Oilseed processing

• US 4,158,656 A
• Filed: 02/27/1978
• Issued: 06/19/1979
• Est. Priority Date: 02/27/1978
• Status: Expired due to Term

• Current Assignee: Her Majesty The Queen In Right of Canada As Represented By The Minister of National Defence
• Original Assignee: Canadian Patents and Development Limited
• Inventors: Jones, John D., Holme, John
• Primary Examiner(s): Danison, Walter C.
• Application Number:
  US05/881,490
• Time in Patent Office: 477 Days
• Field of Search: 260/123.5
• US Class Current: 530/377
• CPC Class Codes: A23J 1/142 by extracting with organic solvents
• CPC Class Codes: A23L 11/32 by extraction with solvents

Abstract

A process for producing a detoxified protein concentrate product from defatted oilseeds, particularly those of the thioglucoside and phenolic containing types such as rapeseed, mustard or Crambe, in which dehulled, defatted seeds are extracted with an aqueous alcohol solvent under substantially non-oxidizing conditions, so as to prevent oxidation of the contained phenolic compounds and inhibit enzymic degradation of the glucosinolates. The solid residue of the extraction is dried at a temperature below about 60° C.

Claims

1. A process for the production of a protein concentrate for a dehulled, defatted oleaginous thioglucoside and phenolic containing seed material, in which the protein has not been subjected to denaturing conditions, comprising the steps of:

(a) contacting said seed material with an aqueous-lower alkanol solvent solution to thereby selectively extract glucosinolates, phenolic compounds and pigments therefrom at a temperature below 60°

C. and under conditions so as to prevent oxidation of said phenolic compounds and inhibiting enzymic degradation of glucosinolates;

(b) separating the liquid extract phase from a solid residue; and

(c) drying the solid residue at a temperature below about 60°

C. to thereby recover said protein concentrate.

2. A process as claimed in claim 1, wherein step (a) is conducted in the presence of an antioxidant.

3. A process as claimed in claim 2 wherein said antioxidant is selected from the group comprising sulphur dioxide, an alkali metal metabisulphite and ascorbic acid.

4. A process as claimed in claim 3, wherein said sulphur dioxide is present in an amount in the range about 200-600 ppm based on said solution.

5. A process as claimed in claim 1, wherein the temperature of said seed material in said solvent extraction step is in the range 20°

-50°

C.

6. A process as claimed in claim 1, wherein said lower alkanol is selected from the group consisting of methanol, ethanol, propanol and isopropanol.

7. A process as claimed in claim 1, wherein said dehulled, defatted seed material is obtained by dehulling, drying below about 70°

C. to a moisture content in the range 1-3% and subjecting to solvent extraction to remove oil.

8. A process as claimed in claim 7 including the step of predrying seed material to a moisture content below 6% prior to dehulling.

9. A detoxified protein concentrate, prepared from a thioglucoside and phenolic-containing oilseed, containing about 65% to 70% protein, 0.1-0.3% fat and not more than 5.5% crude fibre, characterized by bland flavour. off-white colour, a nitrogen solubility index of at least 30%, a Nitrogen Free Extract in the range about 14.7 to 17.1 and a P.E.R. at least as high as that of casein.

10. A concentrate as claimed in claim 9 wherein said oilseed is rape seed.

11. A concentrate as claimed in claim 10 wherein the protein content of said rapeseed concentrate has the essential amino acid composition (in g/16 g N):

isoleucine 4.4, leucine 8.5, lysine 6.7, methionine and cystine 5.0, phenylalamine and tyrosine 8.2, threonine 5.7, trypthophane 1.2 and valine 5.9.