GB756027A - Process for the manufacture of fluorine-containing unsaturated aliphatic hydrocarbons - Google Patents
Process for the manufacture of fluorine-containing unsaturated aliphatic hydrocarbonsInfo
- Publication number
- GB756027A GB756027A GB15163/52A GB1516352A GB756027A GB 756027 A GB756027 A GB 756027A GB 15163/52 A GB15163/52 A GB 15163/52A GB 1516352 A GB1516352 A GB 1516352A GB 756027 A GB756027 A GB 756027A
- Authority
- GB
- United Kingdom
- Prior art keywords
- iron
- zinc
- fluorine
- methanol
- treated
- 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
- C07C17/23—Preparation of halogenated hydrocarbons by dehalogenation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Fluorine-containing aliphatic hydrocarbons are made by reacting at least the theoretical proportion of finely-divided iron with a saturated aliphatic hydrocarbon - containing fluorine and at least two atoms of another halogen bound to vicinal carbon atoms in the presence of a solvent and at a raised temperature to eliminate at least 2 atoms of halogen (other than fluorine) from the saturated hydrocarbon. Raised pressure may be used, e.g. by the introduction of nitrogen under pressure. Pressures of about 10-200 atmospheres are mentioned. Advantageously a small proportion of finely-divided zinc may be added so that the reaction starts at a lower temperature and the fluorine-containing unsaturated hydrocarbon formed produces the required pressure. The reaction is advantageously effected at the vapour pressure of the reactant at the reaction temperature. Temperatures of about 90-200 DEG , especially about 130 DEG C., are indicated although with iron of high activity the temperature may be about 80 DEG C. Advantageously, an excess of about 40 per cent of the theoretical quantity of iron is added. The quantity of zinc added may be up to about 10 per cent of the theoretical. When a small quantity of zinc is used less than the theoretical quantity of iron may be present but the total quantity of iron and zinc should be sufficient to remove at least 2 atoms of halogen from the saturated hydrocarbons. Specified solvents are methanol, ethanol, propanol, isopropanol, butanol, isobutanol, benzyl alcohol and acetamide. Preferably, the solvent should be capable of dissolving the starting material and FeHal2 and be at least partially miscible with water. Chlorine may be eliminated from 1,2,3,4-tetrachloro-1,1,2,3,4,4-hexafluorobutane or 1,2-dichloro-1,1,2,3,3,3 - hexafluoropropane to form hexafluoro - butadiene and -propylene respectively, and bromine may be eliminated from the corresponding bromo compounds. In examples, 1,1,2 - trichloro - 1,2,2 - trifluoroethane is treated with iron powder in (1) aqueous methanol and (2) methanol under nitrogen to produce trifluoro-chlorethylene, the addition of 5 per cent of zinc based on iron being optional in (2); in (3) 1,1,2,2 - tetrachloro - 1,2 - difluorethane is treated with iron and zinc in methanol under nitrogen to yield 1,2-dichloro-1,2-difluorethylene; (4) 1,1,2 - trichloro - 2,2 - difluorethane is treated with iron and zinc in ethanol under nitrogen to yield 1-chloro-2,2-difluorethylene; and in (5) 1,2-dichloro-1,2,3,3,4,4-hexafluorocyclobutane is treated as in (4) to yield hexafluorocyclobutylene. If the last example is effected in methanol, 1-methoxy-pentafluorocyclobutylene is obtained as a by-product.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE756027X | 1951-06-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB756027A true GB756027A (en) | 1956-08-29 |
Family
ID=6659740
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB15163/52A Expired GB756027A (en) | 1951-06-14 | 1952-06-16 | Process for the manufacture of fluorine-containing unsaturated aliphatic hydrocarbons |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR1058345A (en) |
GB (1) | GB756027A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003095401A1 (en) * | 2002-05-13 | 2003-11-20 | Bayer Cropscience Aktiengesellschaft | Method for the production of substituted trifluoroethylenes |
CN109956847A (en) * | 2017-12-25 | 2019-07-02 | 中蓝晨光化工研究设计院有限公司 | A kind of aqueous phase preparation method of fluorine-containing cyclobutane |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8822541D0 (en) * | 1988-09-26 | 1988-11-02 | Ici Plc | Production of fluorocarbons |
-
1952
- 1952-06-14 FR FR1058345D patent/FR1058345A/en not_active Expired
- 1952-06-16 GB GB15163/52A patent/GB756027A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003095401A1 (en) * | 2002-05-13 | 2003-11-20 | Bayer Cropscience Aktiengesellschaft | Method for the production of substituted trifluoroethylenes |
CN109956847A (en) * | 2017-12-25 | 2019-07-02 | 中蓝晨光化工研究设计院有限公司 | A kind of aqueous phase preparation method of fluorine-containing cyclobutane |
CN109956847B (en) * | 2017-12-25 | 2022-05-20 | 中蓝晨光化工研究设计院有限公司 | Aqueous phase preparation method of fluorine-containing cyclobutene |
Also Published As
Publication number | Publication date |
---|---|
FR1058345A (en) | 1954-03-16 |
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