FIELD: chemical industry. SUBSTANCE: method comprises hydrolysis of acetonecyanohydrine to with sulfuric acid prepare hydrolysis mixture and esterification and separation of esterified mixture. Hydrolysis is carried out in such conditions under which total number of moles of 2-methacrylamide, α-sulfateisobutyr amide, α- hydroxyisobutyr amide and methacrylic acid present in the resulting hydrolysis mixture proves to be optimal, and the resulting hydrolysis mixture is then esterified with C1-C12 alkyl alcohols to prepare esterified mixture which comprises C1-C12 alkyl methacrylate, C1-C12 alkyl-α- hydroxyisobutyrate, C1-C12-alkyl-β-C1-C12-alkoxyisobutyrate and C1-C12 alkyl-α-C1-C12 alkoxyisobutyrate. Separation of esterified mixture gives aqueous fraction, first organic fraction comprising C1-C12 alkylmethacrylate, and second organic fraction comprising C1-C12 alkyl -α-hydroxyisobutyrate, C1-C12 alkyl-β-C1-C12 alkoxyisobutyrate and C1-C12 alkyl-α-C1-C12- alkoxyisobutyrate, second organic phase components are then dehydrated to prepare mixture comprising C1-C12 alkylmethacrylate, methacrylic acid, C1-C12 alkyl alcohol and water, mixture is recycled, and recycled mixture is combined either with hydrolysis mixture or with esterified mixture. EFFECT: increased yield of α,β- unsaturated carboxylic acid esters and smaller amount of the resulting reaction by-products and semiproducts recycled to process. 10 cl, 2 ex, 1 tbl
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Authors
Dates
1999-06-20—Published
1994-11-30—Filed