Process for separating triglylcerides by degree of unsaturation

Claim 2

A process for separating triglycerides having the higher degree of unsaturation from a mixture of triglycerides having varying lower degrees of unsaturations, said process comprising contacting said mixture at adsorption conditions with an adsorbent comprising an omega-type zeolite exchanged with Cu, H or K at exchangeable sites thereby selectively absorbing said triglycerides having the higher degree of unsaturation thereon and desorbing at desorption conditions said adsorbed triglycerides with a desorbent selected from the group consisting of toluene, ketones and mixtures of ketones with paraffin hydrocarbons.

Claim 3

The process of claim 1 wherein said desorbent is selected from the group consisting of methylethyl ketone, diethyl ketone, methyl isobutyl ketone, acetone and mixtures thereof with hexane.

Claim 4

The process of claim 1 wherein said desorbent material comprises methyl isobutyl ketone.

Claim 5

The process of claim 2 wherein said desorbent material is toluene.

Claim 6

The process of claim 1 wherein said adsorption conditions include a temperature within the range of from about 20° C. to about 200° C. and a pressure sufficient to maintain liquid phase.

Claim 7

The process of claim 1 wherein said more highly unsaturated triglyceride is polyunsaturated trilinolein and said less highly unsaturated triglyceride is triolein.

Claim 8

A process for separating a triglyceride having a higher degree of unsaturation from a feed mixture comprising triglyceride having varying degrees of unsaturation, which process employs an adsorbent selected from the group consisting of an omega zeolite exchanged with Cu, H or K at exchangeable cationic sites which process comprises the steps of: (a) maintaining net fluid flow through a column of said adsorbent in a single direction, which column contains at least three zones having separate operational functions occurring therein and being serially interconnected with the terminal zones of said column connected to provide a continuous connection of said zones; (b) maintaining an adsorption zone in said column, said zone defined by the adsorbent located between a feed input stream at an upstream boundary of said zone and a raffinate output stream at a downstream boundary of said zone; (c) maintaining a purification zone immediately upstream from said aosorption zone, said purification zone defined by the adsorbent located between an extract output stream at an upstream boundary of said purification zone and said feed input stream at a downstream boundary of said purification zone; (d) maintaining a desorption zone immediately upstream from said purification zone, said desorption zone defined by the adsorbent located between a desorbent input stream at an upstream boundary of said zone and said extract output stream at a downstream boundary of said zone; (e) passing said feed mixture into said adsorption zone at adsorption conditions to effect the selective adsorption of said triglyceride by said adsorbent in said adsorption zone and withdrawing a raffinate output stream from said adsorption zone; (f) passing a desorbent material comprising toluene, methyethyl ketone, methylisobutyl ketone, acetone or diethyl ketone into said desorption zone at desorption conditions to effect the displacement of said triglyceride from the adsorbent in said desorption zone; (g) withdrawing an extract output stream comprising said triglyceride and desorbent material from said desorption zone; (h) withdrawing a raffinate output stream comprising said triglyceride from said desorption zone; and (i) periodically advancing through said column of adsorbent in a downstream direction with respect to fluid flow in said adsorption zone the feed input stream, raffinate output stream, desorbent input stream, and extract output stream to effect the shifting of zones through said adsorbent and the production of extract output and raffinate output stream.

Claim 9

A process for separating a triglyceride having a higher degree of unsaturation from a feed mixture comprising triglyceride having varying degrees of unsaturation, which process employs an adsorbent selected from the group consisting of an omega zeolite exchanged with Cu, H or K at exchangeable cationic sites which process comprises the steps of: (a) maintaining net fluid flow through a column of said adsorbent in a single direction, which column contains at least three zones having separate operational functions occurring therein and being serially interconnected with the terminal zones of said column connected to provide a continuous connection of said zones; (b) maintaining an adsorption zone in said column, said zone defined by the adsorbent located between a feed input stream at an upstream boundary of said zone and a raffinate output stream at a downstream boundary of said zone; (c) maintaining a purification zone immediately upstream from said aosorption zone, said purification zone defined by the adsorbent located between an extract output stream at an upstream boundary of said purification zone and said feed input stream at a downstream boundary of said purification zone; (d) maintaining a desorption zone immediately upstream from said purification zone, said desorption zone defined by the adsorbent located between a desorbent input stream at an upstream boundary of said zone and said extract output stream at a downstream boundary of said zone; (e) passing said feed mixture into said adsorption zone at adsorption conditions to effect the selective adsorption of said triglyceride by said adsorbent in said adsorption zone and withdrawing a raffinate output stream from said adsorption zone; (f) passing a desorbent material comprising toluene, methyethyl ketone, methylisobutyl ketone, acetone or diethyl ketone into said desorption zone at desorption conditions to effect the displacement of said triglyceride from the adsorbent in said desorption zone; (g) withdrawing an extract output stream comprising said triglyceride and desorbent material from said desorption zone; (h) withdrawing a raffinate output stream comprising said triglyceride from said desorption zone; and (i) periodically advancing through said column of adsorbent in a downstream direction with respect to fluid flow in said adsorption zone the feed input stream, raffinate output stream, desorbent input stream, and extract output stream to effect the shifting of zones through said adsorbent and the production of extract output and raffinate output stream.

