GB800974A - Production of diketene - Google Patents

Production of diketene

Info

Publication number
GB800974A
GB800974A GB2637155A GB2637155A GB800974A GB 800974 A GB800974 A GB 800974A GB 2637155 A GB2637155 A GB 2637155A GB 2637155 A GB2637155 A GB 2637155A GB 800974 A GB800974 A GB 800974A
Authority
GB
United Kingdom
Prior art keywords
diketene
acetic anhydride
ketene
production
continuously
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
GB2637155A
Inventor
Richard Norman Lacey
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.)
Distillers Co Yeast Ltd
Distillers Co Ltd
Original Assignee
Distillers Co Yeast Ltd
Distillers Co Ltd
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 Distillers Co Yeast Ltd, Distillers Co Ltd filed Critical Distillers Co Yeast Ltd
Priority to GB2637155A priority Critical patent/GB800974A/en
Publication of GB800974A publication Critical patent/GB800974A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/87Preparation of ketenes or dimeric ketenes
    • C07C45/88Preparation of ketenes or dimeric ketenes from ketones

Abstract

Diketene is obtained from ketene by dimerizing it in the presence of diketene and acetic anhydride and removing the heat of dimerization of the ketene. It is preferred to have present at least 50 per cent of acetic anhydride based on the weight of diketene and acetic anhydride together. The process may be carried out continuously or batchwise. Suitable temperatures for carrying out the process are 0-70 DEG C. and preferably 10-40 DEG C. Desirably, acetic anhydride is added continuously to the reactor to maintain the diketene to acetic anhydride ratio at a constant level. An example is given.
GB2637155A 1955-09-15 1955-09-15 Production of diketene Expired GB800974A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2637155A GB800974A (en) 1955-09-15 1955-09-15 Production of diketene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2637155A GB800974A (en) 1955-09-15 1955-09-15 Production of diketene

Publications (1)

Publication Number Publication Date
GB800974A true GB800974A (en) 1958-09-03

Family

ID=10242607

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2637155A Expired GB800974A (en) 1955-09-15 1955-09-15 Production of diketene

Country Status (1)

Country Link
GB (1) GB800974A (en)

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