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NO961114L - Catalytic reactor for endothermic reactions - Google Patents

Catalytic reactor for endothermic reactions

Info

Publication number
NO961114L
NO961114L NO961114A NO961114A NO961114L NO 961114 L NO961114 L NO 961114L NO 961114 A NO961114 A NO 961114A NO 961114 A NO961114 A NO 961114A NO 961114 L NO961114 L NO 961114L
Authority
NO
Norway
Prior art keywords
housing
catalytic reactor
burners
catalyst
endothermic reactions
Prior art date
Application number
NO961114A
Other languages
Norwegian (no)
Other versions
NO961114D0 (en
Inventor
Francesco Giacobbe
Original Assignee
Mannesmann Ag
Kti Group Bv
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 Mannesmann Ag, Kti Group Bv filed Critical Mannesmann Ag
Publication of NO961114L publication Critical patent/NO961114L/en
Publication of NO961114D0 publication Critical patent/NO961114D0/en

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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • B01J8/062—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 in tube reactors; the solid particles being arranged in tubes being installed in a furnace
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00477—Controlling the temperature by thermal insulation means
    • B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • 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
    • 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
    • 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)
  • Combustion & Propulsion (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Catalysts (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Oppfinnelsen vedrører en katalytisk reaktor for endoterme reaksjoner. Katalysatoren befinner seg i et av ildfast materiale dannet hus (13), hvorved det i husets (13) indre er anordnet minst en rørformet katalysatorbeholder (10). For å oppnå en katalytisk reaktor, hvorved en termisk beskadigelse av reaktorbeholderen unngås, uten at det kreves kostbare konstruksjonstiltak eller uønskede økninger av avgassmengdene samt ulemper ved energiutnyttelsen av brennstoffet som benyttes, foreslås det ifølge oppfinnelsen at det i huset (13) er anordnet flere katalysatorbeholdere (10) som hver står i avstand fra hverandre, at det i huset (13) er anordnet flere brennere (15) slik at katalysator- beholderne (10) ligger mellom brennerne (15) og at de respektive brennemes (15) flammeområde ligger i området for varmefordeleren (16) for å sikre en ikke adiabatisk forbrenning.The invention relates to a catalytic reactor for endothermic reactions. The catalyst is located in a housing (13) formed of refractory material, whereby at least one tubular catalyst vessel (10) is arranged in the interior of the housing (13). In order to obtain a catalytic reactor, thereby avoiding thermal damage to the reactor vessel, without requiring costly structural measures or undesirable increases in the exhaust gas volumes and disadvantages of the energy utilization of the fuel used, it is proposed according to the invention that several catalysts be arranged in the housing (13). (10), each spaced apart from each other, arranged in the housing (13) several burners (15) so that the catalyst containers (10) lie between the burners (15) and that the flame area of the respective burners (15) lies in the area of the heat distributor (16) to ensure non-adiabatic combustion.

NO961114A 1993-10-29 1996-03-19 Catalytic reactor for endothermic reactions NO961114D0 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITRM930719A IT1261857B (en) 1993-10-29 1993-10-29 IMPROVEMENT IN CATALYTIC REACTORS FOR ENDOTHERMAL REACTIONS, IN PARTICULAR FOR THE PRODUCTION OF HYDROGEN.
PCT/DE1994/001293 WO1995011745A1 (en) 1993-10-29 1994-10-26 Catalytic reactor for endothermic reactions

Publications (2)

Publication Number Publication Date
NO961114L true NO961114L (en) 1996-03-19
NO961114D0 NO961114D0 (en) 1996-03-19

Family

ID=11402031

Family Applications (1)

Application Number Title Priority Date Filing Date
NO961114A NO961114D0 (en) 1993-10-29 1996-03-19 Catalytic reactor for endothermic reactions

Country Status (16)

