DE863190C - Process for the production of trifluoroethyl alcohol - Google Patents
Process for the production of trifluoroethyl alcoholInfo
- Publication number
- DE863190C DE863190C DEF3649D DEF0003649D DE863190C DE 863190 C DE863190 C DE 863190C DE F3649 D DEF3649 D DE F3649D DE F0003649 D DEF0003649 D DE F0003649D DE 863190 C DE863190 C DE 863190C
- Authority
- DE
- Germany
- Prior art keywords
- trifluoroethyl
- alcohol
- production
- weight
- parts
- 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
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/34—Halogenated alcohols
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Verfahren zur Herstellung von Trifluoräthylalkohol Der Trifluoräthylalkohol ist von S. w arts (s.Bull. Soc. chim. Belg. Bd. ¢3, S. 471) durch katalytische Hydrierung von Trifluoressigsäureanhydrid in Gegenwart von Platinschwarz bei 5o Atmosphären Druck hergestellt worden. Aus 2 Mol Trifluoressigsäureanhydrid erhält man theoretisch neben 2 Mol Trifluoressigsäure nur 2 Mol Trifluoräthylalkohol. Das Verfahren ist deshalb technisch unwirtschaftlich, zumal die Trifluoressigsäure sehr mühsam durch- Oxydation von 3-Aminobenzotrifluorid gewonnen werden muß.Process for the preparation of trifluoroethyl alcohol Trifluoroethyl alcohol is from S. w arts (see Bull. Soc. chim. Belg. Vol. [3, p. 471) by catalytic hydrogenation of trifluoroacetic anhydride in the presence of platinum black at 50 atmospheres Print has been made. Theoretically, 2 moles of trifluoroacetic anhydride are obtained in addition to 2 moles of trifluoroacetic acid, only 2 moles of trifluoroethyl alcohol. The procedure is therefore technically uneconomical, especially since the trifluoroacetic acid is very laboriously Oxidation of 3-aminobenzotrifluoride must be obtained.
Es wurde nun .gefunden, @daß man den Trifluoräthylalkohol in einfacher und glatter Weise erhalten kann, wenn man ß, ß, ß-Trifluoräthylchlorid mit Alkaliacetat in Gegenwart oder Abwesenheit von Lösungsmitteln bei mindestens 2oo° unter Druck umsetzt und den erhaltenen Essigsäuretrifluoräthylester anschließend mit Alkalilauge verseift. Dias ß, ß, ß-Trifluoräthylchlorid kann nach den Angaben der amerikanischen Patentschrift 2:230 925 hergestellt werden. Der Trifluoräthylal:kohol ist für die Einführung von trifluorierten Äthoxygruppen in Farbstoffe von :Bedeutung.It has now been found that you can use the trifluoroethyl alcohol in a simple way and can be obtained smoothly if you ß, ß, ß-trifluoroethyl chloride with alkali acetate in the presence or absence of solvents at at least 2oo ° under pressure reacted and the resulting acetic acid trifluoroethyl ester then with alkali saponified. This ß, ß, ß-Trifluoroäthylchlorid can according to the information of the American Patent 2: 230 925 can be produced. The trifluoroethylal: alcohol is for the Introduction of trifluorinated ethoxy groups in dyes of: Importance.
Beispiele 1. 1185 Gewichtsteile ß, ß, ß-Trifluoräthylchlorid und 105o Gewichtsteile wasserfreies Kal.i.umacetat werden in einer verbleiten druckfesten Bombe q.0. bis 5ö Stunden auf Zoo bis 25ö°' erhitzt. Der Anfangsdruck beträgt ungefähr 8o bis' 9o Atmosphären; er fällt im Verlauf der Reaktion auf ungefähr 5o Atmosphären ab.Examples 1. 1185 parts by weight of β, β, β-trifluoroethyl chloride and 105o Parts by weight of anhydrous Kal.i.umacetat are pressure-resistant in a leaded bomb q.0. Heated up to 25 ° 'at the zoo for up to 5ö hours. The initial pressure is about 8o to '9o atmospheres; it falls to roughly in the course of the reaction 5o atmospheres.
