GB642557A - Improved manufacture of carbon bisulphide - Google Patents
Improved manufacture of carbon bisulphideInfo
- Publication number
- GB642557A GB642557A GB4517/48A GB451748A GB642557A GB 642557 A GB642557 A GB 642557A GB 4517/48 A GB4517/48 A GB 4517/48A GB 451748 A GB451748 A GB 451748A GB 642557 A GB642557 A GB 642557A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- charcoal
- air
- sulphur
- vapours
- 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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Carbon bisulphide is made by passing sulphur vapours, superheated to 600-800 DEG C. by passage in countercurrent to and in direct contact with a moving bed of hot small particles of a refractory material, into contact with reactive carbon, e.g. charcoal, in an insulated <PICT:0642557/III/1> reaction zone maintained at a temperature not materially exceeding 850 DEG C. solely by the heat of reaction. As shown, molten sulphur from kettle 1 is vaporized at 4 and the vapours passed to a superheater 6 consisting of three refractory lined chambers 8, 9, 10. Mullite pebbles, heated in chamber 8 by the combustion products of gas or oil burner 13, pass through chamber 9 wherein they heat the sulphur vapour and thence to chamber 10 from which they are returned to chamber 8 by an air lift, the air separated at 23 returning to a blower 25 via a dust separator 27. The heated vapours pass into an insulated reactor 28 to react with charcoal from a hopper 33. Ash is removed periodically through outlet 30 while exit gases are passed to condenser 40, liquid carbon bisulphide passing to receiver 42. Non-condensed gases pass to oil scrubber 44, hydrogen sulphide escaping through line 45. The wash oil passes to reboiler 47 and stripper 48 whence the separated vaporized carbon bisulphide is returned to the condenser 40. To start the reaction, the charcoal in chamber 29 is burned by air admitted through inlet 7 until a glowing zone is established, when the air is shut off and a flow of sulphur vapour started. To prevent gas leakage from chamber 8 to chamber 9 or vice versa, the static pressure in the two chambers is equalized by adjustment of valve 15 in vent stack 14 and valve 38 in exit pipe 37 of the reactor.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US642557XA | 1947-03-08 | 1947-03-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB642557A true GB642557A (en) | 1950-09-06 |
Family
ID=22054640
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4517/48A Expired GB642557A (en) | 1947-03-08 | 1948-02-16 | Improved manufacture of carbon bisulphide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB642557A (en) |
-
1948
- 1948-02-16 GB GB4517/48A patent/GB642557A/en not_active Expired
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