GB869959A - Production of dicyclohexyl phthalate - Google Patents
Production of dicyclohexyl phthalateInfo
- Publication number
- GB869959A GB869959A GB31937/58A GB3193758A GB869959A GB 869959 A GB869959 A GB 869959A GB 31937/58 A GB31937/58 A GB 31937/58A GB 3193758 A GB3193758 A GB 3193758A GB 869959 A GB869959 A GB 869959A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cyclohexanol
- mixture
- cyclohexene
- water
- acid
- 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
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/76—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring
- C07C69/80—Phthalic acid esters
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Dicyclohexyl phthalate is produced by heating a mixture of phthalic acid and/or phthalic anhydride and a stoichiometric excess of cyclohexanol in the presence of an acid dehydrating-catalyst, at a pressure not exceeding atmospheric pressure, the temperature of the reaction-mixture being at least sufficient to vaporize the cyclohexanol/water azeotrope, passing the vapours, which contain cyclohexene (formed by decomposition of cyclohexanol), to a cooling-zone where in the cyclohexanol is condensed but cyclohexene (and its water-azeotrope) remains in the vapour phase, and removing cyclohexene from the system. The following catalysts may be used:- sulphuric acid, p-toluene p sulphonic acid, the alkane sulphonic acids, and the sulphamic acids. In an example, a mixture of phthalic anhydride, cyclohexanol and sulphuric acid is heated at a temperature of 117 DEG -125 DEG C. and an absolute pressure of 170-220 mm.; and the vapours are passed to a fractionating column, the head of which is maintained at a temperature between 55 DEG and 75 DEG C. The uncondensed vapours, consisting chiefly of cyclohexene and water, are withdrawn overhead, while the condensate, consisting chiefly of cyclohexanol, is returned to the reaction-mixture. The cooled product is washed with aqueous sodium hydroxide followed by water, and then subjected to steam-distillation to remove volatile material. The dicyclohexyl phthalate so obtained is dried; and a crystalline almost-colourless product is obtained.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US869959XA | 1957-10-07 | 1957-10-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB869959A true GB869959A (en) | 1961-06-07 |
Family
ID=22202204
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31937/58A Expired GB869959A (en) | 1957-10-07 | 1958-10-07 | Production of dicyclohexyl phthalate |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB869959A (en) |
-
1958
- 1958-10-07 GB GB31937/58A patent/GB869959A/en not_active Expired
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