GB605277A - Process of producing vinyl chloride - Google Patents

Process of producing vinyl chloride

Info

Publication number
GB605277A
GB605277A GB27395/45A GB2739545A GB605277A GB 605277 A GB605277 A GB 605277A GB 27395/45 A GB27395/45 A GB 27395/45A GB 2739545 A GB2739545 A GB 2739545A GB 605277 A GB605277 A GB 605277A
Authority
GB
United Kingdom
Prior art keywords
dichlorethane
vinyl chloride
decomposition
separated
smooth walls
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
GB27395/45A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Solvay SA
Original Assignee
Solvay SA
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 by Solvay SA filed Critical Solvay SA
Publication of GB605277A publication Critical patent/GB605277A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/25Preparation 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)

Abstract

Vinyl chloride is produced by thermal decomposition of 1 : 2-dichlorethane at 600-650 DEG C. in a tube with smooth walls in the absence of any catalyst and of any rough surface adapted to promote the decomposition of vinyl chloride to acetylene. By regulation of the temperature and speed of passage, the decomposition is preferably limited to about 50-70 per cent of the dichlorethane present. The process is preferably a continuous one. In an example, dichlorethane including some non-converted from a previous cycle, is passed into a furnace comprising tubular elements with smooth walls, of glass for example, heated to 600-650 DEG C. The products are at once detarred and then pass into a water scrubber and thence into a degassing plant from which the dissolved gases are delivered with the vinyl chloride to a cooler and a condenser and are then separated by known methods, whilst the acidulated liquors and the tars dissolved in the unreacted dichlorethane are run into a decanter where they are separated, the dichlorethane being returned to the cycle.
GB27395/45A 1943-01-06 1945-10-18 Process of producing vinyl chloride Expired GB605277A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
BE605277X 1943-01-06

Publications (1)

Publication Number Publication Date
GB605277A true GB605277A (en) 1948-07-20

Family

ID=3875030

Family Applications (1)

Application Number Title Priority Date Filing Date
GB27395/45A Expired GB605277A (en) 1943-01-06 1945-10-18 Process of producing vinyl chloride

Country Status (3)

Country Link
BE (1) BE448632A (en)
FR (1) FR890679A (en)
GB (1) GB605277A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1568679A1 (en) * 1965-06-09 1970-03-05 Goodrich Co B F Process for the production of 1,2-dichloroethane

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1568679A1 (en) * 1965-06-09 1970-03-05 Goodrich Co B F Process for the production of 1,2-dichloroethane

Also Published As

Publication number Publication date
BE448632A (en)
FR890679A (en) 1944-02-15

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