Continuous process of oxidative cleavage of vegetable oils

摘要

A continuous process for the oxidative cleavage of vegetable oils containing triglycerides of unsaturated carboxylic acids, to obtain saturated carboxylic acids, comprising feeding to a first continuous reactor a vegetable oil, an oxidizing compound and catalyst capable of catalyzing the oxidation reaction of the olefinic double bond to obtain an intermediate compound containing vicinal diols: feeding to a second continuous reactor said intermediate compound, a compound containing oxygen and a catalyst capable of catalyzing the oxidation reaction of the vicinal diols to carboxylic groups, to obtain saturated monocarboxylic acids (i) and triglycerides containing saturated carboxylic acids with more than one acid function (ii); separating the saturated monocarboxylic acids (i) from the triglycerides (ii); hydrolyzing in a third reactor the triglycerides (ii) to obtain glycerol and saturated carboxylic acids with more than one acid function; and purifying said saturated carboxylic acids by fractioned crystallization by means of wash column (melt crystallization).

主权项

1. A continuous process for the oxidative cleavage of derivatives of unsaturated carboxylic acids for the production of saturated carboxylic acids, which comprises the steps of:
a) feeding to a first continuous reactor at least a vegetable oil having an olefinic double bond and an oxidizing compound in the presence of a catalyst capable of catalyzing the oxidation reaction of the olefinic double bond to obtain an intermediate compound containing vicinal diols; b) feeding to a second continuous reactor said intermediate compound, oxygen or a compound containing oxygen, and a catalyst capable of catalyzing the oxidation reaction of said diols to carboxylic groups, to obtain saturated monocarboxylic acids (i) and triglycerides containing saturated carboxylic acids having more than one acid function (ii); c) transferring the product of step b) to an apparatus suitable to separate the saturated monocarboxylic acids (i) from the triglycerides having more than one acid function (ii); d) hydrolyzing in a third reactor said triglycerides (ii) to obtain glycerol and saturated carboxylic acids with more than one acid function; e) purifying said saturated carboxylic acids with more than one acid function by fractioned crystallization by means of wash column (melt crystallization); wherein operations to feed reagents and to remove products take place simultaneously for the entire duration of the process, and in each of said steps the process conditions remain substantially unchanged.