ORGANOSOLV AND OZONE TREATMENT OF BIOMASS TO ENHANCE ENZYMATIC SACCHARIFICATION

• US 20100159522A1
• Filed: 12/17/2009
• Published: 06/24/2010
• Est. Priority Date: 12/19/2008
• Status: Abandoned Application

• Current Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Original Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Inventors: CIRAKOVIC, JELENA
• Application Number:
  US12/640,351
• Publication Number:
  US 20100159522A1
• Time in Patent Office: Days
• US Class Current: 435/72
• CPC Class Codes: C08H 6/00 Macromolecular compounds derived from lignin, e.g. tannins, humic acids
• 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: 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: D21C 3/02 with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
• CPC Class Codes: D21C 3/20 with organic solvents or in solvent environment
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Lignocellulosic biomass comprising lignin is treated with a solvent, such as organosolv, under alkaline conditions at elevated temperatures, filtered, then contacted with a gas comprising ozone to produce a readily saccharifiable biomass.

Claims

1. A method for producing readily saccharifiable carbohydrate-enriched biomass, the method comprising:

(a) providing lignocellulosic biomass comprising lignin;

(b) contacting the biomass with an organic solvent solution comprising water and at least one inorganic base selected from the group consisting of sodium hydroxide, sodium carbonate, potassium hydroxide, potassium carbonate, calcium hydroxide, calcium carbonate, ammonia, and mixtures thereof whereby a biomass-solvent suspension is formed;

(c) heating the biomass-solvent suspension to a temperature of about 100°

C. to about 220°

C. and for a reaction time of about 15 minutes to about 48 hours whereby lignin is fragmented from the biomass and is dissolved in the suspension;

(d) filtering free liquid under pressure after heating the suspension in (c) whereby the dissolved lignin is removed whereby pretreated biomass is formed;

(e) contacting the pretreated biomass from (d) with a gas comprising ozone at a temperature of about 0°

C. to about 50°

C. and for a reaction time of at least about 1 minute whereby a readily saccharifiable carbohydrate-enriched biomass is produced.

2. The method of claim 1, further comprising:

after (d) and before (e), washing the pretreated biomass produced in step (d) with the organic solvent solution.

3. The method of claim 1, wherein the lignocellulosic biomass is subjected to preprocessing prior to step (a).

4. The method of claim 1, wherein the organic solvent solution further comprises an alcohol selected from the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, 2-butanol, isobutanol, and t-butanol, and mixtures of these.

5. The method of claim 4, wherein the alcohol is ethanol.

6. The method of claim 5, wherein the organic solvent solution contains about 0 to about 100 percent (volume/volume) ethanol.

7. The method of claim 1, wherein the amount of the inorganic base is about 1 weight percent to about 14 weight percent, relative to dry weight of biomass.

8. The method of claim 1, wherein the dry weight of biomass is at a concentration of from about 15% to about 70% of the weight of the biomass-solvent suspension of (b).

9. The method of claim 1, wherein the gas comprises about 0.1 to about 20 percent by volume ozone.

10. The method of claim 1, wherein the gas further comprises air, nitrogen, oxygen, argon, or a combination thereof.

11. The method of claim 1, wherein the ratio of ozone to pretreated biomass in step (e) is at least about 1:

1200 on a weight basis.

12. The method of claim 1, further comprising, prior to step (e), a step of contacting the pretreated biomass with a second solvent solution comprising water, whereby a second biomass-solvent suspension is formed.

13. The method of claim 12, wherein the weight percent of biomass in the second biomass-solvent suspension is from about 20 to about 70.

14. The method of claim 1 or 12, wherein the pretreated biomass contains about 30 to about 60 percent moisture.

15. The method of claim 1, further comprising saccharifying the readily saccharifiable carbohydrate-enriched biomass with an enzyme consortium whereby fermentable sugars are produced.

16. The method of claim 15, further comprising fermenting the sugars to produce a target compound.