FR2380072A1 - Four tubulaire de dissociation - Google Patents

Four tubulaire de dissociation

Info

Publication number
FR2380072A1
FR2380072A1 FR7803589A FR7803589A FR2380072A1 FR 2380072 A1 FR2380072 A1 FR 2380072A1 FR 7803589 A FR7803589 A FR 7803589A FR 7803589 A FR7803589 A FR 7803589A FR 2380072 A1 FR2380072 A1 FR 2380072A1
Authority
FR
France
Prior art keywords
catalyst
proposed
process gas
tubular
cracking
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
FR7803589A
Other languages
English (en)
Other versions
FR2380072B1 (fr
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ght Hochtemperaturreak Tech
Original Assignee
Ght Hochtemperaturreak Tech
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
Application filed by Ght Hochtemperaturreak Tech filed Critical Ght Hochtemperaturreak Tech
Publication of FR2380072A1 publication Critical patent/FR2380072A1/fr
Application granted granted Critical
Publication of FR2380072B1 publication Critical patent/FR2380072B1/fr
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/50Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/56Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J15/00Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor
    • B01J15/005Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • 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
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132Tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • 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)
  • Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Materials Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Four tubulaire pour la dissociation catalytique de gaz à haute température dans de longs tubes chauffables de l'extérieur et munis d'un tube intérieur métallique. Dans chaque tube extérieur 1, le support de catalyseur se compose de surfaces à paroi mince 10 abordables des deux côtés par le courant du gaz à dissocier et disposées à peu près parallelement à l'axe des tubes extérieur 1 et interieur 5. L'invention est notamment applicable avec chauffage par des gaz de fumée ou de l'hélium à environ 950 degrés C, par exemple à panir d'un circuit de refroidissement de réacteur nucléaire.
FR7803589A 1977-02-09 1978-02-08 Four tubulaire de dissociation Granted FR2380072A1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19772705324 DE2705324A1 (de) 1977-02-09 1977-02-09 Spaltrohrofen

Publications (2)

Publication Number Publication Date
FR2380072A1 true FR2380072A1 (fr) 1978-09-08
FR2380072B1 FR2380072B1 (fr) 1980-05-16

Family

ID=6000694

Family Applications (1)

Application Number Title Priority Date Filing Date
FR7803589A Granted FR2380072A1 (fr) 1977-02-09 1978-02-08 Four tubulaire de dissociation

Country Status (4)

Country Link
JP (1) JPS5398908A (fr)
CH (1) CH627666A5 (fr)
DE (1) DE2705324A1 (fr)
FR (1) FR2380072A1 (fr)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0025308A1 (fr) * 1979-09-06 1981-03-18 Imperial Chemical Industries Plc Procédé et dispositif pour faire réagir catalytiquement de la vapeur avec des hydrocarbures dans des conditions endothermiques
EP0095748A2 (fr) * 1982-05-28 1983-12-07 Energy Research Corporation Reformeur de carburant
EP0124226A2 (fr) * 1983-03-25 1984-11-07 Imperial Chemical Industries Plc Reformage à la vapeur d'eau
WO1986003822A1 (fr) * 1984-12-15 1986-07-03 Luehr Wolfgang Installation pour la combustion catalytique, en particulier pour la postcombustion des gaz, gaz d'echappement, fumees ou substances combustibles analogues
EP0208929A1 (fr) * 1985-06-19 1987-01-21 BASF Aktiengesellschaft Construction d'un lit fixe catalytique par des corps du type nid d'abeille
WO1994023931A1 (fr) * 1993-04-08 1994-10-27 Christopher Green Procede et appareil de melange
WO2006051098A1 (fr) * 2004-11-12 2006-05-18 Shell Internationale Research Maatschappij B.V. Reacteur tubulaire avec garnissage

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2948107A1 (de) * 1979-11-29 1981-06-04 Didier Engineering Gmbh, 4300 Essen Vorrichtung zur erzeugung von nh (pfeil abwaerts)3(pfeil abwaerts) -synthesegas aus vorgereinigtem kokereigas
US4430304A (en) * 1981-11-13 1984-02-07 The United States Of America As Represented By The United States Department Of Energy Slab reformer
US4504447A (en) * 1981-11-13 1985-03-12 The United States Of America As Represented By The United States Department Of Energy Slab reformer
JPH0773673B2 (ja) * 1985-05-30 1995-08-09 久夫 小嶋 触媒反応装置
DE29722933U1 (de) * 1997-12-19 1998-02-12 Mannesmann AG, 40213 Düsseldorf Tiefschachtreaktor zur kontinuierlichen Durchführung chemischer Reaktionen
DE29722926U1 (de) * 1997-12-19 1998-02-19 Mannesmann AG, 40213 Düsseldorf Tiefschachtreaktor zur kontinuierlichen Durchführung chemischer Reaktionen
AU5386999A (en) * 1999-08-13 2001-03-13 Technip Kti S.P.A. Catalyst tubes for endothermic reaction especially for the production of hydrogen and syngas
NL1036644C2 (en) 2009-02-27 2010-08-30 Green Vision Holding B V Steam reformer.

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2190903A1 (fr) * 1972-06-30 1974-02-01 Foster Wheeler Corp

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2190903A1 (fr) * 1972-06-30 1974-02-01 Foster Wheeler Corp

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0025308A1 (fr) * 1979-09-06 1981-03-18 Imperial Chemical Industries Plc Procédé et dispositif pour faire réagir catalytiquement de la vapeur avec des hydrocarbures dans des conditions endothermiques
EP0095748A2 (fr) * 1982-05-28 1983-12-07 Energy Research Corporation Reformeur de carburant
EP0095748A3 (fr) * 1982-05-28 1985-06-12 Energy Research Corporation Reformeur de carburant
EP0124226A2 (fr) * 1983-03-25 1984-11-07 Imperial Chemical Industries Plc Reformage à la vapeur d'eau
EP0124226A3 (en) * 1983-03-25 1987-03-25 Imperial Chemical Industries Plc Steam reforming
WO1986003822A1 (fr) * 1984-12-15 1986-07-03 Luehr Wolfgang Installation pour la combustion catalytique, en particulier pour la postcombustion des gaz, gaz d'echappement, fumees ou substances combustibles analogues
EP0208929A1 (fr) * 1985-06-19 1987-01-21 BASF Aktiengesellschaft Construction d'un lit fixe catalytique par des corps du type nid d'abeille
US4859642A (en) * 1985-06-19 1989-08-22 Basf Aktiengesellschaft Fixed-bed catalyst structure obtained using honeycomb elements
WO1994023931A1 (fr) * 1993-04-08 1994-10-27 Christopher Green Procede et appareil de melange
WO2006051098A1 (fr) * 2004-11-12 2006-05-18 Shell Internationale Research Maatschappij B.V. Reacteur tubulaire avec garnissage

Also Published As

Publication number Publication date
JPS5398908A (en) 1978-08-29
CH627666A5 (en) 1982-01-29
DE2705324A1 (de) 1978-08-10
FR2380072B1 (fr) 1980-05-16

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Legal Events

Date Code Title Description
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