FRACTIONATION OF LIGNOCELLULOSIC BIOMASS FOR CELLULOSIC ETHANOL AND CHEMICAL PRODUCTION

• US 20130017589A1
• Filed: 07/17/2012
• Published: 01/17/2013
• Est. Priority Date: 04/23/2009
• Status: Abandoned Application

• Current Assignee: GreenField Specialty Alcohols Inc.
• Original Assignee: GreenField Ethanol Inc.
• Inventors: DOTTORI, Frank A., BENSON, Robert Ashley Cooper, BENECH, Regis-Olivier
• Application Number:
  US13/551,087
• Publication Number:
  US 20130017589A1
• Time in Patent Office: Days
• US Class Current: 435/165
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: C13K 13/002 Xylose
• CPC Class Codes: D21B 1/36 Explosive disintegration by sudden pressure reduction
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

A process is defined for the continuous steam pretreatment and fractionation of corn cobs and low lignin lignocellulosic biomass to produce a concentrated cellulose solid stream that is sensitive to enzymatic hydrolysis. Valuable chemicals are recovered by fractionating the liquid and vapor stream composed of hydrolysis and degradation products of the hemicellulose. Cellulosic derived glucose is produced for fermentation to biofuels. A hemicellulose concentrate is recovered that can be converted to value added products including ethanol.

Claims

1. A continuous process for fractionation of lignocellulosic biomass having a lignin content of less than 12% and an acetyl group content of 3-6% weight/weight in the dry matter, comprising the steps of:

a) autohydrolysis of the hemicellulose fraction in the lignocellulosic biomass in the absence of any added acid catalyst, by exposing the biomass in a reaction vessel to steam at an elevated temperature and reaction pressure and for a preselected exposure time to achieve a severity index of about 4.0, the severity index (SI) being calculated as

SI=Log×

Exp [(treatment temperature (°

C.)−

100°

C.)/14.75]×

Retention Time (min),

to obtain a prehydrolyzed lignocellulosic biomass;

b) purging liquid condensate and vapor generated during the exposing step to remove and collect a first liquid stream with water soluble compounds and a first vapor stream with volatile chemicals;

c) liquid extracting from the prehydrolyzed lignocellulosic biomass a liquid hemicellulose degradation stream containing hemicellulose hydrolysis and degradation components;

d) rapidly releasing the reaction pressure after the extracting step to afford explosive decompression of the extracted, prehydrolyzed lignocellulosic biomass into fibrous solids, vapor and condensate;

e) collecting vapor and condensate released during the explosive decompression as a second vapor stream and a second liquid stream; and

f) combining the first and second liquid streams with the liquid hemicellulose degradation stream for separation and recovery of byproducts.

2. A process for producing bio ethanol from lignocellulosic biomass having a lignin content of less than 12% and an acetyl group content of 3-6% weight/weight in the dry matter, comprising the steps of:

a) fractionating the biomass using the process of claim 1;

b) separating a pretreated cellulose stream from the prehydrolyzed lignocellulosic biomass;

c) hydrolyzing the pretreated cellulose stream with cellulose enzymes to generate fermentable sugars;

d) adding ethanol producing yeast to the fermentable sugars to generate a fermentation broth; and

e) extracting ethanol from the fermentation broth.

3. The process of claim 1, where the lignocellulosic biomass is selected from the group consisting of corn cobs, miscanthus, sugar cane bagasse, switchgrass, prairie grass, sorghum bagasse, corn stover, and wheat straw.

4. The process of claim 1, wherein the process is carried out in a pretreatment exposing system and volatile compounds are removed continuously by venting the pretreatment exposing system.

5. The process of claim 1, wherein the process is carried out in a pretreatment exposing system and the purging of the liquid condensate takes place continuously at purging points in the pretreatment exposing system.

6. The process of claim 1, wherein solubilized degradation byproducts of hemicellulose created in the exposing step are extracted and removed from the pretreated lignocellulosic biomass under pressure prior to explosive decompression.

7. The process of claim 6, wherein an eluent is added to the pretreated lignocellulosic biomass prior to the step of extracting and removing the hemicellulose under pressure.

8. The process of claim 6, wherein the process is carried out in a pretreatment unit having a pretreatment reactor with an outlet connected to a solid-liquid separation device, and wherein wash water is added at a bottom of the pretreatment reactor and/or along the solid-liquid separation device to achieve a greater extraction of a soluble hemicellulose fraction of the lignocellulosic biomass.

9. The process of claim 1, wherein solubilized byproducts of hemicellulose degradation created in the exposing step are extracted and removed from the solid portion both before and after explosive decompression, with or without the addition of an eluent.

10. The process of claim 1, wherein extracted fibrous solids are separated from the liquid by mechanical processing selected from the group consisting of compressing, filtering, centrifuging, and combinations thereof.