IP Library Granted Patent US 8,735,544
Granted Patent B1
US 8,735,544 · App. 11/162,944 · Granted May 27, 2014

Value added whole stillage by-products from an ethanol production process

Inventors: John E. Prevost (Slaughter, LA); Neal A. Hammond (Cameron Park, CA)
Assignee: Little Sioux Corn Processors, LLC
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Quick Facts
Patent No.
US 8,735,544
App. No.
11/162,944
Granted
May 27, 2014
Kind
B1
Abstract

An improved process for obtaining value added by-products from an ethanol production whole stillage is disclosed wherein the whole stillage is mixed with additives to form a nutrition enriched product stream that is subsequently dried to produce a nutrition enriched product having a water content of less than 12% by weight. In a preferred embodiment the whole stillage is obtained from a ethanol production process that has utilized a corn flour as the starting feedstock. The corn flour is then hydrolyzed along with added vitamins and/or nutrients and/or enzymes. The hydrolyzed product is then preferably mixed with a soy hull flour, also preferably having a median particle size of less than about 100 microns, and subjected to conventional fermentation conditions to produce an ethanol containing product. The ethanol-containing product is then distilled to produce an ethanol enriched steam and the separate whole stillage to be used as the feedstock.

Claims (18)

1. A process for producing a zein protein containing product comprising:

a) hydrolyzing and fermenting a carbohydrate containing feedstock to produce an ethanol containing product stream;

b) distilling the ethanol containing product stream to produce an ethanol containing product and a separated whole stillage;

c) filtering the separated whole stillage through an ultrafiltration membrane sized and configured to have a molecular weight cut-off between about 10,000 to about 50,000 molecular weight cut-off to form a zein protein containing retentate and a permeate stream; and

d) drying the zein protein containing retentate to form a zein protein containing product having a water content of less than about 12% by weight.

2. The process according to claim 1 further comprising, prior to filtering the whole stillage, mixing an additive selected from the group consisting of vitamins, minerals, amino acids, proteins, flavors, phytochemicals, pharmaceuticals, nutraceuticals, binders, fillers, and mixtures thereof with the whole stillage.

3. The process according to claim 1 , wherein step c) comprises:

i) filtering at least a portion of the separated whole stillage through a microfilter member having a pore size of 0.1 to 1.0 microns to form a retentate and a permeate stream; and

ii) filtering the permeate stream through the ultrafiltration membrane.

4. The process according to claim 1 further comprising, prior to filtering the separated whole stillage through the ultrafiltration membrane, mixing an additive selected from the group consisting of vitamins minerals, amino acids, proteins, flavors, phytochemicals, pharmaceuticals, nutraceuticals, binders, fillers, and mixtures thereof with the separated whole stillage.

5. A process for producing a zein protein containing product comprising:

a) hydrolyzing and fermenting a carbohydrate containing feedstock to produce an ethanol containing product stream;

b) distilling the ethanol containing product stream to produce an ethanol containing product and a whole stillage;

c) filtering at least part of the whole stillage through an ultrafiltration membrane sized and configured to have a molecular weight cut-off between about 10,000 to about 50,000 molecular weight cut-off to form a zein protein containing retentate and a permeate stream; and

d) drying the zein protein containing retentate to form a zein protein containing product having a water content of less than about 12% by weight.

6. The method of claim 5 , further comprising:

filtering the whole stillage through a second filter to form a second retentate, wherein the second filter is configured to allow zein protein to pass therethrough and filtering the whole stillage through the second filter occurs before the at least part of the whole stillage is filtered through the ultrafiltration membrane.

7. The method of claim 6 , wherein the second filter is a microfilter.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 7, 2009
From: UNIVERSITY TECHNOLOGIES, INC.
To: FARMERS FIRST GROUP, LLC
Reel/Frame 023066/0597 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 7, 2009
From: FARMERS FIRST GROUP, LLC; PREVOST, JOHN E, MR.; HAMMOND, NEAL A, MR
To: LITTLE SIOUX CORN PROCESSORS, LLC
Reel/Frame 023066/0813 →
Continuity (8)
Continuation In Part 10458480 · Jun 10, 2003
Continuation 10008834 · Nov 9, 2001
Continuation 09229286 · Jan 13, 1999
Continuation In Part 10710125 · Jun 21, 2004
Continuation In Part 10281490 · Oct 28, 2002
Continuation In Part 10395547 · Mar 24, 2003
Continuation In Part 11162944
Continuation In Part 10619822 · Jul 15, 2003