Process for the production of light colored food grade protein and dietary fibre from grainby-products

• US 4,919,952 A
• Filed: 02/08/1989
• Issued: 04/24/1990
• Est. Priority Date: 11/03/1986
• Status: Expired due to Fees

• Current Assignee: Robin Hood Multifoods, Inc. (The J. M. Smucker Company)
• Original Assignee: Robin Hood Multifoods, Inc. (The J. M. Smucker Company)
• Inventors: Zellen, Wendy, Sadaranganey, Gobind T., Michaelides, John
• Primary Examiner(s): Nucker, Christine M.
• Assistant Examiner(s): McMahon, Timothy M.
• Application Number:
  US07/309,903
• Time in Patent Office: 440 Days
• Field of Search: 426/253, 426/258, 426/615, 426/629, 426/656, 426/481, 426/254, 426/640, 426/436, 426/450, 426/452, 530/372, 530/375, 530/414
• US Class Current: 426/254
• CPC Class Codes: A23J 1/12 from cereals, wheat, bran, or molasses
• CPC Class Codes: A23L 33/21 Addition of substantially indigestible substances, e.g. dietary fibres

Abstract

Food grade protein and dietary fibre concentrates are prepared from wheat millfeed. The process utilizes an efficient alkali extraction to obtain in excess of 75% w/w of the protein present in the millfeed in a solution which is further treated to separate the suspended starch and fat. The clarified liquid containing the protein is passed over a semipermeable membrane during which it is further purified and concentrated. Hydrogen peroxide and heat are introduced to the liquid thereby reducing its color prior to spray drying. The resulting residue from the extraction is dried or further treated with hydrogen peroxide and heat to produce a light colored dietary fibre concentrate.

Claims

1. An integrated process for preparing food grade bleached purified stable protein and dietary fibre concentrates from wheat millfeed comprising the steps of:

(a) mixing wheat millfeed of particle size less than 1680 μ

m with an alkali solution to produce a slurry with solvent/millfeed ratio in the range of 7;

1 to 10;

1 v/w and having pH in the range of pH 9-11;

(b) separating the slurry to remove the alkali liquid to isolate alkali extract and form a millfeed residue;

(c) removing starch and fat from the alkali extract;

(d) ultrafiltration of the alkali extract to form a retantate using a semi-permeable membrane;

(e) bleaching the retantate by adding hydrogen peroxide and heating;

(f) cooling and drying the bleached retantate to provide a protein concentrate;

(g) adding water and 35-70% w/v hydrogen peroxide to said millfeed residue to produce a slurry;

(h) heating said slurry containing millfeed residue to a temperature of 50°

-100°

C.; and

(i) decanting liquid from the slurry and drying the residue to produce a dietary fibre concentrate.

2. The process of claim 1 wherein said retantate is bleached at temperatures of 50°

-60°

C. and held for 120-180 minutes.

3. The process of claim 1 wherein said alkali slurry of solvent and millfeed is agitated for 45-90 minutes at a temperature of 20°

-25°

C. and wherein said retantate is bleached by adding 1 to 4% w/v hydrogen peroxide at temperatures of 50°

-60°

C. and held for 120-180 minutes.

4. The process of claim 1 wherein said hydrogen peroxide added to said millfeed residue is 35-50% w/v in concentration and said slurry produced contains 10-15% w/v residue solids and 1-14% w/v hydrogen peroxide.

5. The process of claim 1 wherein said semi-permeable membrane has a nominal molecular weight cut-off range of 5,000-25,000, the pressure of alkali extract entering said semi-permeable membrane is between 40-60 psi., and said ultrafiltration is continued until the protein matter content of the retantate is at least 70% w/w of the total dry matter of the retantate.

6. The process of claim 1 wherein said alkali solution is comprised of sodium hydroxide and water, with the sodium hydroxide added to the water prior to the introduction of said wheat grain millfeed.

7. The process of claim 1 wherein the food grade bleached purified stable protein concentrate contains approximately 70% protein and the food grade bleached purified dietary fibre contains in excess of 85% dietary fibre.

8. A process for preparing food grade bleached dietary fibre concentrate from wheat millfeed comprising the steps of:

(a) mixing wheat grain millfeed of particle size less than 1680 μ

m with a sodium hydroxide solution to produce a slurry with solvent/millfeed ratio in the range of 7;

1 to 10;

1 v/w having pH in the range of pH 9-11;

(b) separating the alkali liquid from the slurry to isolate alkali extract and form a millfeed residue;

(c) adding water and 35-70% w/v hydrogen peroxide 1-14% to said millfeed residue to produce a slurry;

(d) heating said slurry to a temperature of 80°

-100°

C.;

(e) decanting the liquid and drying the residue to produce a dietary fibre concentrate.

9. The process of claim 8 wherein said hydrogen peroxide and millfeed residue slurry produced contains 10-15% w/v residue solids and is heated at said temperature for 30 to 60 minutes.

10. The process of claim 8 wherein the food grade bleached dietary fibre concentrate contains in excess of 85% dietary fibre.