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US5087468A
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Process for aromatization of treated tea
Assignee: Hopfenextraktion Hvg Barth Raiser and Co
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Filing: 1989-11-15
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Granted: 1992-02-11
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Expires: 2009-11-15
Abstract
Abstract Moistened black tea is decaffeinated using carbon dioxide as a solvent. The mixture consisting of caffeine, water, aroma constituents and gaseous carbon dioxide obtained in the course of the purification of the carbon dioxide (prior to recirculation of the latter) is removed from the separation tank and separated by raising the temperature at atmospheric pressure into an aqueous caffeine solution and a gaseous aroma fraction. The emanating carbon dioxide transports the aroma components, after a dew point depression by lowering the temperature, to decaffeinated, dried tea, to which the aroma constituents are impregnated.
Inventors
- 👤 Josef Schulmeyr
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 23:20
CPC Classifications
A; A23; A23F; A23F3/00; A23F3/36; A23F3/366; A23F3/40; A23F3/42; A23F3/423; A23F3/426
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
232 words
A process of the production of an aromatic decaffeinated tea comprising the steps of: a) charging moist tea to a pressure vessel, b) charging liquid supercritical carbon dioxide to said pressure vessel at a temperature of between 0° to 100° C. and at a pressure of 100 to 500 bars to dissolve therein the caffeine and aroma fractions of said tea to provide a carbon dioxide solution, c) separating said carbon dioxide solution from said tea, d) charging said carbon dioxide solution to a first expansion vessel, reducing the pressure therein to 100 bars, raising the temperature to between 50° and 100° C. and continuously adding there 1 part by weight of water for each 10 parts by weight of originally charged moistened tea per hour, e) recovering the carbon dioxide thus converted to the gaseous state and recycling same into step (b) and collecting the thus produced aqueous extract containing aroma, caffeine, and some carbon dioxide, f) charging said aqueous extract to a second expansion vessel, lowering the pressure to 1 bar and reheating the contents to between 50° and 100° C. whereby the aromatics, some water and the carbon dioxide are volatilized, g) collecting the volatiles from step (f) and cooling same to between 0° and 40° C. whereby a portion of the water is condensed, h) charging the remaining volatiles to dearomatized decaffeinated tea to obtain aromatized decaffeinated tea.
Claim 2
Dependent Claim
232 words
A process of the production of an aromatic decaffeinated tea comprising the steps of: a) charging moist tea to a pressure vessel, b) charging liquid supercritical carbon dioxide to said pressure vessel at a temperature of between 0° to 100° C. and at a pressure of 100 to 500 bars to dissolve therein the caffeine and aroma fractions of said tea to provide a carbon dioxide solution, c) separating said carbon dioxide solution from said tea, d) charging said carbon dioxide solution to a first expansion vessel, reducing the pressure therein to 100 bars, raising the temperature to between 50° and 100° C. and continuously adding there 1 part by weight of water for each 10 parts by weight of originally charged moistened tea per hour, e) recovering the carbon dioxide thus converted to the gaseous state and recycling same into step (b) and collecting the thus produced aqueous extract containing aroma, caffeine, and some carbon dioxide, f) charging said aqueous extract to a second expansion vessel, lowering the pressure to 1 bar and reheating the contents to between 50° and 100° C. whereby the aromatics, some water and the carbon dioxide are volatilized, g) collecting the volatiles from step (f) and cooling same to between 0° and 40° C. whereby a portion of the water is condensed, h) charging the remaining volatiles to dearomatized decaffeinated tea to obtain aromatized decaffeinated tea.
Claim 3
Dependent Claim
21 words
A process of claim 1, wherein the dearomatized decaffeinated tea is dried after separation from the carbon dioxide in step (c).
Claim 4
Dependent Claim
26 words
A process of claim 1, wherein the volatiles of step (h) are charged to dearomatized decaffeinated tea during or after a step of drying said tea.
Claim 5
Dependent Claim
16 words
A process of claim 1, additionally comprising drying the decaffeinated rearomatized tea obtained in step (h).
Claim 6
Dependent Claim
19 words
A process of claim 1, wherein the temperature in step (d) is raised to between 70° and 90° C.
Claim 7
Dependent Claim
21 words
A process of claim 1, which additionally comprises the steps of collecting the aqueous residue of step (f) and filtering same.
Claim 8
Dependent Claim
17 words
A process according to claim 6 which comprises cooling said filtered solution to precipitate the caffeine therefrom.
Claim 9
Dependent Claim
24 words
A process according to claim 1, wherein the cooling of step (g) is carried out in the range of from 10° to 30° C.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1995-02-10 | 1995-08-12 | 1996-02-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-02-10 | 1999-08-12 | 2000-02-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-02-10 | 2003-08-12 | 2004-02-11 | $7700.00 | Window Closed / Lapsed |