ORGANIC SOLVENT PRETREATMENT OF BIOMASS TO ENHANCE ENZYMATIC SACCHARIFICATION

• US 20100159517A1
• Filed: 12/16/2009
• Published: 06/24/2010
• Est. Priority Date: 12/19/2008
• Status: Active Grant

• 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: Diner, Bruce A., Fan, Janine
• Granted Patent: US 8,278,070 B2
• Time in Patent Office: Days
• US Class Current: 435/72
• 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: 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: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Biomass is pretreated using an organic solvent solution, under alkaline conditions, in the presence of one or more organo-mercaptan and optionally one or more additional nucleophile to fragment and extract lignin. Pretreated biomass is further hydrolyzed with a saccharification enzyme consortium. Fermentable sugars released by saccharification may be utilized for the production of target chemicals by fermentation.

Claims

1. A method for producing carbohydrate-enriched biomass comprising

(a) providing lignocellulosic biomass comprising lignin;

(b) suspending the biomass of (a) in an organic solvent solution comprising water and one or more organo-mercaptan(s) under alkaline conditions whereby a biomass-solvent suspension is formed;

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

C. to about 220°

C. for about 5 minutes to about 5 hours whereby lignin is fragmented and is dissolved in the suspension; and

(d) removing the dissolved lignin to produce a carbohydrate-enriched biomass.

2. The method of claim 1 whereby the dissolved lignin of step (d) is removed by filtration.

3. The method of claim 1 further comprising:

(e) washing the biomass produced in step (d) with a solvent solution.

4. The method of claim 3, further comprising:

(f) washing the biomass produced in step (e) with water to produce a readily saccharifiable carbohydrate-enriched biomass.

5. The method of claim 3 further comprising drying the biomass produced in step (e) to produce a readily saccharifiable carbohydrate-enriched biomass.

6. The method of claims 3 or 4, further comprising repeating steps (e) and (f) one or more times.

7. The method of claim 1 wherein the solvent solution further comprises an additional nucleophile selected from the group consisting of NH₃, one or more alkylamines, NaOH, sulfide reagents, and combinations thereof.

8. The method of claim 7 wherein the additional nucleophile is one or more alkylamine and said one or more alkylamine is at a concentration of up to 20% by weight of dry biomass.

9. The method of claim 1 wherein the solvent solution to biomass in step (b) has a weight ratio of about 10 to 1 to 0.5 to 1.

10. The method of claim 2, wherein the heated suspension of step (c) is cooled to room temperature before filtering in step (d).

11. The method of claim 2 further comprising evaporating off the solvent under vacuum of the filtered and washed biomass after step (e).

12. The method of claims 4, 5 or 11, further comprising saccharifying the biomass with an enzyme consortium whereby fermentable sugars are produced.

13. The method of claim 3, further comprising saccharifying the biomass without drying by contacting said biomass with an enzyme consortium after washing in step (f), whereby fermentable sugars are produced.

14. The method of claims 12 or 13, further comprising fermenting the sugars to produce a target product.

15. The method of claim 14 wherein the target product is selected from the group consisting of alcohols, organic acids, amino acids and gases.

16. The method of claim 1 wherein the biomass is selected from the group consisting of switchgrass, waste paper, sludge from paper manufacture, corn fiber, corn cobs, corn husks, corn stover, grasses, wheat, wheat straw, hay, barley, barley straw, rice straw, sugar cane bagasse, sugar cane straw, yellow poplar, sorghum, soy, components obtained from processing of grains, trees, branches, roots, leaves, wood chips, sawdust, shrubs and bushes, vegetables, fruits, flowers, animal manure and combinations thereof.

19. The method of claims 1 or 17 wherein said organic solvent solution further comprises one or additional component selected from the group consisting of alkali or alkaline earth hydroxides or carbonates, ammonia, thiols, polysulfides and combinations thereof.

20. The method of claims 1 or 17 wherein the solvent solution, and any unreacted organo-mercaptan or other unreacted components are recyclable.

21. The method of claims 1 or 17 wherein said organic solvent solution comprises a solvent selected from the group consisting of alcohols, diols, and aprotic solvents

22. The method of claim 21 wherein the organic solvent solution comprises a solvent selected from the group consisting of methanol, ethanol, propanol, butanol, pentanol and hexanol, isomers thereof, and diols thereof.

26. The method of claim 1 wherein the organo-mercaptan is selected form the group consisting of thioglycolate, 2-mercaptoethanol, dithiothreitol, dithioerythritol, cysteine and glutathione, methanethiol, mono- and disubstituted ethane, propane and butane thiols.

17. A method of simultaneous fragmentation and selective extraction of lignin from lignocellulosic biomass to produce a substantially lignin-free biomass, the method comprising the steps of:

(a) providing;

1) an amount of lignocellulosic biomass;

2) a multi-component solvent solution comprising from about 40% to about 70% ethanol in water;

3) one or more organo-mercaptan(s); and

4) and one or more alkylamine(s) under alkaline conditions;

(b) contacting said biomass with the multi-component solvent solution of (a) to form a solvent-biomass mixture;

(c) placing the solvent-biomass mixture in a sealed pressure vessel whereby the mixture of (b) is heated at a temperature of about 100°

C. to about 220°

C. for about 5 minutes to about 5 hours whereby lignin is fragmented and dissolved in the solvent;

(d) removing the dissolved lignin of (c) by filtration; and

(e) washing the residual biomass with organic solvent, whereby substantially lignin-free biomass is produced.

18. The method of claim 17 wherein the substantially lignin-free biomass is from about 60% to about 100% original weight of the biomass.

23. The method of claims 7 or 17 wherein the one or more alkylamines is selected from the group consisting of R—

NH₂, R₂—

NH, R₃N, (H₂N—

R—

NH₂), (H₂N—

R(NH₂)₂), (HO—

R—

NH₂), ((HO)₂—

R—

NH₂), (HO—

R—

(NH₂)₂), (HS—

R—

NH₂), ((HS)₂—

R—

NH₂), (HS—

R—

(NH₂)₂) and (H₂N—

R(OH)(SH) and combinations thereof, wherein R is independently a monovalent, divalent or trivalent 1-6 carbon alkane, alkene or alkyne, linear, cyclic or branched.

24. The method of claim 23 wherein R is independently methyl, ethyl, propyl or butyl.

25. The method of claim 23 wherein the alkylamine is methylamine.

27. The method of claim 17 wherein the temperature of the step (c) is from about 165°

C. to about 195°

C.