEDIMIENTO PARA LA REFORMACION DE HIDROCARBUROS POR VAPOR, EN UN REACTOR DE REFORMACION DE HIDROCARBUROS PARA FORMAR UNA CORRIENTE DE PRODUCTO RICA EN HIDROGENO, QUE COMPRENDE HACER PASAR UNA CORRIENTE DE ALIMENTACION QUE COMPRENDE VAPOR Y UNO O MAS HIDROCARBUROS COMO GAS DE PROCESAMIENTO BAJO CONDICIONES DE REFORMACION POR VAPOR A TRAVES DE UN VOLUMEN DETERMINADO DE CATALIZADOR REFORMADOR POR VAPOR BAJO ALIMENTACION EXTERNA DEL CALOR PARA ASEGURAR UNA TEMPERATURA DESDE 350 HASTA 600*C A LA ENTRADA DEL CATALIZADOR, SIENDO LA RELACION DE VAPOR A CARBONO EN LA CORRIENTE DEALIMENTACION DESDE 1,1:1 A 7:1, COMPRENDE (A) HACER PASAR PRIMERO EL GAS DE PROCESAMIENTO A TRAVES DE UNA PRIMERA PORCION DEL CATALIZADOR DE REFORMACION POR VAPOR QUE CONSTITUYE 25-75% DEL MISMO, EL CALOR NECESARIO PARA LAS REACCIONES ENDOTERMICAS QUE OCURREN EN EL GAS DE PROCESAMIENTO Y PARA CALENTAR EL GAS DE PROCESAMIENTO QUE ES SUMINISTRADO EN PARTE DESDE UN GAS DE COMBUSTION MODERAMENTE CALIENTE TAL COMO SE HA DEFINIDO BAJO (B) Y EN PARTE DESDE LA CORRIENTE DE PRODUCTO, Y (B) HACER PASAR EL GAS DE PROCESAMIENTO REFORMADO EN LA ETAPA (A) A TRAVES DE LA PORCION REMANENTE DELCATALIZADOR SIENDO SUMINISTRADO EL CALOR NECESARIO PARA LAS REACCIONES ENDOTERMICAS ADICIONALES Y EL CALENTAMIENTO DEL GAS DE PROCESAMIENTO, POR UN GAS DE COMBUSTION CALIENTE GENERADO POR LA COMBUSTION DE UN COMBUSTIBLE FLUIDO, ENFRIANDOSE POR LO TANTO EL GAS DE COMBUSTION CALIENTE PARA FORMAR EL GAS DE COMBUSTION MODERAMENTE CALIENTE EMPLEADO EN LA ETAPA (A).
AR86303430A 1985-03-21 1986-03-19 Procedimiento para la reformacion de hidrocarburos por vapor y reactor para llevarlo a cabo. AR245488A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DK126685A DK165946C (da) 1985-03-21 1985-03-21 Reformingproces under varmeudveksling og reaktor dertil

Publications (1)

Publication Number Publication Date
AR245488A1 true AR245488A1 (es) 1994-01-31

Family

ID=8102918

Family Applications (1)

Application Number Title Priority Date Filing Date
AR86303430A AR245488A1 (es) 1985-03-21 1986-03-19 Procedimiento para la reformacion de hidrocarburos por vapor y reactor para llevarlo a cabo.

Country Status (11)

Country Link
US (2) US4678600A (es)
EP (1) EP0195688B1 (es)
JP (1) JPH0798642B2 (es)
AR (1) AR245488A1 (es)
AU (1) AU579227B2 (es)
CA (1) CA1261629A (es)
DE (2) DE3674609D1 (es)
DK (1) DK165946C (es)
ES (1) ES8800881A1 (es)
GR (1) GR860763B (es)
NO (1) NO170535C (es)