Country Link
EP (1) EP0725675B1 (en)
JP (1) JPH09503961A (en)
CN (1) CN1133570A (en)
AT (1) ATE152003T1 (en)
AU (1) AU8057094A (en)
BR (1) BR9407895A (en)
CA (1) CA2175236A1 (en)
CZ (1) CZ117696A3 (en)
DE (1) DE59402559D1 (en)
DK (1) DK0725675T3 (en)
ES (1) ES2100745T3 (en)
FI (1) FI961746A0 (en)
GR (1) GR3023315T3 (en)
IT (1) IT1261857B (en)
NO (1) NO961114D0 (en)
WO (1) WO1995011745A1 (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1283877B1 (en) * 1996-01-12 1998-05-07 Kinetics Technology ISOTHERMAL CATALYTIC REACTOR FOR HIGH TEMPERATURE ENDOTHERMIC REACTIONS
EP0911076A1 (en) * 1997-10-23 1999-04-28 Haldor Topsoe A/S Reformer furnace with internal recirculation
DE60112861T2 (en) * 2000-09-20 2006-07-13 Air Products And Chemicals, Inc. Apparatus and process for hydrocarbon reforming
JP2002274807A (en) * 2001-03-14 2002-09-25 Osaka Gas Co Ltd Multitubular reaction apparatus
JP2007091584A (en) 2005-09-27 2007-04-12 Samsung Sdi Co Ltd Fuel reformer
FR2961117B1 (en) * 2010-06-11 2012-06-08 Inst Francais Du Petrole REACTOR EXCHANGER TUBES BAIONNETTES AND A TUBE OF SMOKE SUSPENDED TO THE SUPERIOR REACTOR OF THE REACTOR
ES2738389T3 (en) * 2016-08-02 2020-01-22 Air Liquide Device for endothermic process with improved tube arrangement
DK3532430T3 (en) 2016-10-25 2020-07-27 Technip France CATALYST PIPE FOR REFORM
KR101898788B1 (en) * 2016-12-30 2018-09-13 주식회사 두산 Apparatus for processing fuel
KR20220052909A (en) 2019-06-28 2022-04-28 테크니프 에너지스 프랑스 Method of loading catalyst tube assembly into tubular reactor and catalyst tube assembly for tubular reactor
EP4244182A1 (en) 2020-11-13 2023-09-20 Technip Energies France A process for producing a hydrogen-comprising product gas from a hydrocarbon
EP4105170A1 (en) 2021-06-18 2022-12-21 Technip Energies France Process and plant for flexible production of syngas from hydrocarbons
EP4279446B1 (en) 2022-05-17 2024-04-17 Technip Energies France Plant and process for producing hydrogen from hydrocarbons
EP4279445B1 (en) 2022-05-17 2024-04-17 Technip Energies France Plant and process for producing and separating syngas
CN116199185B (en) * 2023-05-06 2023-07-18 浙江百能科技有限公司 High-temperature catalytic hydrogen production reaction system and method by utilizing waste water in coal grading manner

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4847051A (en) * 1988-03-21 1989-07-11 International Fuel Cells Corporation Reformer tube heat transfer device
JPH0631323B2 (en) * 1988-09-30 1994-04-27 三井造船株式会社 Decomposition furnace
IT1224600B (en) * 1988-11-10 1990-10-04 Kinetics Technology APPARATUS FOR THE PRODUCTION OF HYDROGEN AND SYNTHESIS GAS BY HYDROCARBON REFORMING THAT USES A METALLIC BARRIER FOR THE CONTROL OF THE SKIN TEMPERATURE OF THE CATALYTIC TUBE

Also Published As

Publication number Publication date
DK0725675T3 (en) 1997-08-25
JPH09503961A (en) 1997-04-22
CN1133570A (en) 1996-10-16
ITRM930719A0 (en) 1993-10-29
DE59402559D1 (en) 1997-05-28
FI961746A7 (en) 1996-04-23
IT1261857B (en) 1996-06-03
ES2100745T3 (en) 1997-06-16
BR9407895A (en) 1996-11-19
ITRM930719A1 (en) 1995-04-29
WO1995011745A1 (en) 1995-05-04
EP0725675B1 (en) 1997-04-23
EP0725675A1 (en) 1996-08-14
FI961746A0 (en) 1996-04-23
CA2175236A1 (en) 1995-05-04
AU8057094A (en) 1995-05-22
ATE152003T1 (en) 1997-05-15
CZ117696A3 (en) 1996-09-11
GR3023315T3 (en) 1997-08-29
NO961114D0 (en) 1996-03-19

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