Distillative separation of liquid mixtures containing aliphatic alcohols

Claim 2

A process for the distillative separation in a fractionating column of a liquid mixture containing at least one aliphatic alcohol into a higher-boiling alcohol-containing fraction and a lower-boiling fraction of the other liquids, which process comprises: contacting the alcohol in a middle zone of the column with a C 2 - to C 5 -alkanal and with a non-volatile or only slightly volatile acid; maintaining said middle zone of the column under conditions of temperature and pressure sufficient to cause a transient bonding of the alcohol to the alkanal in the presence of said acid so as to form a higher boiling acetal or hemiacetal; heating the column such that substances more volatile than the alcohol pass into the upper zone of the column for removal therefrom as a top product; cleaving said acetal or hemiacetal in the lower zone of the column into its respective alcohol and alkanal components; and separating the alcohol from the bottom product of the column.

Claim 3

A process as claimed in claim 1, wherein (a) the alcohol-containing starting mixture is introduced into the middle zone of the column at a temperature at which the lower-boiling fraction vaporizes completely but the higher-boiling fraction does not, (b) an alkanal which is higher-boiling than the alcohol is introduced into the upper zone of the column, (c) an aqueous solution of the acid is introduced into the upper quarter of the column, (d) the lower-boiling fraction is taken off at the top and is fractionated in a conventional manner, where appropriate with the aid of side strippers and (e) the alcohol- and alkanal-containing aqueous acidic fraction which forms in the lower zone of the column is taken off from there and is fractionated, in a side stripper, to give an alcohol-containing fraction and a mixture of aqueous acid and alkanal, and the last-mentioned mixture is returned to the upper zone of the column.

Claim 4

A process as claimed in claim 1 including the steps of contacting liquid from said middle zone of the column with an acidic ion exchanger as a non-volatile acid, and conducting water from the ion exchanger to the lower zone of the column.

Claim 5

A process as claimed in claim 1, wherein (a) the alcohol-containing starting mixture is introduced into the middle zone of the column at a temperature at which the lower-boiling fraction vaporizes completely but the higher-boiling fraction does not, (b) a C 2 - to C 5 -alkanal which is lower-boiling than the alcohol is introduced into the middle or lower zone of the column, (c) an aqueous solution of the acid is introduced into the upper quarter of the column, (d) the lower-boiling fraction is taken off at the top, and the alkanal which passes, together with the lower-boiling fraction, into the upper zone of the column is separated off and returned to the middle zone of the column, and (e) the alcohol-containing aqueous fraction which forms in the lower zone of the column is taken off from there and is separated, in a side stripper, into the alcohol or an alcohol-containing fraction, and an aqueous fraction, and the last-mentioned fraction is returned to the upper zone of the column.

Claim 6

A process as claimed in claim 4 wherein said lower-boiling fraction consisting of a plurality of components is fractionated in the upper zone of the column.

Claim 7

A process as claimed in claims 1, 4, 2, 3 or 5 wherein said alkanal is selected from the group consisting of acetaldehyde, propionaldehyde and n-butyraldehyde.