GB584601A - Production of butadiene - Google Patents

Production of butadiene

Info

Publication number
GB584601A
GB584601A GB74445A GB74445A GB584601A GB 584601 A GB584601 A GB 584601A GB 74445 A GB74445 A GB 74445A GB 74445 A GB74445 A GB 74445A GB 584601 A GB584601 A GB 584601A
Authority
GB
United Kingdom
Prior art keywords
glycol
phosphate
catalyst
butadiene
butenol
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
GB74445A
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.)
Airco Inc
Original Assignee
Air Reduction Co Inc
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 Air Reduction Co Inc filed Critical Air Reduction Co Inc
Priority to GB74445A priority Critical patent/GB584601A/en
Publication of GB584601A publication Critical patent/GB584601A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • C07C1/24Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1,3-Butadiene is produced by feeding 1,3-butylene glycol into a body of inert organic liquid containing a dehydrating catalyst at 220-350, preferably 260-285 DEG C., at substantially the rate at which conversion occurs, and separating butadiene from the withdrawn vapours. Suitable liquids, which may be miscible with the glycol or in which the latter may be slightly soluble, include diphenyl ethane, hexaethyl benzene, benzyl ether, "Dowtherm" (Registered Trade Mark, a mixture of diphenyl and diphenyl oxide), "Nujol" (Registered Trade Mark), various oil fractions, and "cyclic C18 alcohol." The preferred catalyst is ammonium phosphate including the tri-, di- and mono-ammonium salts or their mixtures or decomposition products formed at the reaction temperatures. Other catalysts are phosphoric acid, toluene sulphonic acid, ammonium sulphate, mixed calcium and ammonium phosphates, anilin phosphate, acid sodium phosphate, kaolin and clays. They may be mounted on supports, such as carbon, coke, kaolin, clay, "Filtercel" or "Celite" (Registered Trade Marks). The ratio of catalyst to heating liquid may be 2 per cent or less if finely divided and up to 50 per cent for larger pieces. A reactor fitted with heating jacket and stirrer contains the catalyst suspended or dissolved in the inert liquid, the glycol being introduced beneath the surface at the rate of reaction. The vapours produced pass to a reflux condenser for return of any glycol and heating liquid, and are further cooled to condense water and partially reacted glycol or butenol from the butadiene. The condensate is stratified, the upper butenol layer being recycled to the reactor while the upper layer is rectified to remove most of the water from residual butenol which is recycled. The heating liquid and catalyst may be drawn off periodically or continuously for reviving or replacing. In examples, diammonium phosphate in diphenyl ethane, diammonium phosphate on coke or "Filtercel" in a wash oil, anilin phosphate in a wash oil, and orthophosphoric acid in C18 alcohol are used.
GB74445A 1945-01-09 1945-01-09 Production of butadiene Expired GB584601A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB74445A GB584601A (en) 1945-01-09 1945-01-09 Production of butadiene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB74445A GB584601A (en) 1945-01-09 1945-01-09 Production of butadiene

Publications (1)

Publication Number Publication Date
GB584601A true GB584601A (en) 1947-01-17

Family

ID=9709763

Family Applications (1)

Application Number Title Priority Date Filing Date
GB74445A Expired GB584601A (en) 1945-01-09 1945-01-09 Production of butadiene

Country Status (1)

Country Link
GB (1) GB584601A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0125566A1 (en) * 1983-05-11 1984-11-21 BASF Aktiengesellschaft Process for the production of olefins by dehydration of alcohols
GB2151254A (en) * 1983-12-14 1985-07-17 Penick Corp Dehydration of 2,5-dimethyl-2,5-hexanediol

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0125566A1 (en) * 1983-05-11 1984-11-21 BASF Aktiengesellschaft Process for the production of olefins by dehydration of alcohols
GB2151254A (en) * 1983-12-14 1985-07-17 Penick Corp Dehydration of 2,5-dimethyl-2,5-hexanediol

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