Process for separating esters of fatty acids by selective adsorption

Claim 2

A process for separating an ester of an unsaturated fatty acid from a mixture comprising an ester of an unsaturated fatty acid and an ester of a saturated fatty acid which process comprises contacting at a temperature within the range of from about 20° C. to about 200° C. and a pressure within the range from about atmospheric to about 500 psig. said mixture with an adsorbent comprising a X or Y zeolite containing at exchangeable cationic sites at least one cation selected from the group consisting of cations of metals of Group IA of the Periodic Table of Elements and combinations thereof thereby selectively adsorbing said ester of an unsaturated fatty acid and thereafter recovering said ester of an unsaturated fatty acid.

Claim 3

The process of claim 1 further characterized in that said adsorbent contains sodium cations at the exchangeable cationic sites.

Claim 4

The process of claim 1 further characterized in that said adsorbent contains potassium cations at the exchangeable cationic sites.

Claim 5

The process of claim 1 further characterized in that it is effected in the liquid phase.

Claim 6

The process of claim 1 further characterized in that said ester of an unsaturated fatty acid and said ester of a saturated fatty acid each contain from about 8 to about 30 carbon atoms per molecule.

Claim 7

The process of claim 5 further characterized in that said ester of an unsaturated fatty acid and said ester of a saturated fatty acid are methyl esters.

Claim 8

The process of claim 6 further characterized in that said ester of a saturated fatty acid is methyl palmitate or methyl stearate.

Claim 9

The process of claim 6 further characterized in that said ester of an unsaturated fatty acid is methyl oleate.

Claim 10

The process of claim 6 further characterized in that said ester of an unsaturated fatty acid is methyl linoleate.

Claim 11

The process of claim 1 further characterized in that said ester of an unsaturated fatty acid is recovered by desorption with a desorbent material comprising a monocyclic aromatic hydrocarbon.

Claim 12

A process for separating an ester of an unsaturated fatty acid from a mixture comprising an unsaturated fatty acid and an ester of a saturated fatty acid which process comprises the steps of: a. contacting said mixture at a temperature within the range of from about 20° C. to about 200° C. and a pressure from about atmospheric pressure to about 500 psig. with an adsorbent comprising a X or a Y zeolite containing at the exchangeable cationic sites at least one cation selected from the group consisting of cations of metals of Group IA of the Periodic Table of Elements and combinations thereof thereby selectively adsorbing said ester of an unsaturated fatty acid; b. removing from the adsorbent a raffinate stream comprising said ester of a saturated fatty acid; c. contacting said adsorbent at a temperature within the range of from about 20° C. to about 200° C. and a pressure from about atmospheric pressure to about 500 psig. with a desorbent material comprising a monocyclic aromatic hydrocarbon to effect the desorption of said ester of an unsaturated fatty acid from said adsorbent; and, d. removing from said adsorbent an extract stream comprising said ester of an unsaturated fatty acid.

Claim 13

A process for separating an ester of an unsaturated fatty acid from a mixture comprising an unsaturated fatty acid and an ester of a saturated fatty acid which process comprises the steps of: a. contacting said mixture at a temperature within the range of from about 20° C. to about 200° C. and a pressure from about atmospheric pressure to about 500 psig. with an adsorbent comprising a X or a Y zeolite containing at the exchangeable cationic sites at least one cation selected from the group consisting of cations of metals of Group IA of the Periodic Table of Elements and combinations thereof thereby selectively adsorbing said ester of an unsaturated fatty acid; b. removing from the adsorbent a raffinate stream comprising said ester of a saturated fatty acid; c. contacting said adsorbent at a temperature within the range of from about 20° C. to about 200° C. and a pressure from about atmospheric pressure to about 500 psig. with a desorbent material comprising a monocyclic aromatic hydrocarbon to effect the desorption of said ester of an unsaturated fatty acid from said adsorbent; and, d. removing from said adsorbent an extract stream comprising said ester of an unsaturated fatty acid.

Claim 14

The process of claim 11 further characterized in that said adsorbent contains sodium cations at the exchangeable cationic sites.

Claim 15

The process of claim 11 further characterized in that said adsorbent contains potassium cations at the exchangeable cationic sites.

Claim 16

The process of claim 11 further characterized in that said ester of an unsaturated fatty acid and said ester of a saturated fatty acid each contain from about 8 to about 30 carbon atoms per molecule.

Claim 17

The process of claim 14 further characterized in that said ester of an unsaturated fatty acid and said ester of a saturated fatty acid are methyl esters.

