Process for decaffeinizing raw coffee

Claim 2

A process of decaffeinizing raw coffee, which comprises: extracting the caffeine from the raw coffee by circulating humid nitrogen oxide N 2 O gas in a hypercritical condition through the raw coffee, removing the caffeine laden, humid hypercritical nitrogen oxide N 2 O gas from the raw coffee, and immediately separating the caffeine from the humid hypercritical nitrogen oxide N 2 O gas by passing the hypercritical nitrogen oxide N 2 O gas through an ion exchanger containing functional groups capable of establishing a chemical bond between the ion exchanger and the caffeine thereby allowing the gas to pass away from the ion exchanger while leaving the caffeine with the ion exchanger.

Claim 3

A process of decaffeinizing raw coffee, which comprises: establishing significant fluid pressure on a quantity of raw coffee, and simultaneously establishing a similar pressure on an ion exchanger, introducing humid nitrogen oxide N 2 O gas in a hypercritical condition into said pressure conditions and circulating the humid, hypercritical nitrogen oxide N 2 O gas through the raw coffee to thereby absorb the caffeine from the coffee into the circulating gas, removing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas from the raw coffee, and while maintaining said significant pressure on the gas, passing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas into and through an ion exchanger containing functional groups capable of creating a chemical bond between the ion exchanger and the caffeine thereby separating the caffeine from the circulating gas.

Claim 4

A process of decaffeinizing raw coffee, which comprises: establishing significant fluid pressure on a quantity of raw coffee, and simultaneously establishing a similar pressure on an ion exchanger, introducing humid nitrogen oxide N 2 O gas in a hypercritical condition into said pressure conditions and circulating the humid, hypercritical nitrogen oxide N 2 O gas through the raw coffee to thereby absorb the caffeine from the coffee into the circulating gas, removing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas from the raw coffee, and while maintaining said significant pressure on the gas, passing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas into and through an ion exchanger containing functional groups capable of creating a chemical bond between the ion exchanger and the caffeine thereby separating the caffeine from the circulating gas.

Claim 5

A process of decaffeinizing raw coffee, which comprises establishing a fluid pressure on the order of 5,512 p.s.i. upon a quantity of raw coffee and establishing a like pressure on an ion exchanger, introducing a humid nitrogen oxide N 2 O gas in a hypercritical condition into the pressure conditions established, and circulating the humid, hypercritical nitrogen oxide N 2 O gas through the raw coffee to extract caffeine from the coffee and carry the caffeine away from the coffee with the gas, removing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas from the raw coffee, and while maintaining said pressure on the gas, immediately passing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas removed from the coffee and into and through an ion exchanger containing functional groups capable of establishing a chemical bond between the ion exchanger and the caffeine thereby separating the caffeine from the hypercritical nitrogen oxide N 2 O gas, and recirculating the gas into and through the raw coffee again for extracting additional caffeine, and continuing the circulation of the gas through the coffee and through the ion exchanger and back through the raw coffee again continuously for a period on the order four and a half hours.

Claim 6

A process of decaffeinizing raw coffee, which comprises establishing a fluid pressure on the order of 5,512 p.s.i. upon a quantity of raw coffee and establishing a like pressure on an ion exchanger, introducing a humid nitrogen oxide N 2 O gas in a hypercritical condition into the pressure conditions established, and circulating the humid, hypercritical nitrogen oxide N 2 O gas through the raw coffee to extract caffeine from the coffee and carry the caffeine away from the coffee with the gas, removing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas from the raw coffee, and while maintaining said pressure on the gas, immediately passing the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas removed from the coffee and into and through an ion exchanger containing functional groups capable of establishing a chemical bond between the ion exchanger and the caffeine thereby separating the caffeine from the hypercritical nitrogen oxide N 2 O gas, and recirculating the gas into and through the raw coffee again for extracting additional caffeine, and continuing the circulation of the gas through the coffee and through the ion exchanger and back through the raw coffee again continuously for a period on the order four and a half hours.

Claim 7

A process of decaffeinizing raw coffee, which comprises confining a quantity of raw coffee in a first high pressure vessel, and establishing a significant fluid pressure in said vessel; confining an aqueous solution of ion exchanger in a second high pressure vessel and substantially equalizing the pressure in the second vessel to the pressure in the first vessel, confining a quantity of water in a third high pressure vessel and establishing a fluid pressure therein like the fluid pressure in the first and second vessels; introducing hypercritical nitrogen oxide N 2 O gas into the third vessel and circulating the gas through the water to thereby render the gas humid; while maintaining said significant pressure on the humid, hypercritical nitrogen oxide N 2 O gas, introducing the gas into the first vessel and circulating the gas through the raw coffee to extract the caffeine from the raw coffee; removing the caffeine laden humid, hypercritical, nitrogen oxide N 2 O gas from the raw coffee, and while maintaining said significant pressure on the gas, introducing the gas into the second vessel and circulating the caffeine laden gas through the aqueous solution of an ion exchanger containing functional groups capable of producing a chemical bond between the ion exchanger and the caffeine thereby removing the caffeine from the gas passing through the aqueous solution; and while maintaining said significant pressure on the hypercritical nitrogen oxide N 2 O gas, introducing and circulating the gas into and through the third vessel and through the water therein in a continuing cycle; and continuing the recycling of the gas through the several vessels over a time period of several hours.

