US4251923A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for drying water-containing substances
Assignee: Kuri Chemical Engineers Inc
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Filing: 1979-08-10
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Granted: 1981-02-24
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Expires: 1999-08-10
Abstract
Abstract A liquid food, a medicine or a natural food to be dried is subjected to vacuum evaporation and drying with a dry gas simultaneously or alternately, and by this drying method, the substance is effectively dried without freezing of the substance. A gas containing volatile components, which is discharged from the drying step, is introduced into an absorption layer and is regenerated to a drying gas while the volatile components of the substance, such as aroma, are recovered in the form of a liquid. In this drying method, the drying process is carried out entirely in a closed circuit system.
Inventors
- 👤 Setuya Kuri
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 16:49
CPC Classifications
F; F26; F26B; F26B5/00; F26B5/04; A; A23; A23B; A23B2/00; A23B2/90; A23F; A23F5/00; A23F5/24; A23F5/28; A23F5/285
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
318 words
A drying method comprising the steps of (A) exposing a substance to be dried to a reduced pressure of 1 to 600 mmHg (absolute pressure) to evaporate in vacuum the volatile components contained in said substance without freezing of said substance, (B) contacting said substance uniformly with a drying gas having a dew point of -75° to 0° C. to evaporate the volatile components and elevate the temperature of said substance, said steps (A) and (B) being conducted simultaneously or alternately, whereby, said substance is formed into a dry product without freezing of said substance, and introducing a gas containing said volatile components discharged from said step (A) and/or said step (B) into one of a pair of beds packed with an adsorbent capable of selectively adsorbing the volatile components to regenerate said gas free from volatile components to dryness of a dew point of -75° to 0° C. and recycling the regenerated drying gas to said step (B), changing over introduction of said volatile component-containing gas from said one adsorption bed to the other adsorption bed before the amount of the volatile components adsorbed in said one adsorption bed reaches a saturation level, reducing the pressure in said one adsorption bed below the level of the pressure of said volatile component-containing gas, feeding a part of the drying gas discharged from the other adsorption bed or a drying gas from the outside of the system into said one adsorption bed in an amount smaller than the amount of said volatile component-containing gas to thereby desorb the volatile components adsorbed in said one adsorption bed, performing said adsorption and desorption operations repeatedly on said paired adsorption beds alternately, and mixing the desorption gas, obtained by said desorption operation, with the volatile component-containing gas, if desired, after separation of condensed volatile components in said desorption gas, and recycling the gaseous mixture into one of said pair of adsorption beds.
Claim 2
Dependent Claim
318 words
A drying method comprising the steps of (A) exposing a substance to be dried to a reduced pressure of 1 to 600 mmHg (absolute pressure) to evaporate in vacuum the volatile components contained in said substance without freezing of said substance, (B) contacting said substance uniformly with a drying gas having a dew point of -75° to 0° C. to evaporate the volatile components and elevate the temperature of said substance, said steps (A) and (B) being conducted simultaneously or alternately, whereby, said substance is formed into a dry product without freezing of said substance, and introducing a gas containing said volatile components discharged from said step (A) and/or said step (B) into one of a pair of beds packed with an adsorbent capable of selectively adsorbing the volatile components to regenerate said gas free from volatile components to dryness of a dew point of -75° to 0° C. and recycling the regenerated drying gas to said step (B), changing over introduction of said volatile component-containing gas from said one adsorption bed to the other adsorption bed before the amount of the volatile components adsorbed in said one adsorption bed reaches a saturation level, reducing the pressure in said one adsorption bed below the level of the pressure of said volatile component-containing gas, feeding a part of the drying gas discharged from the other adsorption bed or a drying gas from the outside of the system into said one adsorption bed in an amount smaller than the amount of said volatile component-containing gas to thereby desorb the volatile components adsorbed in said one adsorption bed, performing said adsorption and desorption operations repeatedly on said paired adsorption beds alternately, and mixing the desorption gas, obtained by said desorption operation, with the volatile component-containing gas, if desired, after separation of condensed volatile components in said desorption gas, and recycling the gaseous mixture into one of said pair of adsorption beds.
Claim 3
Dependent Claim
18 words
A drying method according to claim 1 wherein the substance to be dried is a solution or dispersion.
Claim 4
Dependent Claim
15 words
The drying method according to claim 1, wherein steps (A) and (B) are conducted consecutively.
Claim 5
Dependent Claim
42 words
The drying method according to claim 3, wherein step (B) is continued until the temperature of said substance is elevated to a temperature which is at least 20° C. higher than the freezing-initiating point of the substance but lower than 50° C.
Claim 6
Dependent Claim
15 words
The drying method according to claim 1, wherein steps (A) and (B) are conducted simultaneously.
Claim 7
Dependent Claim
21 words
The drying method according to claim 1, wherein the drying gas has a dew point of -73° C. to -50° C.
Claim 8
Dependent Claim
22 words
The drying method according to claim 1, wherein the drying gas has a temperature in the range of 10° to 50° C.
Claim 9
Dependent Claim
25 words
The drying method according to claim 1, wherein the reduced pressure of step (A) is in the range of 1 to 160 mmHg (absolute pressure).
Claim 10
Dependent Claim
16 words
The drying method according to claim 1, wherein the substance to be dried is a food.
Claim 11
Dependent Claim
16 words
The drying method according to claim 1, wherein the substance to be dried is a medicine.
References Cited (Backward Citations)
US1866346A
Cited
US4063367A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-02-24 | 1984-08-25 | 1985-02-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-02-24 | 1988-08-25 | 1989-02-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-02-24 | 1992-08-25 | 1993-02-24 | $7700.00 | Window Closed / Lapsed |