IP Library Granted Patent US 7,608,729
Granted Patent B2
US 7,608,729 · App. 11/688,425 · Granted Oct 27, 2009

Method of freeing the bound oil present in whole stillage and thin stillage

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Quick Facts
Patent No.
US 7,608,729
App. No.
11/688,425
Granted
Oct 27, 2009
Kind
B2
Abstract

A method is provided for recovering oil from stillage including oil resulting from a process used for producing ethanol. In one embodiment, the method includes heating the stillage to a temperature sufficient to at least partially separate, or unbind, the oil therefrom The method further includes recovering the oil from the stillage.

Claims (20)

1. A method of recovering oil from stillage, including oil, resulting from a process used for producing ethanol, comprising:

recovering whole stillage from the process used for producing the ethanol;

mechanically processing the whole stillage to provide distillers wet grains and thin stillage;

evaporating the thin stillage to form a thin stillage concentrate;

heating the thin stillage concentrate to a temperature greater than 212° F. and a pressure sufficient to prevent boiling; and

recovering the oil from the thin stillage concentrate.

2. The method of claim 1 , wherein the temperature is at about 230° F. to less than about 250° F.

3. The method of claim 1 , wherein the heating the thin stillage concentrate includes maintaining a pressure on the thin stillage concentrate of at least a vapor pressure effective to unbind at least part of the oil without boiling the thin stillage concentrate.

4. The method of claim 1 , further comprising lowering the pressure after the heating but before the recovering the oil.

5. The method of claim 1 , wherein the recovering the oil comprises separating the oil from the thin stillage concentrate using a gravity separation process.

6. The method of claim 1 , further comprising cooling the thin stillage concentrate after heating and before recovering the oil.

7. A method of recovering oil from concentrated stillage including oil resulting from a process used for producing ethanol, comprising:

pressure cooking the concentrated stillage at a temperature greater than 212° F. without boiling to unbind the oil from the stillage; and recovering the unbound oil.

8. A method of recovering oil from thin stillage including oil resulting from a process used for producing ethanol, comprising:

evaporating the thin stillage to form a thin stillage concentrate;

hydrolyzing solids in the thin stillage concentrate so as to reduce a viscosity of the concentrate; and

recovering the oil from the thin stillage concentrate.

9. The method of claim 8 , wherein hydrolyzing solids in the thin stillage concentrate comprises heating the stillage to a temperature greater than 212° F. at a pressure greater than atmospheric pressure without boiling.

10. The method of claim 8 , further comprising cooling the thin stillage concentrate before recovering the oil.

11. The process of claim 1 , wherein the recovering the oil comprises centrifuging the oil from the thin stillage concentrate.

Assignments (5)
SECURITY AGREEMENT Recorded Jan 8, 2013
From: ECOSYSTEM TECHNOLOGIES, LLC; GREENSHIFT CORPORATION (F/K/A GS CLEANTECH CORPORATION); GS AGRIFUELS CORPORATION; GS BIG MANAGEMENT, LLC; GS CLEANTECH CORPORATION (F/K/A GS ETHANOL TECHNOLOGIES, INC.); GS COES (YORKVILLE I), LLC; GS COES (ADRIAN I), LLC; GS DESIGN, INC. (F/K/A WARNECKE DESIGN SERVICE, INC.); GS GLOBAL BIODIESEL, LLC; GS RENTALS, LLC (F/K/A WARNECKE RENTALS, LLC); GS TECHNOLOGY, LLC; GREENSHIFT ENGINEERING, INC. (F/K/A GS CARBON DIOXIDE TECHNOLOGIES, INC.); NEXTGEN ACQUISITION, INC.; NEXTGEN FUEL, INC.; SUSTAINABLE SYSTEMS, INC.; SUSTAINABLE SYSTEMS, LLC; VIRIDIS CAPITAL LLC
To: YA GLOBAL INVESTMENTS, L.P., AS COLLATERAL AGENT
Reel/Frame 029588/0092 →
SECURITY AGREEMENT Recorded Nov 16, 2009
From: VIRIDIUS CAPITAL LLC; CARBONICS CAPITAL CORPORATION; GREENSHIFT CORPORATION (F/K/A GS CLEANTECH CORPORATION); GS CLEANTECH CORPORATION (F/K/A GS ETHANOL TECHNOLOGIES, INC.); GS COES (YORKVILLE I), LLC; GS DESIGN, INC. (F/K/A WARNECKE DESIGN SERVICE, INC.); GS RENTAL, LLC (F/K/A WARNECKE RENTALS, LLC); GS CARBON DIOXIDE TECHNOLOGIES, INC.; GS AGRIFUELS CORPORATION; NEXTGEN ACQUISITION, INC.; NEXTGEN FUEL INC.; SUSTAINABLE SYSTEMS, INC.; SUSTAINABLE SYSTEMS LLC; GS GLOBAL BIODIESEL, LLC; BOLLHEIMER & ASSOCIATES, INC.; GS BIG MANAGEMENT, LLC; GS COES (ADRIAN I), LLC; GS TECHNOLOGY, LLC; ECOSYSTEM TECHNOLOGIES, LLC
To: YA GLOBAL INVESTMENTS, L.P.
Reel/Frame 023524/0728 →
SECURITY AGREEMENT Recorded Sep 1, 2009
From: VIRIDIS CAPITAL LLC; CARBONICS CAPITAL CORPORATION (F/K/A GREENSHIFT CORPORATION); GREENSHIFT CORPORATION (F/K/A GS CLEANTECH CORPORATION); GS CLEANTECH CORPORATION (F/K/A GS ETHANOL TECHNOLOGIES, INC.); GS COES (YORKVILLE I), LLC; GS CARBON DIOXIDE TECHNOLOGIES, INC.; GS GLOBAL BIODIESEL, LLC; GS AGRIFUELS CORPORATION; NEXTGEN ACQUISITION, INC.; NEXTGEN FUEL INC.; SUSTAINABLE SYSTEMS, INC.; SUSTAINABLE SYSTEMS LLC; GS DESIGN, INC. (F/K/A WARNECKE DESIGN SERVICE, INC.); GS RENTALS LLC (F/K/A WARNECKE RENTALS, LLC); BOLLHEIMER & ASSOCIATES, INC.; ECOSYSTEM TECHNOLOGIES, LLC; GS BIG MANAGEMENT, LLC; GS COES (ADRIAN I), LLC; GS TECHNOLOGY, LLC
To: YA GLOBAL INVESTMENTS, L.P.
Reel/Frame 023163/0954 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 15, 2009
From: GS INDUSTRIAL DESIGN, INC.
To: GS CLEANTECH CORPORATION
Reel/Frame 022691/0692 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 19, 2007
From: WINSNESS, DAVID J.; DAVIS, JOHN W.; BARLAGE, GREGORY PAUL; CANTRELL, DAVID FRED
To: GS INDUSTRIAL DESIGN, INC.
Reel/Frame 019451/0240 →