DE1076120B - Process for the production of hexachloropropene - Google Patents
Process for the production of hexachloropropeneInfo
- Publication number
- DE1076120B DE1076120B DEC17779A DEC0017779A DE1076120B DE 1076120 B DE1076120 B DE 1076120B DE C17779 A DEC17779 A DE C17779A DE C0017779 A DEC0017779 A DE C0017779A DE 1076120 B DE1076120 B DE 1076120B
- Authority
- DE
- Germany
- Prior art keywords
- hexachloropropene
- production
- heptachloropropane
- saponification
- 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.)
- Pending
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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
Description
Verfahren zur Herstellung von Hexachlorpropen Es ist bekannt, daß man aus Heptachlorpropan durch Einwirkung von Alkalihydroxyd in homogener alkoholischer Lösung Hexachlofpropen herstellen kann.Process for the preparation of hexachloropropene It is known that one from heptachloropropane by the action of alkali hydroxide in homogeneous alcoholic Solution can produce hexachlofpropene.
Es wurde nun gefunden, daß man Hexachlorpropen aus Heptachlorpropan leicht und mit guter Ausbeute durch alkalische Verseifung herstellen kann, wenn man zur Verseifung eine wäßrige Suspension eines Erdalkalihydroxydes verwendet und bei Temperaturen zwischen 70 und 1000 C, vorzugsweise bei 90 bis 950 C, arbeitet. Das Temperaturgebiet zwischen 90 und 950 C ist deshalb vorzuziehen, weil oberhalb von 1000 C in Gegenwart von Wasser gleichzeitig eine teilweise Hydrolyse bis zur Trichloracrylsäure und ihren Folgeprodukten eintritt. Es ist zweckmäßig, den Chlorwasserstoff mit einer Calciumhydroxyd-Aufschlämmung abzuspalten. Die günstigste Konzentration liegt bei etwa 20- bis 300/oigem Gehalt der wäßrigen Phase an Calciumhydroxyd, welches in einem Überschuß von 50 bis 200 0/o, vorzugsweise 90 bis 1000/a, bezogen auf Heptachlorpropan, eingesetzt wird. Man erhält nach dieser Arbeitsweise, die gegeniiber der bekannten Chlorwasserstoffabspaltung in alkoholischer Lösung besonders wirtschaftlich ist, bei praktisch vollständigem Umsatz Ausbeuten von über 900/0. It has now been found that hexachloropropene can be obtained from heptachloropropane can be produced easily and with good yield by alkaline saponification if an aqueous suspension of an alkaline earth metal hydroxide is used for the saponification and at temperatures between 70 and 1000 C, preferably at 90 to 950 C, works. The temperature range between 90 and 950 C is preferable because it is above from 1000 C in the presence of water at the same time a partial hydrolysis up to Trichloroacrylic acid and its derivatives occurs. It is convenient to use the hydrogen chloride split off with a calcium hydroxide slurry. The cheapest concentration is about 20 to 300 per cent content of calcium hydroxide in the aqueous phase, which in an excess of 50 to 200 0 / o, preferably 90 to 1000 / a, based on heptachloropropane, is used. According to this procedure, one obtains the one compared to the known The elimination of hydrogen chloride in alcoholic solution is particularly economical, with practically complete conversion, yields of over 900/0.
Hexachlorpropen findet ausgedehnte Verwendung als Trafoöl, Insecticid, Stabilisator für Bleitetraäthyl und Hilfsmittel zur Herstellung von Urantetrachlorid. Hexachloropropene is used extensively as transformer oil, insecticide, Stabilizer for tetraethyl lead and auxiliary agent for the production of uranium tetrachloride.
Beispiel 1140 Teile l-H-Heptachlorpropan werden mit 320 Teilen Calciumhydroxyd (Gehalt an Ca (OH)2 92,5 0/o) und 1000 Teilen Wasser unter kräftigem Rühren 6 Stunden auf 900 C erhitzt. Anschließend neutralisiert man den Ansatz mit Salzsäure, wobei sich die Emulsion in zwei Schichten trennt. Die organische Phase wird im Vakuum destilliert und ergibt 930 Teile Hexachlorpropen (930/0 der Theorie); Kp.20 = 95 bis 990 C; fl2D0 = 1,5480. Example 1140 parts of 1-H-heptachloropropane are mixed with 320 parts of calcium hydroxide (Content of Ca (OH) 2 92.5 0 / o) and 1000 parts of water with vigorous stirring for 6 hours heated to 900 C. The batch is then neutralized with hydrochloric acid, with the emulsion separates into two layers. The organic phase is in vacuo distilled and gives 930 parts of hexachloropropene (930/0 of theory); Kp.20 = 95 up to 990 C; fl2D0 = 1.5480.
Claims (1)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEC17779A DE1076120B (en) | 1958-11-03 | 1958-11-03 | Process for the production of hexachloropropene |
GB709759A GB841358A (en) | 1958-11-03 | 1959-03-02 | Improvements in the production of hexachlorpropene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEC17779A DE1076120B (en) | 1958-11-03 | 1958-11-03 | Process for the production of hexachloropropene |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1076120B true DE1076120B (en) | 1960-02-25 |
Family
ID=7016307
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEC17779A Pending DE1076120B (en) | 1958-11-03 | 1958-11-03 | Process for the production of hexachloropropene |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1076120B (en) |
GB (1) | GB841358A (en) |
-
1958
- 1958-11-03 DE DEC17779A patent/DE1076120B/en active Pending
-
1959
- 1959-03-02 GB GB709759A patent/GB841358A/en not_active Expired
Non-Patent Citations (1)
Title |
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None * |
Also Published As
Publication number | Publication date |
---|---|
GB841358A (en) | 1960-07-13 |
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