GB268722A - Improvements in or relating to processes for carrying out exothermic chemical reactions - Google Patents
Improvements in or relating to processes for carrying out exothermic chemical reactionsInfo
- Publication number
- GB268722A GB268722A GB26746/26A GB2674626A GB268722A GB 268722 A GB268722 A GB 268722A GB 26746/26 A GB26746/26 A GB 26746/26A GB 2674626 A GB2674626 A GB 2674626A GB 268722 A GB268722 A GB 268722A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tubes
- catalyst
- hotter
- heat
- soc
- 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.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0417—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor
- C01C1/0423—Cold wall reactors
-
- 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
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements 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)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
268,722. Soc. l'Air Liquide, Soc. Anon. pour l'Etude et l'Exploitation des ProcÚdÚs G. Claude, (Assignees of Soc. Chimique de la Grande Paroisse Azote et Produits Chimiques). April 1, 1926, [Convention date]. Catalytic processes and apparatus.-In exothermic reactions such as the synthesis of ammonia, heat is conveyed from hotter to cooler parts of the catalytic mass by means of the reaction gases before they come into direct contact with the catalyst. In one arrangement, the reaction gases entering a pressure vessel are led through a central tube B to the hotter end of the catalytic mass, then by tubes C to the cooler end again, and finally by tubes C<1> back to the hotter end, where they pass into the surrounding catalyst. The tubes C may be partly heat-insulated, and may be arranged coaxially inside the tubes C<1>, so as to minimize loss of heat in transit from the hotter to the cooler regions. A number of separated parallel tubes may replace the central tube B. The tubes C, C<1> may be coiled, and may be pointed at their ends, to facilitate their expansion within the catalytic mass. A part of the fresh gases may be led between the heat-insulated catalyst container J and the pressure tube H, in order to cool the latter, before entering the upper end of the catalyst container J. In another arrangement, the reaction gas entering the pressure vessel is distributed to an outer series of tubes embedded in the catalyst, and after passing up through these tubes is conveyed downwards through an inner series and finally up through a central tube and into contact with the catalyst. An independent current of gas is conveyed between the catalyst container and pressure tube and is discharged to the outside of the pressure vessel, as described in Specification 268,721. Specification 150,744 also is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR626501T | 1926-04-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB268722A true GB268722A (en) | 1927-08-11 |
Family
ID=8988430
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB26746/26A Expired GB268722A (en) | 1926-04-01 | 1926-10-26 | Improvements in or relating to processes for carrying out exothermic chemical reactions |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR626501A (en) |
GB (1) | GB268722A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0080270B1 (en) * | 1981-11-19 | 1985-09-04 | Imperial Chemical Industries Plc | Synthesis process and reactor |
-
1926
- 1926-04-01 FR FR626501D patent/FR626501A/en not_active Expired
- 1926-10-26 GB GB26746/26A patent/GB268722A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
FR626501A (en) | 1927-09-08 |
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