Process for extracting caffeine from solutions thereof in carbon dioxide under high pressure
AssigneeD.E.J. International Research Company B.V.
InventorsGerrit H. D. van der Stegen, Hendricus G. J. de Wilt
Life of this patent
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Abstract
Extraction of caffeine from solutions thereof is accomplished with carbon dioxide under high pressure, using adsorbents which combine a high adsorption capacity for caffeine with such hydrophilic properties that the caffeine-laden adsorbent can be regenerated using water only.
Claims10
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.sub.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.degree. to about 100.degree. C.;
- (f) reusing the regenerated resin from step (e) in step (c);
- and thereafter
- (g) recovering and drying the decaffeinated green coffee product.
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.sub.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.
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.sub.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.degree. to about 100.degree. C.;
- (f) reusing the regenerated resin from step (e) in step (c);
- and thereafter
- (g) recovering and drying the decaffeinated green coffee product.
Dependencies are inferred from the claim text.