Bagasse fractionation for cellulosic ethanol and chemical production

• US 9,932,707 B2
• Filed: 11/13/2015
• Issued: 04/03/2018
• Est. Priority Date: 11/05/2010
• Status: Active Grant

• Current Assignee: GreenField Specialty Alcohols Inc.
• Original Assignee: GreenField Specialty Alcohols Inc.
• Inventors: Dottori, Frank A., Benson, Robert Ashley Cooper, Benech, Rgis-Olivier
• Primary Examiner(s): MINSKEY, JACOB T
• Application Number:
  US14/940,992
• Publication Number:
  US 20160069020A1
• Time in Patent Office: 872 Days
• Field of Search: 162 68
• CPC Class Codes: C08B 37/0057 beta-D-Xylans, i.e. xylosaccharide, e.g. arabinoxylan, arabinofuronan, pentosans; (beta-1,3)(beta-1,4)-D-Xylans, e.g. rhodymenans; Hemicellulose; Derivatives thereof
• CPC Class Codes: C08H 8/00 Macromolecular compounds derived from lignocellulosic materials pretreatment thereof B27N
• CPC Class Codes: C12P 19/02 Monosaccharides 2-ketogulonic acid C12P7/60
• CPC Class Codes: C12P 19/14 produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase , e.g. by cellulase, hemicellulase
• CPC Class Codes: C12P 2201/00 Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• 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: D21C 1/02 with water or steam
• CPC Class Codes: D21C 11/0007 Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for volatile compounds obtained by decomposition of spent liquors in order to regenerate them D21C11/125; compounds obtained by fractionating the liquors in order to regenerate them D21C11/0042
• CPC Class Codes: D21H 11/12 Pulp from non-woody plants or crops, e.g. cotton, flax, straw, bagasse
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

A process is defined for the continuous steam pretreatment and fractionation of bagasse 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 a bagasse biomass, consisting of the steps of:

a) subjecting the biomass to auto-hydrolysis treatment without the addition of acid or base to obtain a pre-hydrolyzed bagasse biomass by exposing the biomass to steam in a reaction vessel at a preselected temperature of between 170 and 220°

C. and a preselected reaction pressure of between 100 and 322 psig, for a preselected exposure time of between 5 to 90 minutes, to remove a desired amount of a hemicellulose fraction from the bagasse biomass and activate a cellulose fraction of the bagasse biomass; and

subjecting the biomass to auto-hydrolysis treatment without the addition of acid to obtain a pre-hydrolyzed bagasse biomass during the exposing step at the preselected temperature and reaction pressure continually purging liquid condensate and vapor formed during the exposure step to remove and collect a first liquid stream containing water soluble compounds and a first vapor stream containing volatile chemicals;

b) selectively extracting at the selected reaction pressure from the prehydrolysed bagasse biomass a second liquid stream containing hemicellulose hydrolysis and degradation components as a hemicellulose degradation stream, said extracting occurring without the addition of acid or base;

c) rapidly releasing the preselected reaction pressure after the extracting step for explosive decompression of the pre-hydrolyzed bagasse into pretreated fibrous solids, vapor and condensate;

d) collecting the vapor and condensate from the explosive decompression for separation and recovery of byproducts;

e) optionally the bagasse biomass is adjusted to a moisture content of 50% to 70%, and is pre-heated to a temperature of about 100°

C. for a minimum of about 10 minutes prior to pretreatment, wherein the adjustment of moisture content occurs without the addition of acid or base,

f) optionally the pre-heated bagasse biomass is compressed prior to the exposure step to the selected pressure required for the exposure step for removing a third liquid stream containing extractives,

q) optionally the first liquid stream from the pretreatment purge is blended with the second liquid stream extracted from the prehydrolysed bagasse biomass,

h) optionally the bagasse biomass is washed and subsequently separated from dissolved hemicellulose and lignin free xylo-oligosaccharides and remaining inhibitory chemicals prior to the explosive decompression, wherein said washing occurs without the addition of acid or base,

i) optionally pretreated fibrous solids are washed with water, wherein said washing occurs without the addition of acid or base, and

j) optionally the washed fibrous solids are separated from the wash water by a separation process selected from the group consisting of compressing, filtering, centrifuging, and combinations thereof.

2. The process of claim 1, wherein the bagasse biomass is adjusted to a moisture content of 50% to 70%, and is pre-heated to a temperature of about 100°

C. for a minimum of about 10 minutes prior to pretreatment, wherein the adjustment of moisture content occurs without the addition of acid or base.

3. The process of claim 2, wherein the moisture content is 80%.

4. The process of claim 2, wherein the pre-heated bagasse biomass is compressed prior to the exposure step to the selected pressure required for the exposure step for removing a third liquid stream containing extractives.

5. The process of claim 1, wherein the first liquid stream from the pretreatment purge is blended with the second liquid stream extracted from the prehydrolysed bagasse biomass.

6. The process of claim 1, wherein preselected exposure time and preselected temperature are selected to achieve a severity index of 3.88 to 4.11.

7. The process of claim 6, wherein the severity index is 4.0.

8. The process of claim 1, wherein the preselected temperature is between 190 and 210°

C., the preselected pressure is between 165 and 260 psig, and the preselected exposure time is between 7 and 10 minutes.

9. The process of claim 8, wherein the preselected temperature is about 205°

C., the preselected pressure is about 235 psig and the preselected exposure time is about 8 minutes.

10. The process of claim 1, wherein the bagasse biomass is washed and subsequently separated from dissolved hemicellulose and lignin free xylo-oligosaccharides and remaining inhibitory chemicals prior to the explosive decompression, wherein said washing occurs without the addition of acid or base.

11. The process of claim 10, wherein the bagasse biomass is washed under a steam pressure that ranges from 100 psig to 290 psig prior to the explosive decompression, wherein said washing occurs without the addition of acid or base.

12. The process of claim 1, wherein pretreated fibrous solids are washed with water, wherein said washing occurs without the addition of acid or base.

13. The process of claim 12, wherein the washed fibrous solids are separated from the wash water by a separation process selected from the group consisting of compressing, filtering, centrifuging, and combinations thereof.

14. The process of claim 13, wherein the washing is counter current washing.

15. The process of claim 12, wherein the wash water is recycled wash water.

16. The process of claim 1, wherein said bagasse is sugarcane bagasse.

17. The process of claim 1, wherein said bagasse is sorghum bagasse.