Method for fractionating soluble fractions of peas, fraction thus obtained and upgrade thereof

Patent metadata

Field	Value
Publication number	US-11377472-B2
Application number	US-201414764748-A
Country	US
Kind code	B2
Filing date	Jan 31, 2014
Priority date	Jan 31, 2013
Publication date	Jul 5, 2022
Grant date	Jul 5, 2022

Abstract

A method for fractionating soluble fractions of peas, includes, in sequence, a step of microfiltering or centrifuging, followed by a step of ultrafiltering, and optionally a reverse-osmosis step. A reduction of the leakage of proteins toward the soluble fractions, an improvement of the yield of the single concentration step by evaporating the soluble fractions, and the selective isolation of proteins of interest are thus achieved. The method is easy to implement, the devices used at each single step are conventional and well known to the person skilled in the art. Also, the method does not use any organic solvent other than water.

First claim

The invention claimed is:

1. A method for treating pea soluble fractions, comprising:
a) a soluble fractions preparation step comprising
(i) preparing a starch milk, by mixing pea flour and water in a kneading machine,
(ii) extracting the starch and the fibers from said milk to obtain a protein-rich product,
(iii) flocculating said protein-rich product,
(iv)isolating through centrifugal decantation carried out on the product obtained from step iii) a highly protein-rich composition called a floc and a supernatant called soluble fractions,

b) microfiltering or centrifuging said soluble fractions to obtain a microfiltration permeate and a microfiltration retentate or a centrifugation supernatant,
c) ultrafiltering one of said microfiltration permeate and centrifugation supernatant to obtain an albumin-rich ultrafiltration permeate and an ultrafiltration retentate rich in PA1b fraction,
d) subjecting said ultrafiltration permeate to reverse osmosis to obtain one of a reverse osmosis permeate enriched in PA1b fraction and a reverse osmosis retentate, and
e) reintroducing all or part of said microfiltration permeate, microfiltration retentate, ultrafiltration retentate, and reverse osmosis retentate to the floc, downstream of the centrifugal decanting step.

2. The method as claimed in claim 1 , wherein said soluble fraction is microfiltered by tangential membrane microfiltration.

3. The method as claimed in claim 2 , wherein the tangential membrane microfiltration is carried out with ceramic membranes having a porosity of 0.01 μm to 1 μm.

4. The method as claimed in claim 1 , wherein said microfiltering or centrifuging step b) is preceded by flocculation of insoluble particles contained in the pea soluble fraction.

5. The method as claimed in claim 1 , wherein said soluble fraction is ultrafiltered using membranes which have a cut-off threshold of between 0.1 and 0.5 μm, at a transmembrane pressure maintained below 4 bar.

6. The method as claimed in claim 1 , wherein the reverse osmosis is carried out with membranes having a cut-off threshold of between 100 Da and 500 Da.

7. The method as claimed in claim 2 , wherein the tangential membrane microfiltration is carried out with ceramic membranes having a porosity of 0.05 μm to 0.5 μm.

8. The method as claimed in claim 2 , wherein flocculation of insoluble particles contained in the pea soluble fraction is performed prior to microfiltering.

9. The method as claimed in claim 3 , wherein flocculation of insoluble particles contained in the pea soluble fraction is performed prior to microfiltering.

10. The method as claimed in claim 2 , wherein the ultrafiltering is carried out using membranes which have a cut-off threshold of between 0.1 and 0.5 μm, and a transmembrane pressure maintained below 4 bar.

11. The method as claimed in claim 3 , wherein ultrafiltering is carried out using membranes which have a cut-off threshold of between 0.1 and 0.5 μm, the transmembrane pressure being maintained below 4 bar.

12. The method as claimed in claim 4 , wherein ultrafiltering is carried out using membranes which have a cut-off threshold of between 0.1 and 0.5 μm, the transmembrane pressure being maintained below 4 bar.

Assignees

• Roquette Freres

Inventors

• Barata Manuel
• Duflot Pierrick
• Dhalleine Claire
• Verrin Jean-Marc

Classifications

• B01D2311/04

  Specific process operations in the feed stream; Feed pretreatment · CPC title

• B01D61/16

  Feed pretreatment · CPC title

• B01D61/025

  Reverse osmosis; Hyperfiltration · CPC title

• A23J3/14 Primary

  Vegetable proteins · CPC title

• B01D61/145

  Ultrafiltration · CPC title