Claim 18

The process of claim 15 further characterized in that said ester of a saturated fatty acid is methyl palmitate or methyl stearate.

Claim 19

The process of claim 15 further characterized in that said ester of an unsaturated fatty acid is methyl oleate.

Claim 20

The process of claim 15 further characterized in that said ester of an unsaturated fatty acid is methyl linoleate.

Claim 21

The process of claim 11 further characterized in that said monocyclic aromatic hydrocarbon is selected from the group consisting of benzene, toluene, xylenes, ethylbenzene and diethylbenzenes.

Claim 22

A process for separating an ester of an unsaturated fatty acid from a mixture comprising an ester of an unsaturated fatty acid and an ester of a saturated fatty acid which process employs an adsorbent comprising a X or a Y zeolite containing at exchangeable cationic sites at least one cation selected from the group consisting of cations of metals of Group IA of the Periodic Table of Elements and combinations thereof which process comprises the steps of: a. maintaining net fluid flow through a column of said absorbent 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 adsorption 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 a temperature within the range of from about 20° C. to about 200° C. and a pressure within the range of from about atmospheric to about 500 psig. to effect the selective adsorption of said ester of an unsaturated fatty acid by said adsorbent in said adsorption zone and withdrawing a raffinate output stream from said adsorption zone; f. passing a desorbent material comprising a monocyclic aromatic hydrocarbon into said desorption zone at a temperature within the range of from about 20° C. to about 200° C. and a pressure within the range of from about atmospheric to about 500 psig. to effect the displacement of said ester of an unsaturated fatty acid from the adsorbent in said desorption zone; g. withdrawing an extract output stream comprising said ester of an unsaturated fatty acid and desorbent material from said desorption zone; h. passing at least a portion of said extract output stream to a separation means and therein separating at separation conditions at least a portion of said desorbent material; 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 streams.

Claim 23

A process for separating an ester of an unsaturated fatty acid from a mixture comprising an ester of an unsaturated fatty acid and an ester of a saturated fatty acid which process employs an adsorbent comprising a X or a Y zeolite containing at exchangeable cationic sites at least one cation selected from the group consisting of cations of metals of Group IA of the Periodic Table of Elements and combinations thereof which process comprises the steps of: a. maintaining net fluid flow through a column of said absorbent 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 adsorption 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 a temperature within the range of from about 20° C. to about 200° C. and a pressure within the range of from about atmospheric to about 500 psig. to effect the selective adsorption of said ester of an unsaturated fatty acid by said adsorbent in said adsorption zone and withdrawing a raffinate output stream from said adsorption zone; f. passing a desorbent material comprising a monocyclic aromatic hydrocarbon into said desorption zone at a temperature within the range of from about 20° C. to about 200° C. and a pressure within the range of from about atmospheric to about 500 psig. to effect the displacement of said ester of an unsaturated fatty acid from the adsorbent in said desorption zone; g. withdrawing an extract output stream comprising said ester of an unsaturated fatty acid and desorbent material from said desorption zone; h. passing at least a portion of said extract output stream to a separation means and therein separating at separation conditions at least a portion of said desorbent material; 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 streams.

Claim 24

The process of claim 20 further characterized in that it includes the step of passing at least a portion of said raffinate output stream to a separation means and therein separating at separation conditions at least a portion of said desorbent material to produce a raffinate product having a reduced concentration of desorbent material.

Claim 25

The process of claim 20 further characterized in that it includes the step of maintaining a buffer zone immediately upstream from said desorption zone, said buffer zone defined as the adsorbent located between the desorbent input stream at a downstream boundary of said buffer zone and a raffinate output stream at an upstream boundary of said buffer zone.

Claim 26

The process of claim 20 further characterized in that said adsorbent contains sodium cations at the exchangeable cationic sites.

Claim 27

The process of claim 20 further characterized in that said adsorbent contains potassium cations at the exchangeable cationic sites.

Claim 28

The process of claim 20 further characterized in that said ester of an unsaturated fatty acid and said ester of a saturated fatty acid each contain from about 8 to about 30 carbon atoms per molecule.

Claim 29

The process of claim 25 further characterized in that said ester of an unsaturated fatty acid and said ester of a saturated fatty acid are methyl esters.

Claim 30

The process of claim 26 further characterized in that said ester of a saturated fatty acid is methyl palmitate or methyl stearate.

Claim 31

The process of claim 26 further characterized in that said ester of an unsaturated fatty acid is methyl oleate.

Claim 32

The process of claim 26 further characterized in that said ester of an unsaturated fatty acid is methyl linoleate.