DE747814C - Process for the production of dichloroethylene from tetrachloroethane - Google Patents

Process for the production of dichloroethylene from tetrachloroethane

Info

Publication number
DE747814C
DE747814C DEC55529D DEC0055529D DE747814C DE 747814 C DE747814 C DE 747814C DE C55529 D DEC55529 D DE C55529D DE C0055529 D DEC0055529 D DE C0055529D DE 747814 C DE747814 C DE 747814C
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DE
Germany
Prior art keywords
tetrachloroethane
dichloroethylene
production
amalgam
reduction
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
Application number
DEC55529D
Other languages
German (de)
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to DEC55529D priority Critical patent/DE747814C/en
Application granted granted Critical
Publication of DE747814C publication Critical patent/DE747814C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/23Preparation of halogenated hydrocarbons by dehalogenation

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Breeding Of Plants And Reproduction By Means Of Culturing (AREA)

Description

Verfahren zur Herstellung von Dichloräthylen aus Tetrachloräthan Es ist bekannt, Dichloräthvlen durch Reduktion von. Tetrachloräthan mit Wasser und Zinkstaub oder Eisen herzustellen. Bei diesen bekannten Verfahren ist es jedoch erforderlich, das Dichloräthylen einer besonderen Reinigung zu unterziehen, wobei es noch weiterer zusätzlicher Maßnahmen bedarf, um die anfallenden. Nebenerzeugnisse einer geeigneten Verwertung zuzuführen. Dies bedeutet aber eine Verteuerung und Verwickelung der Arbeitsweisen.Process for the production of dichloroethylene from tetrachloroethane Es is known to dichloroethylene by reducing. Tetrachloroethane with water and To produce zinc dust or iron. In these known methods, however, it is required to subject the dichloroethylene to a special cleaning process, whereby further additional measures are required to deal with the incurred. By-products suitable recycling. But this means an increase in price and Entanglement of ways of working.

Es hat sich nun gezeigt, daß man diese Nachteile in einfacher Weise vermeiden ünrl das Verfahren besonders wirtschaftlich gestalten kann, wenn man i@m Sinne der vorliegenden Erfindung zur Reduktion des Tetrachloräthans Amalgame, z. B. Alkali-, Erdalkali- oder Zinkamalgam, verwendet. Zur Durchführung des Verfahrens wird beispielsweise eine wässerige Emulsion von 75o kg Tetrachloräthan in i5o kg Wasser der Einwirkung von Natriurnamalgam, .das beliebigen Ursprungs sein kann, bei mäßig erhöhter Temperatur, beispielsweise bei 6o° C, unterworfen. Dabei werden je Quadratmeter wirksamer Amalgamoberfläche je Stunde etwa i i kg Tetrachloräthan zu symmetrischem Dichloräthylen umgesetzt. Das entstehende, zwischen 5o und 6o° C siedende- Gemisch von cis- und trans-Dichloräthylen wird unter den gegebenen Arbeitsbedingungen verflüchtigt und in einer nachgeschalteten Kondensationsanlage unmittelbar in reinstem Zustande mit einer Ausbeute von etwa 95 °/o -der theoretisch berechneten Menge gewonnen. Unerwünschte 2,\'ebenerzeugnisse fallen bei dieser Arbeitsweise nicht an, so daß sich auch,dadurch das Verfahren besonders einfach und wirtschaftlich gestaltet. , Es ist im Schrifttum bereits darauf hingewiesen worden, daß in i, 2-Halogeniden mit Zink- und Eisessig oder auch mit Natriumamalgam das Halogen nicht :durch Wasserstoff ersetzt wird, sondern daß sich unter Halogenentzug eine Äthylenbindung ausbildet.' Dabei entstehen jedoch keine einheitlichen Erzeugnisse, sondern regelmäßig Gemische verschieden chlorierter Verbindungen , die erst durch schwieriges Fraktionieren oder andere Trennungsverfahren abgetrennt werden müssen. Es war deshalb überraschend und nicht vorauszusehen, daß im Falle des Tetrachloräthans die Reduktion mit Amalgam ausschließlich unter Bildung von Dichloräthvlen verläuft. -It has now been shown that these disadvantages can be overcome in a simple manner avoid ünrl the process can be made particularly economical if i @ m For the purposes of the present invention for the reduction of tetrachloroethane amalgams, e.g. B. alkali, alkaline earth or zinc amalgam is used. To carry out the procedure for example, an aqueous emulsion of 750 kg of tetrachloroethane in 150 kg Water from the action of sodium amalgam, which can be of any origin, at a moderately elevated temperature, for example at 6o ° C, subjected. Be there per square meter of effective amalgam surface per hour about i i kg of tetrachloroethane converted to symmetrical dichloroethylene. The resulting, between 5o and 6o ° C boiling mixture of cis and trans dichloroethylene is used under the given working conditions volatilized and immediately in the purest state in a downstream condensation plant States obtained with a yield of about 95% of the theoretically calculated amount. Undesired 2, \ 'even products do not occur with this method of operation, so that also, making the process particularly simple and economical. It has already been pointed out in the literature that in i, 2-halides not with zinc and glacial acetic acid or with sodium amalgam: with hydrogen is replaced, but that an ethylene bond is formed with the removal of halogen. ' However, this does not result in uniform products, but rather regular mixtures different chlorinated compounds, which only through difficult fractionation or other separation methods have to. It was therefore surprising and unforeseeable that in the case of tetrachloroethane the reduction with amalgam takes place exclusively with the formation of dichloroethylene. -

Claims (1)

PATENTANSPRUCH: Verfahren zur Herstellung von Dichloräthvlen durch Reduktion von Tetrachlor@ äthan, ,dadurch gekennzeichnet, daß -rnan Tetrachloräthan mit Amalgamen, vorzugsweise mit Alkaliamalgam umsetzt. Zur Abgrenzung des Amneldungsgegenstandes vom Stand der Technik ist im Erteilungsverfahren folgende Druckschrift in Betracht gezogen worden Weygand, »Organisch-Chemische Expe-imentierkun.st«, 1938, S. 4.17, Abs. a.PATENT CLAIM: Process for the production of Dichloräthvlen by Reduction of tetrachloroethane, characterized in that -rnan tetrachloroethane with amalgams, preferably with alkali amalgam. To delimit the subject of the notification From the state of the art, the following publication is to be considered in the granting procedure Weygand, "Organisch-Chemische Expe-imentierkun.st", 1938, p. 4.17, Paragraph a.
DEC55529D 1939-12-05 1939-12-05 Process for the production of dichloroethylene from tetrachloroethane Expired DE747814C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEC55529D DE747814C (en) 1939-12-05 1939-12-05 Process for the production of dichloroethylene from tetrachloroethane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEC55529D DE747814C (en) 1939-12-05 1939-12-05 Process for the production of dichloroethylene from tetrachloroethane

Publications (1)

Publication Number Publication Date
DE747814C true DE747814C (en) 1944-10-16

Family

ID=7028159

Family Applications (1)

Application Number Title Priority Date Filing Date
DEC55529D Expired DE747814C (en) 1939-12-05 1939-12-05 Process for the production of dichloroethylene from tetrachloroethane

Country Status (1)

Country Link
DE (1) DE747814C (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE256856C (en) *

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE256856C (en) *

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