Patent US4551341A successfully refreshed from Google Patents.
US4551341A
Expired / Lapsed
US
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Method for obtaining clear plant juices and for the recovery of valorizable constituents
Assignee: Individual
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Filing: 1981-08-10
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Granted: 1985-11-05
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Expires: 2001-08-10
Abstract
Abstract Method for obtaining clear plant juices and for the recovery of valorizable constituents wherein the juice from the pressing is subjected to a plurality of ultrafiltration stages, of which at least one is effected on a membrane with a molecular cutoff point on the order of 15,000 to 25,000. The temperature of introduction of raw juices is adjusted to T° C.=-6 PH +80° C.±3° C. Clear juices and valorizable constituents are obtained by this process. Application to the production of fruit and vegetable juices with preservation of the pigmentation is also disclosed.
Inventors
- 👤 Paul Blanie
- 👤 Claude Vernier
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 16:40
CPC Classifications
A; A23; A23L; A23L2/00; A23L2/70; A23L2/72; A23L2/74; C; C08; C08B; C08B37/00; C08B37/0003
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
149 words
A process for the production of clear juices from plants and for the recovery of a pectic concentrate containing valorizable constituents comprising the steps of (a) adjusting the temperature of a raw juice, obtained by pressing, as a function of measured pH of the raw juice according to the formula T° C.=-6 pH+80° C.±about 3° C.; (b) subjecting the temperature-adjusted raw juice to ultrafiltration on a membrane to yield a primary clear juice and a primary retained pectic concentrate containing valorizable constituents; (c) subjecting said primary retained pectic concentrate to a second ultrafiltration on a membrane to yield a second clear juice and a second retained pectic concentrate containing said valorizable constituents; (d) conducting at least one of the ultrafiltrations on a membrane having a cutoff level of molecular weight on the order of 15,000 to 25,000; and (e) recovering said second retained pectic concentrate containing said valorizable constituents.
Claim 2
Dependent Claim
149 words
A process for the production of clear juices from plants and for the recovery of a pectic concentrate containing valorizable constituents comprising the steps of (a) adjusting the temperature of a raw juice, obtained by pressing, as a function of measured pH of the raw juice according to the formula T° C.=-6 pH+80° C.±about 3° C.; (b) subjecting the temperature-adjusted raw juice to ultrafiltration on a membrane to yield a primary clear juice and a primary retained pectic concentrate containing valorizable constituents; (c) subjecting said primary retained pectic concentrate to a second ultrafiltration on a membrane to yield a second clear juice and a second retained pectic concentrate containing said valorizable constituents; (d) conducting at least one of the ultrafiltrations on a membrane having a cutoff level of molecular weight on the order of 15,000 to 25,000; and (e) recovering said second retained pectic concentrate containing said valorizable constituents.
Claim 3
Dependent Claim
33 words
The process according to claim 1 wherein said raw juice contains pigments and the adjusted temperature of said raw juice is below a temperature which causes deterioration of said pigments in said juice.
Claim 4
Dependent Claim
23 words
The process according to claim 1 wherein at least a portion of the second clear juice is added to the primary clear juice.
Claim 5
Dependent Claim
18 words
The process according to claim 1 wherein the primary retained pectic concentrate is diluted before the second ultrafiltration.
Claim 6
Dependent Claim
18 words
The process according to claim 1 wherein the raw juice is subjected to a previous fermentation before ultrafiltration.
Claim 7
Dependent Claim
51 words
The process according to claim 1 wherein the process is carried out at least in one ultrafiltration under a pressure at the introduction and a pressure at the exit on the order respectively of 3 to 5 kilograms per cm 2 and of 1 to 2 kilograms per cm 2 .
Claim 8
Dependent Claim
160 words
A process for the production of clear juices from plants and for the recovery of a pectic concentrate containing valorizable constituents comprising the steps of (a) adjusting the temperature of a raw juice, obtained by pressing, as a function of measured pH of the raw juice according to the formula T° C.=-6 pH+80° C.±about 3° C.; (b) subjecting the temperature-adjusted raw juice to ultrafiltration on a membrane to yield a primary clear juice and a primary retained pectic concentrate containing valorizable constituents; (c) subjecting said primary retained pectic concentrate to a second ultrafiltration on a membrane to yield a second clear juice and a second retained pectic concentrate containing said valorizable constituents; (d) conducting at least one of the ultrafiltrations on a membrane having a cutoff level of molecular weight on the order of 15,000 to 25,000; (e) recovering said second retained pectic concentrate containing said valorizable constituents; and (f) conducting said second ultrafiltration in the absence of added water.
Claim 9
Dependent Claim
160 words
A process for the production of clear juices from plants and for the recovery of a pectic concentrate containing valorizable constituents comprising the steps of (a) adjusting the temperature of a raw juice, obtained by pressing, as a function of measured pH of the raw juice according to the formula T° C.=-6 pH+80° C.±about 3° C.; (b) subjecting the temperature-adjusted raw juice to ultrafiltration on a membrane to yield a primary clear juice and a primary retained pectic concentrate containing valorizable constituents; (c) subjecting said primary retained pectic concentrate to a second ultrafiltration on a membrane to yield a second clear juice and a second retained pectic concentrate containing said valorizable constituents; (d) conducting at least one of the ultrafiltrations on a membrane having a cutoff level of molecular weight on the order of 15,000 to 25,000; (e) recovering said second retained pectic concentrate containing said valorizable constituents; and (f) conducting said second ultrafiltration in the absence of added water.
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FR2202655A1
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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) | 1988-11-04 | 1989-05-06 | 1989-11-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-11-04 | 1993-05-06 | 1993-11-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-11-04 | 1997-05-06 | 1997-11-05 | $7700.00 | Window Closed / Lapsed |