GB833562A - Process for preparation of carbon disulphide - Google Patents
Process for preparation of carbon disulphideInfo
- Publication number
- GB833562A GB833562A GB6174/57A GB617457A GB833562A GB 833562 A GB833562 A GB 833562A GB 6174/57 A GB6174/57 A GB 6174/57A GB 617457 A GB617457 A GB 617457A GB 833562 A GB833562 A GB 833562A
- Authority
- GB
- United Kingdom
- Prior art keywords
- bed
- fluidized bed
- petroleum coke
- heated
- fluidized
- 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
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/70—Compounds containing carbon and sulfur, e.g. thiophosgene
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
Abstract
Carbon disulphide is prepared by passing a gas containing sulphur vapour through a bed of finely-divided electrically-conductive carbon particles to maintain the bed in a fluidized state, passing an electric current through the fluidized bed to maintain it at reaction temperature, e.g. 700-1500 DEG C., preferably 900-1200 DEG C., and recovering CS2 from the effluent gases. The contact time of S and C should be 0.5-10 secs. N2 entering at 21 carries S from heated reflux flask 15 through heated tube 17, superheater 18, and diffuzer 19 into fluidized bed 13 in glass or refractory tube 12. The bed 13 is petroleum coke produced in a fluidized bed-coking process and calcined, e.g. at 900 DEG C. for 2 hours to increase the conductivity. The bed 13 is heated by current supplied through <PICT:0833562/III/1> electrodes 1, 2 and a thermocouple well 20 is also provided, on all of which radiation shields are provided (Figs. 2, 3, not shown). Additional N2 is supplied through 5 and gas disperser 4 of graphite with a porous carbon top, the latter having thermal insulation, e.g. petroleum coke particles 7 below. The calcination of the petroleum coke may be in a separate fluidized bed reactor, or may be in situ by feeding small amounts of "green" coke to the bed 13 to replace that consumed. Effluent gases are withdrawn through trap 22 and filter 23, where sulphur is removed, to condenser 24, whence CS2 passes to receiver 25.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US833562XA | 1956-12-10 | 1956-12-10 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB833562A true GB833562A (en) | 1960-04-27 |
Family
ID=22177785
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB6174/57A Expired GB833562A (en) | 1956-12-10 | 1957-02-25 | Process for preparation of carbon disulphide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB833562A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1935643B (en) * | 2004-12-07 | 2010-08-11 | 孔庆然 | Method for producing carbon bisulfide by fluidization process and its special equipment |
-
1957
- 1957-02-25 GB GB6174/57A patent/GB833562A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1935643B (en) * | 2004-12-07 | 2010-08-11 | 孔庆然 | Method for producing carbon bisulfide by fluidization process and its special equipment |
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