Treatment of biomass to obtain fermentable sugars
View Patent ↗Biomass is pretreated using a low concentration of aqueous ammonia at high biomass concentration. 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.
1. A method for treating biomass to produce fermentable sugars comprising:
a) for a period of time up to about 25 hours, contacting biomass with an aqueous solution comprising ammonia to form a biomass-aqueous ammonia mixture, wherein the ammonia is present at a concentration at least sufficient to maintain alkaline pH of the biomass-aqueous ammonia mixture wherein said ammonia is present at 12 weight percent or less, relative to dry weight of biomass, and further wherein the dry weight of biomass is at a solids concentration of about 15 weight percent or more relative to the weight of the biomass-aqueous ammonia mixture, to produce a pretreated biomass product; and
b) contacting the product of step (a) with a saccharification enzyme consortium comprising one or more hemicellulose-hydrolyzing glycosidase, under suitable conditions, to produce fermentable sugars wherein said fermentable sugars provide a carbohydrate source for a biocatalyst for a fermentation process.
2. The method of claim 1 wherein the pH of the biomass-aqueous ammonia mixture is greater than 8.
3. The method of claim 1 wherein vacuum is applied to the biomass prior to contacting the biomass with an aqueous solution comprising ammonia.
4. The method of claim 1 wherein said dry weight of biomass is a solids concentration of from about 15% to about 80%.
5. The method of claim 3 wherein said dry weight of biomass is a solids concentration of from about 15% to about 60%.
6. The method of claim 1 wherein said ammonia is present at 10 weight percent, or less, relative to dry weight of biomass.
7. The method of claim 1 wherein said ammonia is present at 6 or less weight percent relative to dry weight of biomass.
8. The method of claim 1 wherein biomass is selected from the group consisting of bioenergy crops, agricultural residues, municipal solid waste, industrial solid waste, yard waste, wood and forestry waste.
9. The method of claim 1 wherein biomass is selected from the group consisting of switchgrass, waste paper, sludge from paper manufacture, corn grain, corn cobs, corn husks, corn stover, grasses, wheat, wheat straw, hay, rice straw, sugar cane bagasse, sorghum, soy, trees, branches, roots, leaves, wood chips, sawdust, shrubs and bushes, vegetables, fruits, flowers and animal manure.
10. The method of claim 9 wherein biomass is selected from the group consisting of corn cobs, corn stover, corn husks, sugar can bagasse, switchgrass, wheat straw, hay, barley, barley straw, rice straw, and grasses.
11. The method of claim 10 wherein biomass is selected from the group consisting of corn cobs, corn stover and sugar cane bagasse.
12. The method of claim 1 wherein the ammonia is selected from the group consisting of ammonia gas, ammonium hydroxide, urea, and combinations thereof.
13. The method of claim 1 wherein said aqueous solution comprising ammonia further comprises at least one additional base.
14. The method of claim 13 wherein said at least one base is selected from the group consisting of sodium hydroxide, sodium carbonate, potassium hydroxide, potassium carbonate, calcium hydroxide, and calcium carbonate.
15. The method of claim 1 wherein (a) is carried out a temperature of from about 4° C. to about 200° C.
16. The method of claim 15 wherein (a) is carried out a temperature of from about 75° C. to about 150° C.
17. The method of claim 16 wherein (a) is carried out a temperature of from greater than 90° C. to about 150° C.
18. The method of claim 1 wherein (a) is carried out for a period of time of up to about 8 hours.
19. The method of claim 1 or claim 2 wherein at least a portion of the ammonia of a) is removed prior to (b).
20. The method of claim 1 wherein ammonia from (a) is recycled.
21. The method of claim 1 wherein the contacting of (b) is at a dry weight of biomass concentration of at least 15%.
22. The method of claim 1 wherein (a), (b) or (a) and (b) are repeated at least one time.
23. The method of claim 1 further comprising adding at least plasticizer, softening agent or combination thereof in (a).
24. The method of claim 23 wherein said at least one plasticizer, softening agent or combination thereof is selected from the group consisting of polyols, esters of polyols, glycol ethers, acetamide, ethanol, and ethanolamines.
25. The method of claim 1 , further comprising applying energy before or during (a), before or during (b), or a combination thereof.
26. The method of claim 25 wherein said energy is selected from the group consisting of milling, crushing, grinding, shredding, chopping, disk refining, ultrasound and microwave.
27. The method of claim 1 , wherein carbon dioxide from fermentation is used to adjust the pH of the pretreatment mixture prior to saccharification.
28. The method of claim 1 wherein said saccharification enzyme consortium further comprises at least one additional enzyme selected from the group consisting of cellulose-hydrolyzing glycosidases, starch-hydrolyzing glycosidases, peptidases, lipases, ligninases and feruloyl esterases.
29. The method of claim 1 wherein said saccharification enzyme consortium comprises at least two enzymes selected from the group consisting of cellulases, endoglucanases, exoglucanases, cellobiohydrolasese, β-glucosidases, xylanases, endoxylanases, exoxylanases, β-xylosidases, arabinoxylanases, mannases, galactases, pectinases, glucuronidases, amylases, α-amylases, β-amylases, glucoamylases, α-glucosidases, and isoamylases.
30. The method of claim 1 wherein step (b) is performed at a temperature of from about 15° C. to about 100° C. and at a pH of from about 2 to about 11.