Removal of acetophenone from phenol purification residues

Distillation: processes – separatory – Plural distillations performed on same material – And returning distillation product to a previous...

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203 65, 203 78, 203DIG19, 568324, 568335, 568754, B01D 314, C07C 3774

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052405680

ABSTRACT:
A process for separating phenol obtained by the decomposition of cumene hydroperoxide from high boiling impurities, includes the following steps:
a) feeding phenol rectification bottoms comprising phenol, acetophenone, cumylphenol, alpha-methylstyrene dimers and high boiler residues to a first phenol freeing distillation column A;
b) feeding concentrated bottoms with substantially reduced phenol content from column A to a second residue concentration distillation column B;
c) withdrawing a stream rich in compounds boiling between phenol and residue, particularly cumylphenol, from said column B from a point below the feed and returning at least a portion of said stream to said column A at a point above the feed;
d) recovering overheads from column A comprising at least 95 weight percent phenol; and
e) recovering acetophenone-rich overheads from column B comprising at least 70 weight percent acetophenone.

REFERENCES:
patent: 2727074 (1955-12-01), Bewley
patent: 2750424 (1956-06-01), Armstrong et al.
patent: 2757209 (1956-07-01), Joris
patent: 2906789 (1959-09-01), McNaughton
patent: 3441618 (1969-04-01), Flickinger
patent: 4415409 (1983-11-01), Zudkevitch et al.
patent: 4544776 (1985-10-01), Osterburg et al.
patent: 4559110 (1985-12-01), Swearingen et al.
patent: 5046507 (1991-11-01), O'Donnell
Chemical Abstracts, vol. 83 No. 21 Nov. 24, 1975 Columbus, Ohio, U.S.; Abstract No. 178548m.

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