Multi-stage pervaporation process run at progressively higher vacuum, higher temperature or both at each successive retentate stage

Claim 2

A process for separating a multi-component feed stream into fractions of different molecular type and of different boiling point comprising feeding the multi-component feed stream to a multi-stage membrane pervaporation separation unit, the multi-component stream being the feed to a first separation stage producing a permeate and a retentate, the retentate from the first and each succeeding stage in turn being the feed to the next succeeding separation stage wherein the retentate which constitutes the feed to the next succeeding stage is heated to a temperature higher than that used in the preceding stage and wherein each succeeding permeation stage is run at a higher vacuum than that used in the preceding permeation stage to thereby fractionate the multi-component stream into numerous fractions of different molecular type and different boiling point.

Claim 3

A process for separating a multi-component feed stream into fractions of different molecular type and of different boiling point comprising feeding the multi-component feed stream to a multi-stage membrane pervaporation separation unit run at isothermal conditions wherein the multi-component stream is fed to a first membrane pervaporation separation stage run at a vacuum sufficient to recover the lightest component as a permeate and produce a retentate, the retentate from the first and each succeeding separation stage of the multi-stage separation unit constituting the feed to the next succeeding separation stage wherein each succeeding separation stage is run at a higher vacuum than the preceding separation stage to thereby fractionate the multi-component stream into numerous fractions of different molecular type and different boiling point.

Claim 4

A process for separating a multi-component feed stream into fractions of different molecular type and of different boiling point comprising feeding the multi-component feed stream to a multi-stage membrane pervaporation separation unit run at isothermal conditions wherein the multi-component stream is fed to a first membrane pervaporation separation stage run at a vacuum sufficient to recover the lightest component as a permeate and produce a retentate, the retentate from the first and each succeeding separation stage of the multi-stage separation unit constituting the feed to the next succeeding separation stage wherein each succeeding separation stage is run at a higher vacuum than the preceding separation stage to thereby fractionate the multi-component stream into numerous fractions of different molecular type and different boiling point.

Claim 5

A process for separating a multi-component feed stream into fractions of different molecular type and of different boiling point comprising feeding the multi-component feed stream to a multi-stage membrane pervaporation separation unit run at constant vacuum wherein the feed to a first membrane pervaporation separation stage is heated to a temperature sufficient to provide the heat of vaporization of the lightest component of the multi-component feed stream to produce a permeate and a retentate and wherein the retentate from the first and each succeeding separation stage of the multi-stage separation unit which constitutes the feed to the next succeeding separation stage is heated to a temperature higher than that employed in the preceding separation stage to thereby fractionate the multi-component steam into numerous fractions of different molecular type and different boiling point

Claim 6

A process for separating a multi-component feed stream into fractions of different molecular type and of different boiling point comprising feeding the multi-component feed stream to a multi-stage membrane pervaporation separation unit run at constant vacuum wherein the feed to a first membrane pervaporation separation stage is heated to a temperature sufficient to provide the heat of vaporization of the lightest component of the multi-component feed stream to produce a permeate and a retentate and wherein the retentate from the first and each succeeding separation stage of the multi-stage separation unit which constitutes the feed to the next succeeding separation stage is heated to a temperature higher than that employed in the preceding separation stage to thereby fractionate the multi-component steam into numerous fractions of different molecular type and different boiling point

Claim 7

The method of claim 1, 2 or 3 wherein the multi-component feed stream is a mixture of aromatic hydrocarbons and non-aromatic hydrocarbons.

Claim 8

The method of claim 4 wherein the membrane used in each separation stage is the same or different and selected from membranes made of cellulose esters, cellulose ethers, combinations of cellulose esters and ethers, polyurea-urethane copolymers.