GB575530A - Improvements in or relating to the production of trichlorethylene - Google Patents
Improvements in or relating to the production of trichlorethyleneInfo
- Publication number
- GB575530A GB575530A GB5310/44A GB531044A GB575530A GB 575530 A GB575530 A GB 575530A GB 5310/44 A GB5310/44 A GB 5310/44A GB 531044 A GB531044 A GB 531044A GB 575530 A GB575530 A GB 575530A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tetrachlorethane
- trichlorethylene
- water
- chiefly
- porcelain
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/25—Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated hydrocarbons
Abstract
Trichlorethylene is prepared by the pyrolysis of tetrachlorethane, made by the chlorination of acetylene and containing 5 per cent impurities, at a temperature in the range 400-500 DEG C. Perchlorethyele and dichlorethylene are also formed. The hydrogen chloride evolved is adsorbed in water and the liquid products are water washed and separated by fractionation. The apparatus for pyrolysis is made of a corrosion resisting, non-catalytic metal such as iron, steel or nickel, or can be made of carbon, porcelain or similar materials. Cracking is carried out in unpacked coils of tube of small diameter, or in pipes of larger diameter packed with Rashig rings, porcelain or other non-catalytic materials. In the examples: (1) crude tetrachlorethane from the acetylene chlorinator is vaporized at 170-190 DEG C., preheated to 350-370 DEG C. and passed through the reaction chamber maintained at 460-470 DEG C. The liquid product, chiefly trichlorethylene, is condensed and the hydrogen chloride absorbed in water; (2) crude tetrachlorethane is vaporized at 200 DEG C. and passed through a nickel coil maintained at 460 DEG C. The liquid product is chiefly trichlorethylene, but contains some perchlorethylene and tetrachlorethane.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US575530XA | 1943-03-23 | 1943-03-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB575530A true GB575530A (en) | 1946-02-21 |
Family
ID=22011289
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5310/44A Expired GB575530A (en) | 1943-03-23 | 1944-03-22 | Improvements in or relating to the production of trichlorethylene |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB575530A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2682512A (en) * | 1948-08-02 | 1954-06-29 | Minnesota Mining & Mfg | Unsaturated organosilanes and method of making same |
US2859254A (en) * | 1955-11-21 | 1958-11-04 | Columbia Southern Chem Corp | Dehydrochlorination of tetrachloroethane |
DE1090651B (en) * | 1955-11-21 | 1960-10-13 | Columbia Southern Chem Corp | Process for the production of trichlorethylene |
-
1944
- 1944-03-22 GB GB5310/44A patent/GB575530A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2682512A (en) * | 1948-08-02 | 1954-06-29 | Minnesota Mining & Mfg | Unsaturated organosilanes and method of making same |
US2859254A (en) * | 1955-11-21 | 1958-11-04 | Columbia Southern Chem Corp | Dehydrochlorination of tetrachloroethane |
DE1090651B (en) * | 1955-11-21 | 1960-10-13 | Columbia Southern Chem Corp | Process for the production of trichlorethylene |
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