Process of the decaffeination of green coffee beans

Claim 2

A continuous process for extracting caffeine from an aqueous solution containing same with an adsorbent and regenerating the adsorbent with water, said process comprising the steps of: (1) contacting a caffeine-laden aqueous solution at a temperature of about 50° to about 100° C. with a macroporous synthetic polymer resin adsorbent produced by polymerizing a monomer containing aromatic ring systems and polar acidic groups having a P K value greater than 6.5 and wherein the ratio of to adsorption capacity for said caffeine to total ion exchange capacity of said polymer is greater than 1 and less than 25 and thereafter (2) regenerating the caffeine-laden resin adsorbent by contacting it with water as the sole regenerating means and removing the adsorbed caffeine from said resin.

Claim 3

The process of claim 1 wherein said adsorbent resin is a highly porous, very weak-acid resin having a phenolic matrix.

Claim 4

A process according to claim 1, wherein a formophenolic resin is used.

Claim 5

A continuous process for the decaffeination of green coffee beans comprising (a) a treating caffeine-containing green coffee beans at a temperature of about 50° to about 100° C. with an aqueous solution containing green coffee bean solubles which solution is caffeine unsaturated, and thereby extracting a predetermined amount of caffeine from said beans and forming an aqueous caffeine-containing extract; (b) treating the extract produced in step (a) at a temperature of about 50° to 100° C. with a synthetic polymer resin, said polymer produced by the polymerization or the copolymerization of monomers containing aromatic ring systems and acidic groups, the monomer containing said acidic group having a P Ka of at least 6.5, and thereby extracting a predetermined amount of caffeine from said extract producing a caffeine loaded resin and an aqueous solution, and thereafter (c) recirculating the aqueous solution of step (b) to use as the aqueous extracting solution of step (a) (d) regenerating the caffeine-laden resin adsorbent by contacting it with water as the sole regenerating means and removing the adsorbed caffeine from said resin.

Claim 6

A continuous process for the decaffeination of green coffee beans comprising (a) a treating caffeine-containing green coffee beans at a temperature of about 50° to about 100° C. with an aqueous solution containing green coffee bean solubles which solution is caffeine unsaturated, and thereby extracting a predetermined amount of caffeine from said beans and forming an aqueous caffeine-containing extract; (b) treating the extract produced in step (a) at a temperature of about 50° to 100° C. with a synthetic polymer resin, said polymer produced by the polymerization or the copolymerization of monomers containing aromatic ring systems and acidic groups, the monomer containing said acidic group having a P Ka of at least 6.5, and thereby extracting a predetermined amount of caffeine from said extract producing a caffeine loaded resin and an aqueous solution, and thereafter (c) recirculating the aqueous solution of step (b) to use as the aqueous extracting solution of step (a) (d) regenerating the caffeine-laden resin adsorbent by contacting it with water as the sole regenerating means and removing the adsorbed caffeine from said resin.

Claim 7

The process according to claim 4 wherein said polymer resin has a ratio of the total adsorption capacity for caffeine to the total ion exchange capacity greater than 1 and less than 25.

Claim 8

A continuous aqueous process for the decaffeination of green coffee beans devoid of organic solvents and regenerating the resin employed, said process comprising the steps of: (a) treating caffeine-containing green coffee beans at a temperature of about 50° to about 100° C. with an aqueous solution containing green coffee bean solubles which solution is caffeine unsaturated, and thereby extracting a predetermined amount of caffeine from said beans and forming an aqueous caffeine-containing extract containing green coffee bean solubles; (b) treating the extract produced in step (a) at a temperature of about 50° to about 100° C. with a synthetic polymer resin highly selective in the adsorption of caffeine in an aqueous system containing chlorogenic acid and caffeine, said polymer produced by the polymerization or the copolymerization of monomers containing aromatic ring systems and acidic groups, the monomer containing said acidic group having a P Ka of at least 6.5, the ratio of total adsorption capacity for caffeine to total ion exchange capacity of said polymer being greater than 1 and less than 25, and thereby extracting a predetermined amount of caffeine from said extract producing a caffeine loaded resin and an aqueous solution substantially free from caffeine, and thereafter regenerating the resin by (c) rinsing the solids and caffeine-loaded resin produced in step (b) with cold water at a temperature of about 0° C. to about ambient thereby extracting, removing and discharging the non-caffeine solids from the resin leaving a caffeine loaded resin, (d) rinsing the caffeine-loaded resin remaining from step (c) with hot water at a temperature of about 50° C. to about 100° C. thereby extracting, removing and discharging caffeine from the resin and freeing the resin of green coffee bean solids and caffeine, and thereafter (e) reusing the resin of step (d), the entire process being conducted in the absence of organic solvents.

Claim 9

A continuous aqueous process for the decaffeination of green coffee beans devoid of organic solvents and regenerating the resin employed, said process comprising the steps of: (a) treating caffeine-containing green coffee beans at a temperature of about 50° to about 100° C. with an aqueous solution containing green coffee bean solubles which solution is caffeine unsaturated, and thereby extracting a predetermined amount of caffeine from said beans and forming an aqueous caffeine-containing extract containing green coffee bean solubles; (b) treating the extract produced in step (a) at a temperature of about 50° to about 100° C. with a synthetic polymer resin highly selective in the adsorption of caffeine in an aqueous system containing chlorogenic acid and caffeine, said polymer produced by the polymerization or the copolymerization of monomers containing aromatic ring systems and acidic groups, the monomer containing said acidic group having a P Ka of at least 6.5, the ratio of total adsorption capacity for caffeine to total ion exchange capacity of said polymer being greater than 1 and less than 25, and thereby extracting a predetermined amount of caffeine from said extract producing a caffeine loaded resin and an aqueous solution substantially free from caffeine, and thereafter regenerating the resin by (c) rinsing the solids and caffeine-loaded resin produced in step (b) with cold water at a temperature of about 0° C. to about ambient thereby extracting, removing and discharging the non-caffeine solids from the resin leaving a caffeine loaded resin, (d) rinsing the caffeine-loaded resin remaining from step (c) with hot water at a temperature of about 50° C. to about 100° C. thereby extracting, removing and discharging caffeine from the resin and freeing the resin of green coffee bean solids and caffeine, and thereafter (e) reusing the resin of step (d), the entire process being conducted in the absence of organic solvents.

Claim 10

The process according to claim 6 including continuing the hot water rinsing of step (c) until the wash water passed from said resin is reduced in caffeine content to less than 0.5 g/l.

Claim 11

The process according to claim 6 wherein the volume of cold water used in step (c) is from 1 to 15 times the void volume of the loaded resin and the velocity of cold rinse water through the bed is between 0.25 and 10 cm/minute.

Claim 12

The process according to claim 6 or 8 wherein the volume of hot water used in step (d) is from 25 to 100 times the void volume of the loaded resin and the velocity of hot rinse water through the bed is between 0.25 and 10 cm/minute.

Claim 13

The process according to claim 1 or 6 wherein said ratio is between about 5 and 15.

Claim 14

The process according to claim 10 wherein said ratio is about 10.