Families Citing this family (54)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4692306A (en) * 1986-03-24 1987-09-08 Kinetics Technology International Corporation Catalytic reaction apparatus
GB8609099D0 (en) * 1986-04-15 1986-05-21 British Petroleum Co Plc Production of synthesis gas
CH670052A5 (es) * 1986-05-23 1989-05-12 Silberring Ludwig Ingbuero
JPH0642940B2 (ja) * 1987-03-31 1994-06-08 東洋エンジニアリング株式会社 気体吸熱反応用装置
JPH01122901A (ja) * 1987-11-05 1989-05-16 Osaka Gas Co Ltd 水素富化ガス製造用改質器の反応管
GB8728882D0 (en) * 1987-12-10 1988-01-27 Ici Plc Hydrogen
DK159963C (da) * 1988-07-01 1991-06-03 Haldor Topsoe As Fremgangsmaade til fremstilling af ammoniak
US5164163A (en) * 1988-09-19 1992-11-17 Kabushiki Kaisha Kobe Seiko Sho Hydrocarbon reforming apparatus
IT1224600B (it) * 1988-11-10 1990-10-04 Kinetics Technology Apparato per la produzione di idrogeno e gas di sintesi mediante reforming di idrocarburi che utilizza una barriera metallica per il controllo della temperatura di pelle del tubo catalitico
IT1232200B (it) * 1989-01-24 1992-01-28 Kinetics Technology Reattore catalitico isotermo per reazioni endotermiche
US5002752A (en) * 1989-06-09 1991-03-26 Gas Research Institute Process for hydroforming hydrocarbon liquids
US4929585A (en) * 1989-06-09 1990-05-29 Gas Research Institute Mixed-solid solution tri-metallic oxide/sulfide catalyst and process for its preparation
JPH0333002A (ja) * 1989-06-29 1991-02-13 Hitachi Ltd 水素製造装置
JPH03232703A (ja) * 1989-12-26 1991-10-16 Tokyo Electric Power Co Inc:The 炭化水素の改質装置
DK167864B1 (da) * 1990-02-02 1993-12-27 Topsoe Haldor As Fremgangsmaade og reaktorsystem til reforming af carbonhydrider under varmeveksling
DK171830B1 (da) * 1995-01-20 1997-06-23 Topsoe Haldor As Fremgangsmåde til generering af elektrisk energi
US5733347A (en) * 1995-12-27 1998-03-31 International Fuel Cells Corp. Compact fuel gas reformer assemblage
DE69800734T2 (de) * 1997-01-22 2001-08-09 Haldor Topsoee A/S, Lyngby Erzeugung eines Synthesegases durch Dampfreformierung unter Verwendung eines katalysierten Hardware
DE19828777A1 (de) * 1998-06-27 1999-12-30 Krupp Uhde Gmbh Vorrichtung zur Durchführung katalytischer chemischer Reaktionen eines Fluids in der Gasphase
US6641625B1 (en) 1999-05-03 2003-11-04 Nuvera Fuel Cells, Inc. Integrated hydrocarbon reforming system and controls
US6284217B1 (en) * 1999-08-17 2001-09-04 Battelle Memorial Institute Method and catalyst structure for steam reforming of a hydrocarbon
US7335346B2 (en) * 1999-08-17 2008-02-26 Battelle Memorial Institute Catalyst and method of steam reforming
US6607678B2 (en) 1999-08-17 2003-08-19 Battelle Memorial Institute Catalyst and method of steam reforming
DE19953233A1 (de) * 1999-11-04 2001-05-10 Grigorios Kolios Autotherme Reaktorschaltungen zur direkten Kopplung endothermer und exothermer Reaktionen
ATE302736T1 (de) * 2000-09-20 2005-09-15 Air Prod & Chem Vorrichtung und verfahren zur reformierung von kohlenwasserstoff
AU2002211388A1 (en) 2000-10-02 2002-04-15 Chevron U.S.A. Inc. Process for reducing coke formation in hydrocarbon processing by application of radio frequency electromagnetic radiation
US6967063B2 (en) 2001-05-18 2005-11-22 The University Of Chicago Autothermal hydrodesulfurizing reforming method and catalyst
DE60222123T2 (de) * 2001-06-04 2007-12-20 Tokyo Gas Co. Ltd. Zylinderförmige wasserdampfreformierungseinheit
WO2003056642A2 (en) * 2001-12-21 2003-07-10 Nuvera Fuel Cells, Inc. Fuel processor modules integration into common housing
US6793700B2 (en) * 2002-01-14 2004-09-21 Air Products And Chemicals, Inc. Apparatus and method for production of synthesis gas using radiant and convective reforming
AU2003219821A1 (en) * 2002-02-22 2003-09-09 Chevron U.S.A. Inc. Process for reducing metal catalyzed coke formation in hydrocarbon processing
DE10209886A1 (de) * 2002-03-04 2003-09-25 Fraunhofer Ges Forschung Vorrichtung sowie Verfahren zur Reformierung von Kohlenwasserstoffen aus einem Einsatzgas
DE10213891B4 (de) * 2002-03-28 2014-02-27 Robert Bosch Gmbh Vorrichtung zur Umformung eines kohlenwasserstoffhaltigen Stoffstroms
EP1403215B1 (en) * 2002-09-26 2013-03-13 Haldor Topsoe A/S Process and apparatus for the preparation of synthesis gas
EP1403217A1 (en) * 2002-09-26 2004-03-31 Haldor Topsoe A/S Process and apparatus for the preparation of synthesis gas
EP1413547A1 (en) 2002-09-26 2004-04-28 Haldor Topsoe A/S Process for the production of synthesis gas
US8277773B2 (en) 2004-02-13 2012-10-02 Velocys Corp. Steam reforming method
US20040266615A1 (en) * 2003-06-25 2004-12-30 Watson Junko M. Catalyst support and steam reforming catalyst
US20050132648A1 (en) * 2003-11-27 2005-06-23 Kyocera Corporation Fuel reformer housing container and fuel reforming apparatus
US6948656B2 (en) * 2003-12-23 2005-09-27 First Data Corporation System with GPS to manage risk of financial transactions
US7320778B2 (en) * 2004-07-21 2008-01-22 Catacel Corp. High-performance catalyst support
US7472936B2 (en) * 2005-04-14 2009-01-06 Catacel Corp. Tool for insertion and removal of a catalytic reactor cartridge
US20060230613A1 (en) * 2005-04-14 2006-10-19 Catacel Corporation Catalytic reactor cartridge
US7565743B2 (en) * 2005-04-14 2009-07-28 Catacel Corp. Method for insertion and removal of a catalytic reactor cartridge
US7682580B2 (en) * 2005-05-19 2010-03-23 Catacel Corp. Catalytic reactor having radial leaves
US7501102B2 (en) * 2005-07-28 2009-03-10 Catacel Corp. Reactor having improved heat transfer
DE102006019409B4 (de) * 2006-04-23 2010-02-04 Zentrum für Brennstoffzellen-Technik GmbH Reformer-Reaktor, seine Verwendung und Verfahren zum Betrieb des Reformers
US7622087B2 (en) * 2006-11-16 2009-11-24 H2Gen Innovations, Inc. Reactor air supply system and burner configuration
US20130195735A1 (en) * 2012-02-01 2013-08-01 Delphi Technologies, Inc. Heat exchanger reformer with thermal expansion management
KR101361698B1 (ko) 2012-06-01 2014-02-11 충북대학교 산학협력단 연소기와 개질기가 일체로 복합된 연료전지 시스템
CN103466546B (zh) * 2013-09-06 2015-04-15 清华大学 一种将双功能吸附剂应用于吸附增强式水蒸气重整和水气变换反应的中温变压吸附方法
GB201813431D0 (en) 2018-08-17 2018-10-03 Weedon Geoffrey Gerald Process & apparatus for steam reforming
EP3900820A1 (en) * 2020-09-21 2021-10-27 Haldor Topsøe A/S Double tubes combined heat exchanger and steam reformer reactor comprising two types of catalyst beds
GB202202363D0 (en) * 2022-02-22 2022-04-06 Johnson Matthey Davy Technologies Ltd Reactor

