ENZYMATIC TREATMENT OF LIGNOCELLULOSIC MATERIALS

• US 20090098616A1
• Filed: 10/08/2008
• Published: 04/16/2009
• Est. Priority Date: 10/09/2007
• Status: Abandoned Application

• Current Assignee: Mascoma Canada Inc.
• Original Assignee: Mascoma Canada Inc.
• Inventors: Burke, Murray, Ishizawa, Claudia, Saville, Bradley
• Application Number:
  US12/247,554
• Publication Number:
  US 20090098616A1
• Time in Patent Office: Days
• US Class Current: 435/99
• 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 7/04 acyclic
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

A method for treating plant materials to release fermentable sugars is disclosed. More specifically, a two-stage enzymatic hydrolysis process for treating lignocellulosic materials and producing a sugar rich process stream that may subsequently be subjected to fermentation to produce biofuels and chemicals is disclosed.

Claims

1. A method for treating a lignocellulosic feedstock comprising cellulose, hemicellulose and lignin to produce a sugar rich process stream, the method comprising:

a) subjecting the feedstock to a first enzymatic hydrolysis process using a first enzyme preparation and obtaining a volatile component stream and a low viscosity effluent stream;

b) subjecting the low viscosity effluent stream to a second enzymatic hydrolysis process using a second enzyme preparation and obtaining a sugar rich process stream.

2. The method of claim 1 wherein the low viscosity effluent stream has a viscosity that is at least 15% lower than that of the feedstock.

3. The method of claim 1 wherein the low viscosity effluent stream has a viscosity that is at least 20% lower than that of the feedstock.

4. The method of claim 1 wherein the low viscosity effluent stream has a viscosity that is at least 50% lower than that of the feedstock.

5. The method of claim 1 wherein the first enzyme preparation preferentially acts upon the hemicellulose relative to cellobiose in the feedstock.

6. The method of claim 1 wherein the first enzyme preparation has hemicellulase activity and cellulase activity.

7. The method of claim 6 wherein the first enzyme preparation has a hemicellulase activity of about 10 to about 90% and a cellulase activity of between 90 to 10%.

8. The method of claim 6, wherein the first enzyme preparation has a hemicellulase activity of about 30% to about 90% and a cellulase activity of about 70% to about 10%.

9. The method of claim 8, wherein the first enzyme preparation has a hemicellulase activity of about 50% to about 90% and a cellulase activity of about 50% to 10%

10. The method of claim 7 wherein the hemicellulase enzymes preferentially act upon the β

-1,4 linkage of the xylose residues of xylan and the β

-1,4 linkage of the mannose residues of mannan.

11. The method of claim 1 wherein the second enzyme preparation preferentially acts on the cellulose and cellobiose relative to xylans in the feedstock.

12. The method of claim 11 wherein the second enzyme preparation comprises β

-glucosidase and cellulase enzymes, wherein the β

-glucosidase and cellulase enzymes preferentially act upon the β

-1,4 linkage of cellobiose and cellulose.

13. The method of claim 12 wherein the p-glucosidase and cellulase enzymes completely convert cellulose and oligosaccharides produced from the first enzymatic hydrolysis to monomeric sugars.

14. The method of claim 13, wherein at least 60% of the cellulose and oligosaccharides are converted to monomeric sugars.

15. The method of claim 14, wherein at least 75% of the cellulose and oligosaccharides are converted to monomeric sugars.

16. The method of claim 15, wherein at least 90% of the cellulose and oligosaccharides are converted to monomeric sugars

17. The method of claim 1 wherein the feedstock is subjected to at least one of activation, extraction, hydrolysis and physical modification prior to step (a).

18. The method of claim 17 wherein the at least one of activation, extraction, hydrolysis and physical modification is produced by at least one of auto-hydrolysis, acid hydrolysis, ammonia activation, disc refining, kraft pulping, organic solvent pulping, hot water pretreatment, ammonia percolation, lime pretreatment, caustic solvent pulping, and alkali peroxide pretreatment.

19. The method of claim 18 wherein the at least one of activation, extraction, hydrolysis and physical modification comprises autohydrolysis that is conducted by steam explosion.

20. The method of claim 1 further comprising using the sugar rich process stream to produce sugar derived products for fermentation.

21. The method of claim 1 further comprising using the sugar rich process stream to produce a raw alcohol stream through fermentation.

22. The method of claim 21, wherein the raw alcohol stream comprises an alcohol content of about 3% to about 22% (v/v).

23. The method of claim 22, wherein the raw alcohol stream comprises an alcohol content of about 5% to about 22% (v/v).

24. The method of claim 23, wherein the raw alcohol stream comprises an alcohol content of about 8% to about 22% (v/v).

25. The method of claim 21 wherein the alcohol is at least one of methanol, ethanol and butanol.

26. The method of claim 1 wherein at least one yeast, fungi, bacteria and enzyme inhibiting compound is present during the first enzymatic hydrolysis process and the method further comprises operating the first enzymatic hydrolysis process under vacuum.

27. The method of claim 26 wherein the first enzymatic hydrolysis process is operated under a vacuum of at least 100 mm Hg.

28. The method of claim 26 wherein the method further comprises operating the second enzymatic process under vacuum.

29. The method of claim 26 wherein the at least one inhibiting compound comprises at least one of furfural, HMF, organic acids, phenolic compounds and the method further comprises operating the first enzymatic hydrolysis process under vacuum to reduce the level of at least one inhibiting compound.

30. The method of claim 26 wherein the at least one inhibiting compound comprises at least one of furfural, HMF, organic acids, phenolic compounds and the method further comprises operating the second enzymatic hydrolysis process under vacuum to reduce the level of at least one inhibiting compound.

31. The method of claim 1 further comprising passing the feedstock through a disc refiner prior to step (a).

32. The method of claim 1 further comprising obtaining a recycle stream from step (a) and reintroducing the recycle stream into the first enzymatic hydrolysis process.

33. The method of claim 32 wherein a portion of the recycle stream is first passed through a disc refiner.