Treatment of biomass to obtain a target chemical
View Patent ↗Target chemicals were produced using biocatalysts that are able to ferment sugars derived from treated biomass. Sugars were obtained by pretreating biomass under conditions of high solids and low ammonia concentration, followed by saccharification.
1. A method for producing a target chemical derivable from biomass comprising:
a) for a period of time up to about 25 hours, contacting biomass with an aqueous solution comprising ammonia, wherein the ammonia is present at a concentration at least sufficient to maintain alkaline pH of the biomass-aqueous ammonia mixture but wherein said ammonia is present at 12 or less weight percent relative to dry weight of biomass, and further wherein the dry weight of biomass is at a solids concentration of at least about 15 weight percent relative to the weight of the biomass-aqueous ammonia mixture;
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; and
c) contacting the product of step (b) with at least one biocatalyst able to ferment the sugars to produce the target chemical under suitable fermentation conditions.
2. The method of claim 1 wherein steps (b) and (c) are performed concurrently.
3. The target chemical of claim 1 selected from the group consisting of acids, alcohols, alkanes, alkenes, aromatics, aldehydes, ketones, biopolymers, proteins, peptides, amino acids, vitamins, antibiotics, and pharmaceuticals.
4. The method of claim 1 , wherein the target chemical is selected from the group consisting of methanol, ethanol, propanol, isopropanol, butanol, ethylene glycol, propanediol, butanediol, glycerol, erythritol, xylitol, sorbitol, acetic acid, lactic acid, propionic acid, 3-hydroxypropionic acid, butyric acid, gluconic acid, itaconic acid, citric acid, succinic acid, levulinic acid, glutamic acid, aspartic acid, methionine, lysine, glycine, arginine, threonine, phenylalanine, tyrosine, methane, ethylene, acetone, and industrial enzymes.
5. The method of claim 4 , wherein the target chemical is lactic acid, propanediol, or ethanol.
6. The method of claim 1 wherein said at least one biocatalyst is selected from the group consisting of bacteria, filamentous fungi and yeast.
7. The method of claim 1 wherein said at least one biocatalyst is selected from the group consisting of wild type, mutant, or recombinant Escherichia, Zymomonas, Candida, Saccaromyces, