SE7713225L - COMPACT CATALYTIC REACTION EQUIPMENT WITH SEVERAL ROWS - Google Patents
COMPACT CATALYTIC REACTION EQUIPMENT WITH SEVERAL ROWSInfo
- Publication number
- SE7713225L SE7713225L SE7713225A SE7713225A SE7713225L SE 7713225 L SE7713225 L SE 7713225L SE 7713225 A SE7713225 A SE 7713225A SE 7713225 A SE7713225 A SE 7713225A SE 7713225 L SE7713225 L SE 7713225L
- Authority
- SE
- Sweden
- Prior art keywords
- combustion chamber
- furnace
- reactors
- wall arrangement
- catalytic reaction
- Prior art date
Links
Classifications
-
- 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
-
- 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
- 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
Abstract
The reactor installation (10) has a furnace (12) which delivers heat for an endothermic reaction. This furnace (12) has a part having elevated heating output and a wall arrangement (89) which delimits a combustion chamber (60). The furnace (12) has an outlet device (103). Means (16, 18) are assigned to the combustion chamber (60) which introduce the fuel (16) and an oxidant (18) into the combustion chamber (60). The installation (10) has a plurality of tubular reactors (20) which are arranged at least almost in the tightest packing and which are arranged within the furnace (12) and each of which has a first part (56) arranged within the combustion chamber (60) and a second part (58). The latter is arranged within the furnace part having elevated heating output, this oven part being provided with an inlet apparatus (104), which is in gas connection to the combustion chamber (60), and an outlet apparatus (67), which is in gas connection with the outlet device (103). Shield devices (90) arranged within the combustion chamber (60) are provided for reducing the temperature differences among the reactors (20). These shield devices (90) are arranged between the combustion chamber wall arrangement (89) and the reactors (20) adjacent to this wall arrangement (89), in order to reduce the radiant heating of the first parts (56) of the reactors (20) which are adjacent to the wall arrangement (89). This compact catalytic reactor installation simultaneously has a higher life expectancy and operates extremely efficiently. <IMAGE>
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US75333576A | 1976-12-22 | 1976-12-22 | |
US05/827,803 US4098587A (en) | 1976-12-22 | 1977-08-25 | Compact multi-tube catalytic reaction apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
SE7713225L true SE7713225L (en) | 1978-06-23 |
SE423895B SE423895B (en) | 1982-06-14 |
Family
ID=27115728
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE7713225A SE423895B (en) | 1976-12-22 | 1977-11-23 | COMPACT CATALYTIC REACTION EQUIPMENT WITH MULTIPLE PIPES FOR MANUFACTURING GAS PRODUCTS FROM HYDRAULIC FUEL |
Country Status (13)
Country | Link |
---|---|
JP (1) | JPS5379768A (en) |
AU (1) | AU509038B2 (en) |
BR (1) | BR7707896A (en) |
CH (1) | CH625827A5 (en) |
DE (1) | DE2751308A1 (en) |
DK (1) | DK514377A (en) |
ES (1) | ES464566A1 (en) |
FR (1) | FR2374947A1 (en) |
GB (1) | GB1564995A (en) |
IL (1) | IL53404A (en) |
IT (1) | IT1089105B (en) |
NL (1) | NL7712715A (en) |
SE (1) | SE423895B (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5735935A (en) * | 1980-08-11 | 1982-02-26 | Mitsui Toatsu Chem Inc | Heat-absorptive reactor |
JPS63162503A (en) * | 1986-12-25 | 1988-07-06 | Toyo Eng Corp | Gas producer |
US5164163A (en) * | 1988-09-19 | 1992-11-17 | Kabushiki Kaisha Kobe Seiko Sho | Hydrocarbon reforming apparatus |
JPH03232703A (en) * | 1989-12-26 | 1991-10-16 | Tokyo Electric Power Co Inc:The | Reformer of hydrocarbon |
JP2513485Y2 (en) * | 1991-08-06 | 1996-10-09 | 北越消雪機械工業株式会社 | Watering nozzle |
JP3442167B2 (en) * | 1993-12-28 | 2003-09-02 | 千代田化工建設株式会社 | Heat transfer method in reformer |
DE10119083C1 (en) * | 2001-04-19 | 2002-11-28 | Joachim Alfred Wuenning | Compact steam reformer |
US20070104641A1 (en) * | 2005-11-08 | 2007-05-10 | Ahmed M M | Method of controlling oxygen addition to a steam methane reformer |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1580740A (en) * | 1923-02-20 | 1926-04-13 | Commercial Solvents Corp | Catalyzing apparatus |
US2173844A (en) * | 1935-07-19 | 1939-09-26 | Houdry Process Corp | Heat exchange |
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 |
US3645701A (en) * | 1967-06-19 | 1972-02-29 | Lummus Co | Reformer furnace |
US3541729A (en) * | 1968-05-09 | 1970-11-24 | Gen Electric | Compact reactor-boiler combination |
US3909299A (en) * | 1973-10-01 | 1975-09-30 | United Technologies Corp | Fuel cell system including reform reactor |
DE2521710A1 (en) * | 1975-05-15 | 1976-11-18 | Siemens Ag | REACTOR FOR THE CATALYTIC REVISION OF HYDROCARBONS WITH AN OXYGEN-CONTAINING GAS |
-
1977
- 1977-11-15 FR FR7734286A patent/FR2374947A1/en active Granted
- 1977-11-16 IL IL53404A patent/IL53404A/en unknown
- 1977-11-16 DE DE19772751308 patent/DE2751308A1/en active Granted
- 1977-11-17 AU AU30725/77A patent/AU509038B2/en not_active Expired
- 1977-11-18 GB GB48125/77A patent/GB1564995A/en not_active Expired
- 1977-11-18 NL NL7712715A patent/NL7712715A/en not_active Application Discontinuation
- 1977-11-21 DK DK514377A patent/DK514377A/en not_active Application Discontinuation
- 1977-11-21 CH CH1416577A patent/CH625827A5/en not_active IP Right Cessation
- 1977-11-23 SE SE7713225A patent/SE423895B/en not_active IP Right Cessation
- 1977-11-24 IT IT7729977A patent/IT1089105B/en active
- 1977-11-28 BR BR7707896A patent/BR7707896A/en unknown
- 1977-11-29 JP JP14323877A patent/JPS5379768A/en active Granted
- 1977-11-29 ES ES464566A patent/ES464566A1/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
AU509038B2 (en) | 1980-04-17 |
CH625827A5 (en) | 1981-10-15 |
IL53404A (en) | 1981-03-31 |
JPS577539B2 (en) | 1982-02-10 |
IL53404A0 (en) | 1978-01-31 |
IT1089105B (en) | 1985-06-18 |
ES464566A1 (en) | 1978-09-01 |
DE2751308C2 (en) | 1987-05-14 |
FR2374947A1 (en) | 1978-07-21 |
BR7707896A (en) | 1978-08-01 |
FR2374947B1 (en) | 1983-08-19 |
NL7712715A (en) | 1978-06-26 |
DE2751308A1 (en) | 1978-07-06 |
SE423895B (en) | 1982-06-14 |
AU3072577A (en) | 1979-05-24 |
DK514377A (en) | 1978-06-23 |
JPS5379768A (en) | 1978-07-14 |
GB1564995A (en) | 1980-04-16 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
NUG | Patent has lapsed |
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