GB260236A - Process for the continuous distillation of crude carbon bisulphide to obtain pure carbon bisulphide - Google Patents
Process for the continuous distillation of crude carbon bisulphide to obtain pure carbon bisulphideInfo
- Publication number
- GB260236A GB260236A GB25053/26A GB2505326A GB260236A GB 260236 A GB260236 A GB 260236A GB 25053/26 A GB25053/26 A GB 25053/26A GB 2505326 A GB2505326 A GB 2505326A GB 260236 A GB260236 A GB 260236A
- Authority
- GB
- United Kingdom
- Prior art keywords
- still
- carbon bisulphide
- column
- sulphur
- crude
- 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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
260,236. I. G. Farbenindustrie Akt.- Ges., (Assignees of Chemische Fabrik Griesheim-Elektron). Oct. 24, 1925, [Convention date]. Carbon bisulphide, distilling.-In saparating crude carbon bisulphide into pure carbon bisulphide, sulphuretted hydrogen and sulphur, the crude liquid is fed into the upper part of a column A from which the residual liquid passes into a still A<2>. Carbon bisulphide vapours pass from the base of the column through a pipe x to the top of a column B. Residual liquid containing sulphur passes into a still B<2>, which may be arranged as an annular chamber above the still A<2>. Pure carbon bisulphide vapours pass from the base of the column to a condenser C. Sulphuretted hydrogen passes from the upper parts of the columns through reflux condensers A', B<1>, and through a final condenser D, the condensate from which is passed into the column A. The still A<2> is maintained at a temperature above the melting-point of sulphur, and the still B<2> slightly above the boiling-point of carbon bisulphide. Residue from the still B<2> is passed into the still A<2>, and liquid sulphur is discharged from the still A<2>. The columns are surrounded by heatinsulating material.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE260236X | 1925-10-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB260236A true GB260236A (en) | 1927-10-06 |
Family
ID=5968028
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB25053/26A Expired GB260236A (en) | 1925-10-24 | 1926-10-08 | Process for the continuous distillation of crude carbon bisulphide to obtain pure carbon bisulphide |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB260236A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3250595A (en) * | 1962-07-12 | 1966-05-10 | Fmc Corp | Method of producing carbon bisulfide |
-
1926
- 1926-10-08 GB GB25053/26A patent/GB260236A/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3250595A (en) * | 1962-07-12 | 1966-05-10 | Fmc Corp | Method of producing carbon bisulfide |
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