IP Library Granted Patent US 8,287,651
Granted Patent B2
US 8,287,651 · App. 12/560,843 · Granted Oct 16, 2012

Cellulose pretreatment process

Assignee: GreenField Ethanol Inc.
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Quick Facts
Patent No.
US 8,287,651
App. No.
12/560,843
Granted
Oct 16, 2012
Kind
B2
Abstract

A process for the production of ethanol from biomass is disclosed. The process relates to the pretreatment of corncob biomass and includes the steps of exposing corncob to steam in a reaction vessel at an elevated temperature and reaction pressure for a preselected exposure time. Volatile compounds are continuously vented during pretreatment. The reaction pressure is released for explosive decomposition of the corncob biomass into fibrous solids and condensate. The exposure is preferably carried out at a temperature of 190-210° C. and a pressure of 190 psig to 275 psig and an exposure time of 3 to 10 minutes.

Claims (10)

1. A process for the pretreatment of corncob biomass for biofuel production by fermentation, comprising the steps of exposing corncob to steam in a reaction vessel at an elevated temperature and reaction pressure for a preselected exposure time, venting volatile compounds continuously over the pretreatment time and releasing the reaction pressure for explosive decomposition of the corncob biomass into a fibrous solids portion and a condensate portion, wherein the exposing step is carried out at a temperature of 190° C.-210° C. and a pressure of 190 psig to 275 psig and an exposure time of 3 to 10 minutes for minimizing the acetic content in the fibrous solids portion.

2. A process for the pretreatment of corncob biomass for biofuel production by fermentation, comprising the steps of exposing corncob to steam in a reaction vessel at an elevated temperature and reaction pressure for a preselected exposure time, venting volatile compounds continuously over the pretreatment time and releasing the reaction pressure for explosive decomposition of the corncob biomass into a fibrous solids portion and condensate, wherein the exposing step is carried out at a temperature of 203-207° C. and a pressure of 220-250 psig and an exposure time of 7-9 minutes for minimizing acetic acid content in the fibrous solids portion.

3. The process of claim 2 , further comprising the steps of separately capturing the condensate and the solids generated during the pressure release and removing the captured condensate.

4. The process of claim 2 , comprising the further step of collecting condensate and liquid reaction products in the reaction vessel during the exposure time and removing the collected reaction products from the reaction vessel prior to the pressure release.

5. A process for the pretreatment of corncob biomass for biofuel production by fermentation, comprising the steps of exposing corncob to steam in a reaction vessel at an elevated temperature and reaction pressure for a preselected exposure time, venting volatile compounds continuously over the pretreatment time and releasing the reaction pressure for explosive decomposition of the corncob biomass into a fibrous solids portion and condensate, wherein the exposing step is carried out at a temperature of 205° C., a pressure of 235 psig and for a time interval of 8 minutes for minimizing acetic acid content in the fibrous solids portion.

6. The process of claim 5 , wherein the pressure is released within less than 1000 milliseconds.

7. The process of claim 6 , wherein the pressure is released within 300 milliseconds.

8. A process for the pretreatment of corncob biomass, comprising the steps of exposing corncob to steam in a reaction vessel at an elevated temperature and reaction pressure for a preselected exposure time, venting volatiles and releasing the reaction pressure for explosive decomposition of the corncob biomass into fibrous solids and condensate, the process conditions being selected for the achievement of a severity index of 3.88 to 4.11.

9. The process of claim 8 , comprising the further step of collecting condensate and liquid reaction products in the reaction vessel during the exposure time and removing the collected reaction products from the reaction vessel prior to the pressure release.

10. The process of claim 8 , wherein the process conditions are selected for the achievement of a severity index of 4.0.

Assignments (4)
CHANGE OF NAME Recorded Nov 13, 2013
From: GREENFIELD ETHANOL INC.
To: GREENFIELD SPECIALTY ALCOHOLS INC.
Reel/Frame 031628/0314 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 28, 2012
From: LEHOUX, RICHARD ROMEO
To: GREENFIELD ETHANOL INC.
Reel/Frame 028457/0787 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE NAME PREVIOUSLY RECORDED ON REEL 023588 FRAME 0075. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNEE'S NAME WAS INCORRECTLY IDENTIFIED AS "GREENFIELD ETHANOL", WHEN IT SHOULD IN FACT BE "GREENFIELD ETHANOL INC.". Recorded Mar 10, 2010
From: BENSON, ROBERT ASHLEY COOPER; BRADT, CHRIS; BENECH, REGIS-OLIVIER
To: GREENFIELD ETHANOL INC.
Reel/Frame 024057/0715 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 1, 2009
From: BENSON, ROBERT ASHLEY COOPER; BRADT, CHRIS; BENCH, REGIS-OLIVIER
To: GREENFIELD ETHANOL
Reel/Frame 023588/0075 →
Continuity (2)
Provisional Application 61097692 · Sep 17, 2008
Related Publication 20100065128A1 · Mar 18, 2010