Methods and systems for saccharification of biomass

• US 8,563,277 B1
• Filed: 11/27/2012
• Issued: 10/22/2013
• Est. Priority Date: 04/13/2012
• Status: Active Grant

• Current Assignee: Apalta Patents OU
• Original Assignee: SweetWater Energy, Inc
• Inventors: Parekh, Sarad, Felice, Carl P.
• Primary Examiner(s): Weber, Jon P
• Assistant Examiner(s): Luo, Chunyuan
• Application Number:
  US13/686,477
• Publication Number:
  US 20130274455A1
• Time in Patent Office: 329 Days
• Field of Search: None
• US Class Current: 435/105
• 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: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: C13K 13/002 Xylose

Abstract

Provided are methods and compositions for high yields while using reduced enzyme loads in saccharification and fermentation processes. These methods increase the efficiency of enzymes and result in improved yields and composition of saccharification and fermentation end products.

Claims

1. A method of producing a composition comprising C5 and C6 saccharides and low levels of an inhibitor compound from a biomass composition comprising cellulose, hemicellulose, and/or lignocellulose, the method comprising:

(a) pretreating the biomass composition comprising cellulose, hemicellulose, and/or lignocellulose to produce a pretreated biomass composition comprising a mixture of solid particles, wherein at least 50% of the solid particles are less than 1.5 mm in a dimension, and C5 monosaccharides and/or disaccharides in a yield that is at least 50% of a theoretical maximum, wherein pretreating produces low levels of the inhibitor compound and comprises;

(i) hydration of the biomass composition in an acid medium to produce a hydrated biomass composition,

(ii) mechanical size reduction of the hydrated biomass composition to produce the mixture of solid particles, and

(iii) heating the hydrated biomass composition for a time sufficient to produce the pretreated biomass composition comprising C5 monosaccharides and/or disaccharides in the yield that is at least 50% of the theoretical maximum while producing low levels of the inhibitor compound; and

(b) hydrolyzing the pretreated biomass composition with one or more enzymes for a time sufficient to produce the composition comprising C5 and C6 saccharides and low levels of the inhibitor compound.

2. The method of claim 1, wherein at least 50% of the mixture of solid particles in the pretreated biomass composition are from about 0.1 mm to about 1 mm in a dimension.

3. The method of claim 1, wherein all of the solid particles in the pretreated biomass are less than 7.5 mm in a dimension.

4. The method of claim 1, wherein all of the solid particles in the pretreated biomass are less than 1 mm in a dimension.

5. The method of claim 1, wherein the yield of C5 monosaccharides and/or disaccharides is at least 80% of the theoretical maximum.

6. The method of claim 1, wherein the pretreated biomass composition further comprises a yield of glucose that is less than about 20% of a theoretical maximum.

7. The method of claim 1, wherein the hydrated biomass composition comprises from about 1% to about 20% solids by dry biomass weight.

8. The method of claim 1, wherein the acid medium is at from about 30°

C. to about 70°

C.

9. The method of claim 1, wherein hydration of the biomass composition is for about 1 minute to about 60 minutes.

10. The method of claim 1, wherein the acid medium comprises an acid at from about 0.1% to about 5% v/w by dry biomass weight.

11. The method of claim 10, wherein the acid medium comprises the acid that is sulfuric acid, peroxyacetic acid, lactic acid, formic acid, acetic acid, citric acid, phosphoric acid, hydrochloric acid, sulfurous acid, chloroacetic acid, dichloroacetic acid, trichloroacetic acid, trifluoroacetic acid, oxalic acid, benzoic acid, or a combination thereof.

12. The method of claim 1, wherein mechanical size reduction comprises cutting, steam explosion, acid-catalyzed steam explosion, or a combination thereof.

13. The method of claim 1, wherein heating of the hydrated biomass composition is at a temperature of from about 100°

C. to about 250°

C.

14. The method of claim 1, wherein heating of the hydrated biomass composition is performed at a pressure of from about 100 PSIG to about 150 PSIG.