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH389809A (de) * 1960-07-27 1965-03-31 Didier Werke Ag Vorrichtung zum Umformen gasförmiger oder flüssiger Kohlenwasserstoffe oder Gemischen von gasförmigen und flüssigen Kohlenwasserstoffen
US3144312A (en) * 1961-06-06 1964-08-11 Mertens Carl Catalytic conversion plant for the continuous generation of gases of any kind out of ydrocarbons
US3446594A (en) * 1965-08-03 1969-05-27 United Aircraft Corp Method for generating hydrogen from liquid hydrogen-containing feedstocks
DE1667573B2 (de) * 1967-08-10 1976-10-21 Krupp-Koppers Gmbh, 4300 Essen Verfahren und vorrichtung zur erzeugung eines wasserstoffreichen gases durch spaltung eines gemisches aus gasfoermigen und/oder fluessigen kohlenwasserstoffen und wasserdampf
GB1247338A (en) * 1967-10-13 1971-09-22 Power Gas Ltd Steam reforming of hydrocarbons
US3909299A (en) * 1973-10-01 1975-09-30 United Technologies Corp Fuel cell system including reform reactor
DE3244252A1 (de) * 1982-11-30 1984-05-30 Uhde Gmbh, 4600 Dortmund Verfahren und vorrichtung zur erzeugung von produktgas mit wasserstoff- und kohlenoxyde-gehalten
DE3480192D1 (en) * 1983-03-25 1989-11-23 Ici Plc Steam reforming
JPH0669881B2 (ja) * 1984-11-26 1994-09-07 日揮株式会社 炭化水素の水蒸気改質法

