Process for working up diacetone acrylamide solutions for the preparation of pure diacetone acrylamide
View Patent ↗Improved process for working up diacetone acrylamide solutions, obtained by reaction of acetone or diacetone alcohol with acrylonitrile and sulfuric acid and subsequent dilution and neutralization, in which a) the organic phase obtained subsequent to the neutralization, which comprises the crude diacetone acrylamide, is hydrolyzed by addition of an aqueous alkaline solution in order to remove acrylamide, then b) after phase separation has been carried out, the organic phase, which comprises the crude diacetone acrylamide, is neutralized by addition of an acid, and c) in succession, low-boiling-point byproducts are removed by distillation in the presence of one or more polymerization inhibitors, then t-butylacrylamide is removed by distillation and, finally, the diacetone acrylamide is isolated by product distillation, and d) the diacetone acrylamide thus obtained is converted into its final form.
1. An improved process for working up of a diacetone acrylamide solution obtained by reaction of acetone or diacetone alcohol with acrylonitrile and sulfuric acid and subsequent dilution and neutralization, wherein the process comprises:
a) hydrolyzing an organic phase which comprises crude diacetone acrylamide obtained subsequent to the neutralization of the diacetone acrylamide solution by addition of an aqueous alkaline solution in order to remove acrylamide, then subsequently
b) after phase separation has been carried out, neutralizing the organic phase which comprises the crude diacetone acrylamide by addition of an acid, then
c) in succession, c1) removing, by distillation in the presence of one or more polymerization initiators, low-boiling-point byproducts then c2) removing t-butylacrylamide by distillation carried out at a temperature of from 80 to 150° C. and a pressure of from 0.01 to 20 mbar, and, finally, c3) isolating the diacetone acrylamide by product distillation carried out at a temperature of from 100 to 130° C. and a pressure of from 0.01 to 5 mbar, and
d) converting the diacetone acrylamide thus obtained in step c) into a final form.
2. The process according to claim 1 , wherein the hydrolysis of step a) is carried out by addition of a 5 to 50% by weight aqueous NaOH or KOH solution or a mixture thereof at a temperature of from 50 to 90° C.
3. The process according to claim 1 , wherein step b) is practiced by adding an amount of acid sufficient for pH to be adjusted to a value of from 4 to 8.
4. The process according to claim 1 , wherein the distillation of step c1) for removing low-boiling-point byproducts is carried out at a temperature of at most 85° C. and with a vacuum of up to 25 mbar.
5. The process according to claim 1 , wherein the distillation of step c1) for removing low-boiling-point byproducts is carried out in the presence of one or more polymerization inhibitors selected from the group consisting of hydroquinone, hydroquinone monomethyl ether, phenothiazine, diphenylamine and copper powder.
6. The process according to claim 1 , wherein the distillation of step c2) for removing t-butylacrylamide is carried out using distillation equipment with a number of theoretical plates of from 1 to 5.
7. The process according to claim 1 , wherein step d) is practiced by converting the diacetone acrylamide into a flake form.