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US4820537A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for decaffeinating coffee with a supercritical fluid

Assignee: General Foods Corp
•
Filing: 1988-03-08
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Granted: 1989-04-11
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Expires: 2008-03-08
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Abstract

Abstract A method of extracting caffeine from green coffee beans whereby an essentially caffeine-free supercritical fluid is continuously fed to one end of an extraction vessel containing green coffee beans and caffeine-laden supercritical fluid is continuously withdrawn from the opposite end. A portion of decaffeinated beans is periodically discharged while a fresh portion of undecaffeinated beans is essentially simultaneously charged to the extraction vessel. The caffeine-laden supercritical fluid is fed to a countercurrent water absorber. Supercritical carbon dioxide is the preferred supercritical fluid. The method of the present invention is more efficient than batch processes and produces an improved decaffeinated coffee.

Inventors

  • 👤 Saul N. Katz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 23:03
CPC Classifications
A; A23; A23F; A23F5/00; A23F5/20; A23F5/206

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 347 words
A method of extracting caffeine from green coffee comprising: (a) continuously feeding essentially caffeine-free supercritical carbon dioxide containing non-caffeine solids and saturated with water to the lower end of an elongate, substantially vertical extraction vessel containing green coffee beans having a moisture content of 25-50% by weight, continuously countercurrently contacting the supercritical carbon dioxide and the green coffee beans in said extraction vessel to affect extraction of caffeine from the coffee into the supercritical carbon dioxide, and continuously withdrawing supercritical carbon dioxide containing caffeine and non-caffeine solids from the upper end of the extraction vessel; (b) discharging a portion of the coffee beans in said vessel from the lower end of the extraction vessel, the discharged portion comprising decaffeinated coffee beans; (c) moving the remaining coffee beans downwardly in the extraction vessel to an extent corresponding substantially to the amound of decaffeinated coffee beans discharged from the extraction vessel; (d) introducing moist green coffee beans having a moisture content of 25-50% into the upper end of said extraction vessel in an amount corresponding substantially to the amount of decaffeinated coffee beans discharged from the extraction vessel; (e) maintaining the temperature in the extraction vessel at from 80°-140° C.; (f) feeding the supercritical carbon dioxide containing caffeine and non-caffeine solids withdrawn from the upper end of the extraction vessel to an absorber; (g) continuously countercurrently contacting the supercritical carbon dioxide containing caffeine and non-caffeine solids with water in the absorber at a temperature and pressure substantially the same as in the extraction vessel to extract substantially all of the caffeine contained in the supercritical carbon dioxide but extracting no appreciable amount of said non-caffeine solids therefrom; (h) withdrawing caffeine-laden water from the absorber; (i) withdrawing substantially caffeine-free supercritical carbon dioxide containing non-caffeine solids from said absorber; (j) recycling the substantially caffeine-free supercritical carbon dioxide containing non-caffeine solids to the lower end of the extraction vessel as required by step (a); and (k) periodically repeating steps (b), (c) and (d) while carrying out steps (a) and (e) through (j) to effect extraction of caffeine from said green coffee beans.
Claim 2
Independent Claim 347 words
A method of extracting caffeine from green coffee comprising: (a) continuously feeding essentially caffeine-free supercritical carbon dioxide containing non-caffeine solids and saturated with water to the lower end of an elongate, substantially vertical extraction vessel containing green coffee beans having a moisture content of 25-50% by weight, continuously countercurrently contacting the supercritical carbon dioxide and the green coffee beans in said extraction vessel to affect extraction of caffeine from the coffee into the supercritical carbon dioxide, and continuously withdrawing supercritical carbon dioxide containing caffeine and non-caffeine solids from the upper end of the extraction vessel; (b) discharging a portion of the coffee beans in said vessel from the lower end of the extraction vessel, the discharged portion comprising decaffeinated coffee beans; (c) moving the remaining coffee beans downwardly in the extraction vessel to an extent corresponding substantially to the amound of decaffeinated coffee beans discharged from the extraction vessel; (d) introducing moist green coffee beans having a moisture content of 25-50% into the upper end of said extraction vessel in an amount corresponding substantially to the amount of decaffeinated coffee beans discharged from the extraction vessel; (e) maintaining the temperature in the extraction vessel at from 80°-140° C.; (f) feeding the supercritical carbon dioxide containing caffeine and non-caffeine solids withdrawn from the upper end of the extraction vessel to an absorber; (g) continuously countercurrently contacting the supercritical carbon dioxide containing caffeine and non-caffeine solids with water in the absorber at a temperature and pressure substantially the same as in the extraction vessel to extract substantially all of the caffeine contained in the supercritical carbon dioxide but extracting no appreciable amount of said non-caffeine solids therefrom; (h) withdrawing caffeine-laden water from the absorber; (i) withdrawing substantially caffeine-free supercritical carbon dioxide containing non-caffeine solids from said absorber; (j) recycling the substantially caffeine-free supercritical carbon dioxide containing non-caffeine solids to the lower end of the extraction vessel as required by step (a); and (k) periodically repeating steps (b), (c) and (d) while carrying out steps (a) and (e) through (j) to effect extraction of caffeine from said green coffee beans.
Claim 3
Dependent Claim 54 words
A method according to claim 1 wherein, in step (a) the caffeine concentration in the supercritical carbon dioxide withdrawn from the upper end of the extraction vessel is at least 50% of the maximum obtainable caffeine concentration, said maximum obtainable caffeine concentration being defined by the caffeine partition coefficient for said supercritical carbon dioxide.
Claim 4
Dependent Claim 17 words
A method according to claim 2 wherein said caffeine concentration is at least 70% of said maximum.
Claim 5
Dependent Claim 38 words
A method according to claim 1 wherein the amount of coffee beans discharged from and introduced into said extraction vessel is between about 5 and 33% of the volume of the coffee beans contained in the extraction vessel.
Claim 6
Dependent Claim 34 words
A method according to claim 4 wherein the discharging of coffee beans from and the introducing of coffee beans into said extraction vessel are carried out between about every 10 minutes and 120 minutes.
Claim 7
Dependent Claim 27 words
A method according to claim 1 wherein the weight ratio of supercritical carbon dioxide to coffee beans is between 30 and 100 kg supercritical carbon dioxide/kg coffee.
Claim 8
Dependent Claim 29 words
A method according to claim 1 wherein the discharging of coffee beans from and the introducing of coffee beans into said extraction vessel are carried out via blow cases.
Claim 9
Dependent Claim 28 words
A method according to claim 1 further comprising combining an enhancer with said caffeine-free supercritical carbon dioxide prior to feeding the supercritical carbon dioxide to said extraction vessel.
Claim 10
Dependent Claim 34 words
A method according to claim 1 wherein, in step (g), at least 90% of the caffeine and less that 5% of the non-caffeine solids are transferred from the supercritical carbon dioxide to the water.
Claim 11
Dependent Claim 18 words
A method according to claim 1 further comprising recovering caffeine from the caffeine-laden water withdrawn from said absorber.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-04-10 1992-10-10 1993-04-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-04-10 1996-10-10 1997-04-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-04-10 2000-10-10 2001-04-11 $7700.00 Window Closed / Lapsed

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