Separation of citric acid from fermentation broth with a neutral polymeric adsorbent

Claim 2

A process for separating citric acid from a fermentation broth feed mixture comprising contacting said mixture with a neutral polymeric adsorbent selected from the group consisting of an insoluble, crosslinked, polystyrene polymer and a nonionic, hydrophobic, insoluble polyacrylic ester polymer at adsorption conditions selected to selectively adsorb said citric acid.

Claim 3

The process of claim 1 further characterized in that said citric acid is recovered by desorption with a desorbent at desorption conditions.

Claim 4

The process of claim 2 further characterized in that said adsorption and desorption conditions include 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 (3450 kPa gauge).

Claim 5

The process of claim 3 further characterized in that said adsorption is effected in the liquid phase with water.

Claim 6

The process of claim 1 further characterized in that the pH of said feed mixture is lower than the first ionization constant (kPa 1 ) of citric acid.

Claim 7

The process of claim 1 further characterized in that said adsorbent is a neutral styrene-divinylbenzene crosslinked polymer.

Claim 8

The process of claim 1 further characterized in that said adsorbent is a neutral polyacrylic ester resin.

Claim 9

The process of claim 7 further characterized in that said adsorbent has a surface area of at least 10 m 2 /g.

Claim 10

The process of claim 1 wherein said desorbent is water.

Claim 11

The process of claim 1 wherein said desorbent is a mixture of water and acetone.

Claim 12

The process of claim 10 wherein said desorbent contains up to 15% acetone.

Claim 13

The process of claim 11 wherein said desorbent contains from 5-10% acetone.

Claim 14

The process of claim 1 wherein said fermentation broth comprises citric acid, carbohydrates and salts.

Claim 15

A process for separating citric acid from a feed mixture comprising a fermentation broth, which process employs an adsorbent selected from the group consisting of a nonionic, hydrophobic, insoluble crosslinked polystyrene polymer and a nonionic, hydrophobic, insoluble crosslinked polyacrylic ester polymer 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 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 adsorption conditions to effect the selective adsorption of said citric acid by said adsorbent in said adsorption zone and withdrawing a raffinate output stream comprising the nonadsorbed components of said fermentation broth from said adsorption zone; (f) passing a desorbent material into said desorption zone at desorption conditions to effect the displacement of said citric acid from the adsorbent in said desorption zone; (g) withdrawing an extract output stream comprising said citric 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 16

A process for separating citric acid from a feed mixture comprising a fermentation broth, which process employs an adsorbent selected from the group consisting of a nonionic, hydrophobic, insoluble crosslinked polystyrene polymer and a nonionic, hydrophobic, insoluble crosslinked polyacrylic ester polymer 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 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 adsorption conditions to effect the selective adsorption of said citric acid by said adsorbent in said adsorption zone and withdrawing a raffinate output stream comprising the nonadsorbed components of said fermentation broth from said adsorption zone; (f) passing a desorbent material into said desorption zone at desorption conditions to effect the displacement of said citric acid from the adsorbent in said desorption zone; (g) withdrawing an extract output stream comprising said citric 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 17

The process of claim 14 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 18

The process of claim 14 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 the raffinate output stream at an upstream boundary of said buffer zone.

Claim 19

The process of claim 14 further characterized in that said adsorption conditions and desorption conditions include 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 (3450 kPa gauge) to ensure liquid phase.

Claim 20

The process of claim 14 further characterized in that said desorbent comprises water.

Claim 21

The process of claim 14 wherein said desorbent is a mixture of water and acetone.

Claim 22

The process of claim 14 further characterized in that the pH of said feed mixture is lower than the first ionization constant (pKa 1 ) of citric acid.

Claim 23

The process of claim 14 wherein the pH of the said feed mixture is below 3.13.

Claim 24

The process of claim 14 wherein said fermentation broth comprises citric acid, carbohydrates and salts.

Claim 25

The process of claim 22 wherein said fermentation broth additionally contains proteins and amino acids.