NO961114L - Catalytic reactor for endothermic reactions - Google Patents
Catalytic reactor for endothermic reactionsInfo
- 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
Links
- 230000003197 catalytic effect Effects 0.000 title abstract 3
- 238000006243 chemical reaction Methods 0.000 title abstract 2
- 239000003054 catalyst Substances 0.000 abstract 4
- 238000002485 combustion reaction Methods 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 239000011819 refractory material Substances 0.000 abstract 1
- 230000003685 thermal hair damage Effects 0.000 abstract 1
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)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (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)
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.
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 |
---|---|
NO961114D0 NO961114D0 (en) | 1996-03-19 |
NO961114L true NO961114L (en) | 1996-03-19 |
Family
ID=11402031
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO961114A NO961114L (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) | NO961114L (en) |
WO (1) | WO1995011745A1 (en) |
Families Citing this family (14)
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 |
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 reforming apparatus |
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 |
DK3279561T3 (en) * | 2016-08-02 | 2019-07-29 | Air Liquide | DEVICE FOR ENDOTERMIC PROCESS WITH IMPROVED PIPE DEVICE |
WO2018077969A1 (en) | 2016-10-25 | 2018-05-03 | Technip France | Catalyst tube for reforming |
KR101898788B1 (en) * | 2016-12-30 | 2018-09-13 | 주식회사 두산 | Apparatus for processing fuel |
JP2022540802A (en) | 2019-06-28 | 2022-09-20 | テクニップ エナジーズ フランス | Method of incorporating a catalyst tube assembly into a tubular reactor and catalyst tube assembly for a tubular reactor |
AU2021379842A1 (en) | 2020-11-13 | 2023-06-29 | 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 |
EP4279445B1 (en) | 2022-05-17 | 2024-04-17 | Technip Energies France | Plant and process for producing and separating syngas |
EP4279446B1 (en) | 2022-05-17 | 2024-04-17 | Technip Energies France | Plant and process for producing hydrogen from hydrocarbons |
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)
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 |
-
1993
- 1993-10-29 IT ITRM930719A patent/IT1261857B/en active IP Right Grant
-
1994
- 1994-10-26 DK DK94931507.1T patent/DK0725675T3/en active
- 1994-10-26 AT AT94931507T patent/ATE152003T1/en not_active IP Right Cessation
- 1994-10-26 AU AU80570/94A patent/AU8057094A/en not_active Abandoned
- 1994-10-26 CN CN94193908.1A patent/CN1133570A/en active Pending
- 1994-10-26 EP EP94931507A patent/EP0725675B1/en not_active Expired - Lifetime
- 1994-10-26 ES ES94931507T patent/ES2100745T3/en not_active Expired - Lifetime
- 1994-10-26 WO PCT/DE1994/001293 patent/WO1995011745A1/en not_active Application Discontinuation
- 1994-10-26 BR BR9407895A patent/BR9407895A/en not_active Application Discontinuation
- 1994-10-26 CZ CZ961176A patent/CZ117696A3/en unknown
- 1994-10-26 CA CA002175236A patent/CA2175236A1/en not_active Abandoned
- 1994-10-26 JP JP7512355A patent/JPH09503961A/en active Pending
- 1994-10-26 DE DE59402559T patent/DE59402559D1/en not_active Expired - Lifetime
-
1996
- 1996-03-19 NO NO961114A patent/NO961114L/en unknown
- 1996-04-23 FI FI961746A patent/FI961746A0/en not_active Application Discontinuation
-
1997
- 1997-05-02 GR GR970400973T patent/GR3023315T3/en unknown
Also Published As
Publication number | Publication date |
---|---|
NO961114D0 (en) | 1996-03-19 |
DE59402559D1 (en) | 1997-05-28 |
CZ117696A3 (en) | 1996-09-11 |
IT1261857B (en) | 1996-06-03 |
GR3023315T3 (en) | 1997-08-29 |
ITRM930719A1 (en) | 1995-04-29 |
EP0725675A1 (en) | 1996-08-14 |
ATE152003T1 (en) | 1997-05-15 |
ITRM930719A0 (en) | 1993-10-29 |
FI961746A (en) | 1996-04-23 |
AU8057094A (en) | 1995-05-22 |
CN1133570A (en) | 1996-10-16 |
JPH09503961A (en) | 1997-04-22 |
ES2100745T3 (en) | 1997-06-16 |
WO1995011745A1 (en) | 1995-05-04 |
DK0725675T3 (en) | 1997-08-25 |
CA2175236A1 (en) | 1995-05-04 |
FI961746A0 (en) | 1996-04-23 |
EP0725675B1 (en) | 1997-04-23 |
BR9407895A (en) | 1996-11-19 |
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