Also Published As

Publication number Publication date
NO861106L (no) 1986-09-22
DE195688T1 (de) 1987-03-19
ES8800881A1 (es) 1987-12-01
EP0195688A2 (en) 1986-09-24
DK126685A (da) 1986-09-22
GR860763B (en) 1986-07-21
EP0195688A3 (en) 1988-08-24
US4678600A (en) 1987-07-07
AU579227B2 (en) 1988-11-17
CA1261629A (en) 1989-09-26
DE3674609D1 (de) 1990-11-08
AU5494886A (en) 1986-09-25
DK126685D0 (da) 1985-03-21
ES553213A0 (es) 1987-12-01
EP0195688B1 (en) 1990-10-03
DK165946B (da) 1993-02-15
US4830834A (en) 1989-05-16
JPH0798642B2 (ja) 1995-10-25
DK165946C (da) 1993-07-05
JPS61222904A (ja) 1986-10-03
NO170535B (no) 1992-07-20
NO170535C (no) 1992-10-28

Similar Documents

Publication Publication Date Title
AR245488A1 (es) Procedimiento para la reformacion de hidrocarburos por vapor y reactor para llevarlo a cabo.
US4642272A (en) Integrated fuel cell and fuel conversion apparatus
KR101210684B1 (ko) 수소 리사이클형 ｍｃｆｃ 발전 시스템
JP5252795B2 (ja) 燃料加工法およびシステム
US20030110693A1 (en) Production enhancement for a reactor
ES2057936T3 (es) Procedimiento de reformado autotermico con vapor de agua.
NO20023081D0 (no) Fremgangsmåte og apparat til å oppnå forbedret produktivitet under termiske kjemiske reaksjoner
DK162935B (da) Apparat til fremstilling af produktgas med indhold af hydrogen og carbonoxider
JPS61247601A (ja) 炭化水素燃料処理装置
CN111344249A (zh) 氢产生装置
RU2261756C2 (ru) Способ и реактор для проведения неадиабатических каталитических реакций
MX168297B (es) Procedimiento para la preparacion de un gas reductor
US9738518B2 (en) Reformer reactor and method for converting hydrocarbon fuels into hydrogen rich gas
JP5078165B2 (ja) 水蒸気改質ユニット
JPWO2004071951A1 (ja) 水素生成装置及び燃料電池発電システム
KR101846969B1 (ko) 연료 개질 장치
TWI626784B (zh) 氣體燃料重組裝置及其發電整合系統
BR112020015822A2 (pt) Operação unitária dentro de um sistema para gerar gás de síntese, e, sistema integrado para gerar gás de síntese.
JPH08301601A (ja) メタノール改質器
JP2009173479A (ja) 熱交換器及び複合型燃料反応器
KR20240028346A (ko) 암모니아로부터 수소를 생산하는 방법 및 장치
RU2001107419A (ru) Способ получения текучего теплоносителя, используемого в качестве косвенного источника тепла при проведении эндотермических реакций
JPH04320999A (ja) 高温ガス炉による水素ガス製造装置
GB1159247A (en) Steam Reforming of Hydrocarbons
GB991523A (en) Production of hydrogen-containing gases particularly useful for ammonia synthesis