Nach Ablassen der Bombe-erhält man 1300 Gewichtsteile Kondensat;- davon sind 120o Gewichtsteile Essigsäuretrifluoräthylester vom Siedepunkt 78° und Zoo Gewichtsteile nicht umgesetztes ß, ß, ß-Trifluoräthylchlorid. Das entspricht einer Ausbeute an Trifluoräthylalkoholacetat von 91,5%, bezogen .auf das in Reaktion getretene Trifluorätfhylchlorid.After the bomb has been released, 1,300 parts by weight of condensate are obtained, 120o parts by weight of trifluoroethyl acetate with a boiling point of 78 ° and zoo parts by weight of unreacted β, β, β-trifluoroethyl chloride. This corresponds to a yield of trifluoroethyl alcohol acetate of 91.5%, based on the trifluoroethyl chloride which has reacted.
2. 1185 Gewichtsteile Trifluoräthylchlorid, looö Gewichtsteile wasserfreies Natriumacetat und looo Gewichtsteile Eisessig werden_ unter den gleichen Bifedingungen, wie in Beispiel r eschrieben, umgesetzt. Man erhält ungefähr 110o Gewichtsteile Essigsäuretrifluoräthylester. Durch Verseifung des nach Beispiel 1 oder 2 erhaltenen. Essigsäuretriflüoräthylesters mit Alkalilauge erhält man in quantitativer Ausbeute den Trifluoräthylalkohol vom Siedepunkt 7q.°.2. 1185 parts by weight Trifluoräthylchlorid, looö parts by weight of anhydrous sodium acetate and looo parts by weight of glacial acetic acid _, reacted under the same Bifedingungen, esch rubbed as in Example r. About 110o parts by weight of trifluoroethyl acetate are obtained. By saponification of that obtained according to Example 1 or 2. Acetic acid trifluoroethyl ester with alkali lye gives the trifluoroethyl alcohol with a boiling point of 7q. ° in quantitative yield.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEF3649D DE863190C (en) | 1941-07-04 | 1941-07-04 | Process for the production of trifluoroethyl alcohol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEF3649D DE863190C (en) | 1941-07-04 | 1941-07-04 | Process for the production of trifluoroethyl alcohol |
Publications (1)
Publication Number | Publication Date |
---|---|
DE863190C true DE863190C (en) | 1953-01-15 |
Family
ID=7083874
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEF3649D Expired DE863190C (en) | 1941-07-04 | 1941-07-04 | Process for the production of trifluoroethyl alcohol |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE863190C (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2868846A (en) * | 1956-01-05 | 1959-01-13 | Pennsalt Chemicals Corp | Preparation of 2, 2, 2-trifluoroethanol |
DE1075583B (en) * | 1960-02-18 | Pennsalt Chemicals Corporation, Philadelphia, Pa. (V. St. A.) | Process for the production of trifluoroethanol | |
US4434297A (en) | 1981-03-23 | 1984-02-28 | Halocarbon Products Corporation | Process for the preparation of trifluoroethanol |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2230925A (en) * | 1939-03-23 | 1941-02-04 | Kinetic Chemicals Inc | Preparation of 1, 1, 1-trifluoro-2-chloro-ethane |
-
1941
- 1941-07-04 DE DEF3649D patent/DE863190C/en not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2230925A (en) * | 1939-03-23 | 1941-02-04 | Kinetic Chemicals Inc | Preparation of 1, 1, 1-trifluoro-2-chloro-ethane |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1075583B (en) * | 1960-02-18 | Pennsalt Chemicals Corporation, Philadelphia, Pa. (V. St. A.) | Process for the production of trifluoroethanol | |
US2868846A (en) * | 1956-01-05 | 1959-01-13 | Pennsalt Chemicals Corp | Preparation of 2, 2, 2-trifluoroethanol |
US4434297A (en) | 1981-03-23 | 1984-02-28 | Halocarbon Products Corporation | Process for the preparation of trifluoroethanol |
EP0101526A1 (en) * | 1981-03-23 | 1984-02-29 | Halocarbon Products Corporation | Process for the preparation of trifluoroethanol |
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