GB584601A - Production of butadiene - Google Patents
Production of butadieneInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
- C07C1/24—Preparation 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preferably 260-285 DEG C., at substantially the rate at which conversion occurs, and separating butadiene from the withdrawn vapours.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.
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)
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 |
-
1945
- 1945-01-09 GB GB74445A patent/GB584601A/en not_active Expired
Cited By (2)
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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