Separation of mannose by selective adsorption on zeolitic molecular sieves

Claim 2

A selective adsorption process for the separation of mannose from a mixture containing mannose and at least one of glucose, arabinose, xylose and galactose which comprises contacting said mixture of mannose and at least one of glucose, arabinose, xylose and galactose at a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising at least one crystalline aluminosilicate zeolite selected from the group consisting of BaX, BaY, SrY, NaY, CaY and mixtures thereof, whereby mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said mixture from contact with the zeolite adsorbent and desorbing the adsorbent therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed adsorbate.

Claim 3

A process in accordance with claim 1 wherein the temperature is from about 4° C. to about 150° C.

Claim 4

A process in accordance with claim 1 wherein the temperature is from about 20° C. to about 110° C.

Claim 5

A process in accordance with claim 1 wherein the desorbent is selected from the group consisting of water and mixtures thereof with alcohols or ketones.

Claim 6

A process in accordance with claim 1 wherein the desorbent is water.

Claim 7

A process in accordance with claim 1 wherein said mixture contains mannose and glucose.

Claim 8

A process in accordance with claim 1 wherein said mixture contains mannose and at least one of glucose, arabinose, xylose and galactose, and wherein said zeolite is BaY.

Claim 9

A process in accordance with claim 1 wherein said mixture comprises the hydrolysis product of plant tissue.

Claim 10

A process in accordance with claim 1 wherein said mixture comprises sodium-based sulfite liquor.

Claim 11

A process in accordance with claim 1 wherein said mixture comprises the epimerization product of glucose.

Claim 12

A process for separating mannose from the epimerization product of glucose which contains mannose and glucose, by selective adsorption which comprises contacting said product at a temperature of from about 4° C. to 150° C. and at a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising at least one crystalline aluminosilicate zeolite selected from the group consisting of BaX, BaY, SrY, NaY, CaY and mixtures thereof, whereby the mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said product from contact with the zeolite adsorbent, and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.

Claim 13

A process for separating mannose from the epimerization product of glucose which contains mannose and glucose, by selective adsorption which comprises contacting said product at a temperature of from about 4° C. to 150° C. and at a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising at least one crystalline aluminosilicate zeolite selected from the group consisting of BaX, BaY, SrY, NaY, CaY and mixtures thereof, whereby the mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said product from contact with the zeolite adsorbent, and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.

Claim 14

A process for separating mannose from plant tissue hydrolyzate by selective adsorption which comprises contacting said hydrolyzate at a temperature of from about 4° C. to 150° C. and a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising at least one crystalline aluminosilicate zeolite selected from the group consisting of BaX, BaY, SrY, NaY, CaY and mixtures thereof whereby the mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said hydrolyzate from contact with the zeolite adsorbent, and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.

Claim 15

A process for separating mannose from plant tissue hydrolyzate by selective adsorption which comprises contacting said hydrolyzate at a temperature of from about 4° C. to 150° C. and a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising at least one crystalline aluminosilicate zeolite selected from the group consisting of BaX, BaY, SrY, NaY, CaY and mixtures thereof whereby the mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said hydrolyzate from contact with the zeolite adsorbent, and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.

Claim 16

A two-stage process for separating mannose from plant tissue hydrolyzate which contains mannose, glucose, arabinose, xylose and galactose, by selective adsorption which comprises contacting in a first stage said hydrolyzate at a temperature of from about 4° C. to 150° C. and at a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising a BaY crystalline aluminosilicate zeolite whereby a mixture of mannose and galactose are selectively adsorbed, removing the non-adsorbed portion of said hydrolyzate from contact with the zeolite adsorbent, desorbing the mixture of mannose and galactose therefrom by contacting said adsorbent with a desorbing agent; contacting in a second stage said mixture at a temperature of from about 4° C. to 150° C. and at a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising a BaX crystalline aluminosilicate zeolite whereby mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said mixture from contact with the zeolite adsorbent and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.

Claim 17

A two-stage process for separating mannose from plant tissue hydrolyzate which contains mannose, glucose, arabinose, xylose and galactose, by selective adsorption which comprises contacting in a first stage said hydrolyzate at a temperature of from about 4° C. to 150° C. and at a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising a BaY crystalline aluminosilicate zeolite whereby a mixture of mannose and galactose are selectively adsorbed, removing the non-adsorbed portion of said hydrolyzate from contact with the zeolite adsorbent, desorbing the mixture of mannose and galactose therefrom by contacting said adsorbent with a desorbing agent; contacting in a second stage said mixture at a temperature of from about 4° C. to 150° C. and at a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising a BaX crystalline aluminosilicate zeolite whereby mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said mixture from contact with the zeolite adsorbent and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.

Claim 18

A process for separating mannose from plant tissue hydrolyzate by selective adsorption which comprises contacting said hydrolyzate at a temperature of from about 4° C. to 150° C. and a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising a BaY zeolite whereby the mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said hydrolyzate from contact with the zeolite adsorbent, and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.

Claim 19

A process for separating mannose from plant tissue hydrolyzate by selective adsorption which comprises contacting said hydrolyzate at a temperature of from about 4° C. to 150° C. and a pressure sufficient to maintain the system in the liquid phase with an adsorbent composition comprising a BaY zeolite whereby the mannose is selectively adsorbed thereon, removing the non-adsorbed portion of said hydrolyzate from contact with the zeolite adsorbent, and desorbing the mannose therefrom by contacting said adsorbent with a desorbing agent and recovering the desorbed mannose.