Method for continuous production of dihydroxydiphenylalkanes
First Claim
1. A continuous process for the production of dihydroxydiarylalkane comprising(i) reacting an aromatic hydroxy compound with at least some ketone and at least some isoalkenylphenol at the lowest possible temperature in a first of a cascade of at least two reactors to form a reaction mixture and continuing the reaction at increasing temperature in the succeeding at least one reactor into which ketone and isoalkenylphenol are apportioned, and removing acidic constituents from the reaction mixture, and (ii) distilling water of reaction and residual ketone from the reaction mixture to form a dry reaction mixture, and (iii) distilling phenol from said dry reaction mixture to obtain a first bottom product, and (iv) distilling said first bottom product to obtain a distillate rich in dihydroxydiarylalkane and a second bottom product containing high-boiling fractions, and (v) distilling said distillate to obtain a second distillate containing fractions which are lower-boiling than dihydroxydiarylalkane and to obtain a third bottom product containing bisphenol, (vi) combining said second bottom product with said second distillate to form a combination and continuously cracking said combination in the presence of a base, in a multi-step reactive distillation, to produce (a) phenol and isoalkenylphenol which pass overhead and (b) a high-boiling bottom product, (vii) acidifying and cracking said high-boiling bottom product in reactive distillation, to produce phenol and resin, and (viii) recycling the phenol distillate obtained in (vii) and the phenol and isoalkenylphenol produced in (vi), optionally after purification, to said reaction mixture said aromatic hydroxy compounds being unsubstituted in the p-position and containing no second order substituents.
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Abstract
The present invention relates to a process for the continuous production of dihydroxydiphenylalkanes (bisphenols) by the reaction of fresh phenol, and of phenol obtained from the cracking of by-products, with isoalkenylphenol and ketone. In the course of this process, the reaction mixture is worked up by distillation and a high purity bisphenol is produced. The bottom products and distillates containing the by-products are cracked under basic conditions and optionally thereafter under acidic conditions. The cracked products, which substantially consist of isoalkenylphenol and phenol, are recycled, optionally after purification, with the phenol obtained during the purification of bisphenol, to the reaction to form bisphenol, and the residue obtained from cracking is disposed of.
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1 Claim
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1. A continuous process for the production of dihydroxydiarylalkane comprising
(i) reacting an aromatic hydroxy compound with at least some ketone and at least some isoalkenylphenol at the lowest possible temperature in a first of a cascade of at least two reactors to form a reaction mixture and continuing the reaction at increasing temperature in the succeeding at least one reactor into which ketone and isoalkenylphenol are apportioned, and removing acidic constituents from the reaction mixture, and (ii) distilling water of reaction and residual ketone from the reaction mixture to form a dry reaction mixture, and (iii) distilling phenol from said dry reaction mixture to obtain a first bottom product, and (iv) distilling said first bottom product to obtain a distillate rich in dihydroxydiarylalkane and a second bottom product containing high-boiling fractions, and (v) distilling said distillate to obtain a second distillate containing fractions which are lower-boiling than dihydroxydiarylalkane and to obtain a third bottom product containing bisphenol, (vi) combining said second bottom product with said second distillate to form a combination and continuously cracking said combination in the presence of a base, in a multi-step reactive distillation, to produce (a) phenol and isoalkenylphenol which pass overhead and (b) a high-boiling bottom product, (vii) acidifying and cracking said high-boiling bottom product in reactive distillation, to produce phenol and resin, and (viii) recycling the phenol distillate obtained in (vii) and the phenol and isoalkenylphenol produced in (vi), optionally after purification, to said reaction mixture said aromatic hydroxy compounds being unsubstituted in the p-position and containing no second order substituents.
Specification