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US4551341A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for obtaining clear plant juices and for the recovery of valorizable constituents

Assignee: Individual
•
Filing: 1981-08-10
•
Granted: 1985-11-05
•
Expires: 2001-08-10
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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 07:30
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.

References Cited (Backward Citations)

GB190143A Cited
GB1324031A Cited
US3799806A Cited
FR2202655A1 Cited
US4083779A Cited
US4115147A Cited
FR2443216A1 Cited

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

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