Process for extracting caffeine from solutions thereof in carbon dioxide under high pressure

Claim 2

A process for decaffeinating green coffee beans without introducing foreign ions into the green coffee beans or green coffee extract, said process comprising the steps of: (a) adjusting the moisture content of the green coffee beans to a value of from about 30 to about 60% by weight; (b) passing water-saturated carbon dioxide through said green coffee beans under a high pressure of about 20.3 to about 40.5 MPa and extracting caffeine from the moistened coffee beans; (c) contacting the caffeine-containing carbon dioxide gas stream of step (b) with a macroporous synthetic polymer resin adsorbent, said resin produced by the polymerization or copolymerization of monomers containing aromatic ring systems and polar acidic groups having a P K value greater than 7, and wherein the ratio in said resin of the total molar adsorption capacity for caffeine, expressed as the number of moles of caffeine adsorbed per kg of resin, to complete saturation, to the total number of acidic groups, expressed as acid equivalents per kg of resin, is between 1 and 25, thereby adsorbing and removing the caffeine from the caffeine-laden carbon dioxide gas stream; (d) returning the carbon dioxide stream of step (c) to step (b) for reuse; (e) regenerating the caffeine-laden adsorbent of step (c) by contacting said resin with water as the sole regenerating material at a temperature in the range of about 50° to about 100° C.; (f) reusing the regenerated resin from step (e) in step (c); and thereafter (g) recovering and drying the decaffeinated green coffee product.

Claim 3

A process according to claim 1, wherein the ratio ranges from 5 to 15.

Claim 4

The process of claim 1 wherein the moist coffee beans are at a temperature of about 20° C. to about 30° C. when contacted with the saturated carbon dioxide of step (b) and wherein step (b) is conducted at a temperature of about 50° C. to about 90° C.

Claim 5

The process of claim 1 or 3 wherein said adsorbent resin is a highly porous, very weak-acid resin having a phenolic matrix.

Claim 6

A process for extracting caffeine from a solution thereof in carbon dioxide with an adsorbent and regenerating the adsorbent with water, said process comprising the steps of: (1) contacting a caffeine-laden carbon dioxide stream under high pressure 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 7 and wherein the ratio of the total molar adsorption capacity for said caffeine, expressed as the number of moles of caffeine adsorbed to complete saturation per kg resin, to the total number of acidic groups, expressed as acid equivalents per kg resin, is from 1 to 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 7

A process for extracting caffeine from a solution thereof in carbon dioxide with an adsorbent and regenerating the adsorbent with water, said process comprising the steps of: (1) contacting a caffeine-laden carbon dioxide stream under high pressure 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 7 and wherein the ratio of the total molar adsorption capacity for said caffeine, expressed as the number of moles of caffeine adsorbed to complete saturation per kg resin, to the total number of acidic groups, expressed as acid equivalents per kg resin, is from 1 to 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 8

The process of claim 5 wherein said adsorbent resin is a highly porous, very weak-acid resin having a phenolic matrix.

Claim 9

The process of claim 5 wherein said ratio is from 5 to 15.

Claim 10

The process according to claim 5, 6 or 7 wherein said synthetic polymeric resin has an adsorbent surface with an aromatic character, and wherein the hydrophobic properties inherent in such aromatic character are suppressed by the presence of a polar, very weakly ionic acidic groups derived from said monomers having a P K value greater than 7.

Claim 11

The process of claim 1 or 5 wherein said monomer having a P K value greater than 7 is selected from the group consisting of phenol, anisol and naphthol.

Claim 12

A process for decaffeinating green coffee beans to produce a substantially caffeine-free green coffee extract without introducing foreign ions into the green coffee beans or green coffee extract, said process comprising the steps of: (a) adjusting the moisture content of the green coffee beans to a value of from about 30 to about 60% by weight; (b) passing water-saturated carbon dioxide through said green coffee beans under a high pressure of about 20.3 to about 40.5 MPa and extracting caffeine from the moistened coffee beans; (c) contacting the caffeine-containing carbon dioxide gas stream of step (b) with a macroporous synthetic polymer resin adsorbent, said resin is a highly porous, very weak-acid resin having a phenolic matrix, produced by the polymerization or copolymerization of monomers containing aromatic ring systems and polar acidic groups having a P K value greater than 7, and wherein the ratio in said resin of the total molar adsorption capacity for caffeine, expressed as the number of moles of caffeine adsorbed per kg of resin, to complete saturation, to the total number of acidic groups, expressed as acid equivalents per kg of resin, is between 1 and 25, thereby adsorbing and removing the caffeine from the caffeine-laden carbon dioxide gas stream; (d) returning the carbon dioxide stream of step (c) to step (b) for reuse; (e) regenerating the caffeine-laden adsorbent of step (c) by contacting said resin with water as the sole regenerating material at a temperature in the range of about 50° to about 100° C.; (f) reusing the regenerated resin from step (e) in step (c); and thereafter (g) recovering and drying the decaffeinated green coffee product.

Claim 13

A process for decaffeinating green coffee beans to produce a substantially caffeine-free green coffee extract without introducing foreign ions into the green coffee beans or green coffee extract, said process comprising the steps of: (a) adjusting the moisture content of the green coffee beans to a value of from about 30 to about 60% by weight; (b) passing water-saturated carbon dioxide through said green coffee beans under a high pressure of about 20.3 to about 40.5 MPa and extracting caffeine from the moistened coffee beans; (c) contacting the caffeine-containing carbon dioxide gas stream of step (b) with a macroporous synthetic polymer resin adsorbent, said resin is a highly porous, very weak-acid resin having a phenolic matrix, produced by the polymerization or copolymerization of monomers containing aromatic ring systems and polar acidic groups having a P K value greater than 7, and wherein the ratio in said resin of the total molar adsorption capacity for caffeine, expressed as the number of moles of caffeine adsorbed per kg of resin, to complete saturation, to the total number of acidic groups, expressed as acid equivalents per kg of resin, is between 1 and 25, thereby adsorbing and removing the caffeine from the caffeine-laden carbon dioxide gas stream; (d) returning the carbon dioxide stream of step (c) to step (b) for reuse; (e) regenerating the caffeine-laden adsorbent of step (c) by contacting said resin with water as the sole regenerating material at a temperature in the range of about 50° to about 100° C.; (f) reusing the regenerated resin from step (e) in step (c); and thereafter (g) recovering and drying the decaffeinated green coffee product.