Claim 10

The process of claim 7 wherein said adsorption and desorption conditions include a temperature within the range of from about 20° C. to about 200° C. and a pressure sufficient to maintain liquid phase.

Claim 11

The process of claim 7 wherein a buffer zone is maintained immediately upstream from said desorption zone, said buffer zone is defined as the adsorbent located between the desorbent input stream as the downstream boundary of said buffer zone and the raffinate output stream at an upstream boundary of said buffer zone.

Claim 12

A process for separating triglycerides having the lower degree of unsaturation from a mixture of triglycerides having varying degrees of unsaturation, said process comprising contacting said mixture at adsorption conditions with an adsorbent comprising carbon thereby selectively adsorbing said triglycerides having the lower degree of unsaturation and desorbing at desorption conditions said adsorbed triglycerides with a desorbent selected from the group consisting of toluene, ketones and mixtures of ketones with paraffin hydrocarbons.

Claim 13

A process for separating triglycerides having the lower degree of unsaturation from a mixture of triglycerides having varying degrees of unsaturation, said process comprising contacting said mixture at adsorption conditions with an adsorbent comprising carbon thereby selectively adsorbing said triglycerides having the lower degree of unsaturation and desorbing at desorption conditions said adsorbed triglycerides with a desorbent selected from the group consisting of toluene, ketones and mixtures of ketones with paraffin hydrocarbons.

Claim 14

The process of claim 10 wherein said desorbent is toluene.

Claim 15

The process of claim 10 wherein said adsorption conditions include a temperature within the range of from about 20° C. to about 200° C. and a pressure sufficient to maintain a liquid phase.

Claim 16

A process for separating triglycerides having a higher degree of unsaturation from a mixture of triglycerides having varying lower degrees of unsaturations including monunsaturated triglycerides, said process comprising contacting said mixture at adsorption conditions with an adsorbent comprising copper-exchanged omega zeolite thereby selectively absoring said triglycerides having the higher degree of unsaturation thereon and desorbing in a first desorption step at desorption conditions said triglycerides with lower degree of unsaturation with a desorbent consisting of toluene thereby obtaining triglycerides enriched in less unsaturated triglycerides, desorbing in a second desorption step at desorption conditions, said triglycerides having high degree of unsaturation with a desorbent selected from the group consisting of ketones and mixtures of ketones with paraffin hydrocarbons.

Claim 17

A process for separating triglycerides having a higher degree of unsaturation from a mixture of triglycerides having varying lower degrees of unsaturations including monunsaturated triglycerides, said process comprising contacting said mixture at adsorption conditions with an adsorbent comprising copper-exchanged omega zeolite thereby selectively absoring said triglycerides having the higher degree of unsaturation thereon and desorbing in a first desorption step at desorption conditions said triglycerides with lower degree of unsaturation with a desorbent consisting of toluene thereby obtaining triglycerides enriched in less unsaturated triglycerides, desorbing in a second desorption step at desorption conditions, said triglycerides having high degree of unsaturation with a desorbent selected from the group consisting of ketones and mixtures of ketones with paraffin hydrocarbons.

Claim 18

The process of claim 13 wherein the second desorbent comprises methyl isobutyl ketone.

Claim 19

The process of claim 14 wherein the second desorbent additionally comprises isooctane.

Claim 20

A process for separating triglycerides having varying lower degrees of unsaturation from a mixture of triglycerides having varying degrees of unsaturation, said process comprising contacting said mixture at adsorption conditions with an adsorbent comprising carbon, thereby selectively adsorbing said triglycerides having lower degrees of unsaturation thereon and desorbing said adsorbed triglycerides at desorption conditions with a desorbent comprising toluene.

Claim 21

A process for separating triglycerides having varying lower degrees of unsaturation from a mixture of triglycerides having varying degrees of unsaturation, said process comprising contacting said mixture at adsorption conditions with an adsorbent comprising carbon, thereby selectively adsorbing said triglycerides having lower degrees of unsaturation thereon and desorbing said adsorbed triglycerides at desorption conditions with a desorbent comprising toluene.

Claim 22

The process of claim 16 wherein said triglycerides having lower degrees of unsaturation comprise monounsaturated triglycerides.