Claim 8

A process of decaffeinizing raw coffee, which comprises confining a quantity of raw coffee in a first high pressure vessel, and establishing a significant fluid pressure in said vessel; confining an aqueous solution of ion exchanger in a second high pressure vessel and substantially equalizing the pressure in the second vessel to the pressure in the first vessel, confining a quantity of water in a third high pressure vessel and establishing a fluid pressure therein like the fluid pressure in the first and second vessels; introducing hypercritical nitrogen oxide N 2 O gas into the third vessel and circulating the gas through the water to thereby render the gas humid; while maintaining said significant pressure on the humid, hypercritical nitrogen oxide N 2 O gas, introducing the gas into the first vessel and circulating the gas through the raw coffee to extract the caffeine from the raw coffee; removing the caffeine laden humid, hypercritical, nitrogen oxide N 2 O gas from the raw coffee, and while maintaining said significant pressure on the gas, introducing the gas into the second vessel and circulating the caffeine laden gas through the aqueous solution of an ion exchanger containing functional groups capable of producing a chemical bond between the ion exchanger and the caffeine thereby removing the caffeine from the gas passing through the aqueous solution; and while maintaining said significant pressure on the hypercritical nitrogen oxide N 2 O gas, introducing and circulating the gas into and through the third vessel and through the water therein in a continuing cycle; and continuing the recycling of the gas through the several vessels over a time period of several hours.

Claim 9

The invention according to claim 4 wherein the fluid pressure established in said vessels is approximately 5,512 p.s.i., and the temperature is maintained at approximately 75° C.; and the time period extends for approximately four and one half hours.

Claim 10

A process of decaffeinizing raw coffee, which comprises: confining quantities of humid, raw coffee and a dry ion exchanger which contains caffeine bonding functional groups in a single high pressure vessel wherein the humid, raw coffee is located at the lower portion of the vessel, and the dry ion exchanger is supported in an upper portion of the vessel; establishing a significant fluid pressure in said vessel and continuing the fluid pressure; introducing hypercritical nitrogen oxide N 2 O gas into the lower portion of the vessel and passing the gas through the raw coffee to render the gas humid and to cause the gas to extract caffeine from the raw coffee; circulating the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas upwardly through the ion exchanger which produces a chemical bond with the caffeine in the gas and separates the caffeine from the gas which is circulated through and out of the ion exchanger; and recirculating the hypercritical nitrogen oxide gas into the lower portion of the vessel for passing through the raw coffee again.

Claim 11

A process of decaffeinizing raw coffee, which comprises: confining quantities of humid, raw coffee and a dry ion exchanger which contains caffeine bonding functional groups in a single high pressure vessel wherein the humid, raw coffee is located at the lower portion of the vessel, and the dry ion exchanger is supported in an upper portion of the vessel; establishing a significant fluid pressure in said vessel and continuing the fluid pressure; introducing hypercritical nitrogen oxide N 2 O gas into the lower portion of the vessel and passing the gas through the raw coffee to render the gas humid and to cause the gas to extract caffeine from the raw coffee; circulating the caffeine laden, humid, hypercritical nitrogen oxide N 2 O gas upwardly through the ion exchanger which produces a chemical bond with the caffeine in the gas and separates the caffeine from the gas which is circulated through and out of the ion exchanger; and recirculating the hypercritical nitrogen oxide gas into the lower portion of the vessel for passing through the raw coffee again.

Claim 12

A process as defined in claim 1 wherein for recovering the caffeine the caffeine-loaded ion exchanger is suspended in water and the caffeine attached to said ion exchanger is separated by altering the pH.

Claim 13

A process as defined in claim 7 wherein the pH is adjusted to about 4 by means of organic halogen-free acid.

Claim 14

A process as defined in claim 8 wherein as an organic halogen-free acid is employed an aliphatic acid selected acetic acid or formic acid.

Claim 15

A process as defined in claim 1 wherein the ion exchanger employed is a three-dimensional cross-linked polysaccharide.

Claim 16

A process as defined in claim 10 wherein the ion exchanger employed is SEPHADEX, and wherein the polysaccharide is obtained by cross-linking linear macramolecules of dextrane.