Abstract Resorcinol is prepared in high yield and purity by an improved process through superacid (such as perfluorinated alkanesulfonic acids of one to eighteen carbon atoms or polymeric perfluorinated resinsulfonic acids, such as acidified Nafion-H, catalyzed cleavage-rearrangement reaction of meta-bis(2-hydroperoxy-2-propyl)-benzene (meta-diisopropylbenzene dihydroperoxide). Part of the process is the preparation of needed meta-diisopropylbenzene in high purity (98-100%) substantially free of other isomers by treating any mixture of diisopropylbenzenes with an excess of anhydrous hydrogen fluoride or a perfluorinated alkanesulfonic acid of one to six carbon atoms and a Lewis acid fluoride, or by alkylating (transalkylating) cumene with a propyl alkylating agent in the aforementioned superacid systems.
The process of producing resorcinol, selectively in high yield, which comprises reacting meta-diisopropylbenzene dihydroperoxide in the presence of a fluoroalkanesulfonic acid superacid cleavage rearrangement catalyst at a temperature sufficient to produce resorcinol selectively with high yields.
Claim 2
Dependent Claim
36 words
The process of producing resorcinol, selectively in high yield, which comprises reacting meta-diisopropylbenzene dihydroperoxide in the presence of a fluoroalkanesulfonic acid superacid cleavage rearrangement catalyst at a temperature sufficient to produce resorcinol selectively with high yields.
Claim 3
Dependent Claim
26 words
The process of claim 1 in which the superacid catalyst is a perfluorinated alkanesulfonic acid of one to eighteen carbon atoms or a perfluorinated resinsulfonic acid.
Claim 4
Dependent Claim
45 words
The process of producing resorcinol, selectively and in high yield, from meta-diisopropylbenzene dihydroperoxide in situ which comprises reacting meta-bis-(2-hydroxy-2-propyl)-benzene with hydrogen peroxide in the presence of a superacid catalyst as defined in claim 2 with azeotropic removal of water and acetone formed during the reaction.