15. The method of claim 1, wherein the time sufficient to produce the yield of C5 monosaccharides and/or disaccharides is from about 1 minute to about 30 minutes.

16. The method of claim 1, wherein pretreating the biomass composition further comprises dewatering the hydrated biomass composition to from about 10% to about 40% solids by dry biomass weight.

17. The method of claim 1, wherein heating comprises steam injection, steam explosion, acid-catalyzed steam explosion, or a combination thereof.

18. The method of claim 1, wherein the pretreating is performed in a continuous mode of operation.

19. The method of claim 1, wherein the pretreating is performed in a total time of from about 15 minutes to about 45 minutes.

20. The method of claim 1, wherein the one or more enzymes comprise one or more hemicellulases and/or one or more cellulases.

21. The method of claim 1, wherein the one or more enzymes are at a total level of from about 1% to about 20% w/w, about 1% to about 10% w/w, or about 1% to about 5% w/w by dry biomass weight.

22. The method of claim 1, further comprising adjusting the water content of the pretreated biomass composition to from about 5% to about 30% solids by dry biomass weight prior to hydrolyzing.

23. The method of claim 1, wherein the composition comprising C5 and C6 saccharides comprises glucose, xylose, mannose, galactose, rhamnose, arabinose, or a combination thereof.

24. The method of claim 1, wherein the composition comprising C5 and C6 saccharides comprises glucose in a yield that is greater than 55% of a theoretical maximum at 21 hours of hydrolysis.

25. The method of claim 1, wherein the biomass composition comprises alfalfa, algae, bagasse, bamboo, corn stover, corn cobs, corn kernels, corn mash, corn steep liquor, corn steep solids, distiller'"'"'s grains, distiller'"'"'s dried solubles, distiller'"'"'s dried grains, condensed distiller'"'"'s solubles, distiller'"'"'s wet grains, distiller'"'"'s dried grains with solubles, eucalyptus, food waste, fruit peels, garden residue, grass, grain hulls, modified crop plants, municipal waste, oat hulls, paper, paper pulp, prairie bluestem, poplar, rice hulls, seed hulls, silage, sorghum, straw, sugarcane, switchgrass, wheat, wheat straw, wheat bran, de-starched wheat bran, willows, wood, plant cells, plant tissue cultures, tissue cultures, or a combination thereof.

26. The method of claim 1, wherein mechanical size reduction does not comprise milling.

27. A composition comprising C5 and C6 saccharides produced by the method of claim 1.

29. The method of claim 1, wherein the dimension is diameter or length.

30. The method of claim 1, wherein the inhibitor compound is furfural.

28. A method of producing a composition comprising C5 and C6 saccharides and low levels of an inhibitor compound from a biomass composition comprising cellulose, hemicellulose, and/or lignocellulose, the method comprising:

(a) pretreating the biomass composition comprising cellulose, hemicellulose, and/or lignocellulose to produce a pretreated biomass composition comprising a mixture of solid particles, wherein at least 50% of the solid particles are less than 1.5 mm in a dimension, and C5 monosaccharides and/or disaccharides in a yield that is at least 50% of a theoretical maximum, wherein pretreating produces low levels of the inhibitor compound and comprises;

(i) hydration of the biomass composition in an acid medium to produce a hydrated biomass composition,

(ii) mechanical size reduction of the hydrated biomass composition to produce the mixture of solid particles, wherein mechanical size reduction comprises cutting with a first rotating cutter and a second rotating cutter, and

(iii) heating the hydrated biomass composition for a time sufficient to produce the pretreated biomass composition comprising C5 monosaccharides and/or disaccharides in the yield that is at least 50% of the theoretical maximum while producing low levels of the inhibitor compound; and

(b) hydrolyzing the pretreated biomass composition with one or more enzymes for a time sufficient to produce the composition comprising C5 and C6 saccharides and low levels of the inhibitor compound.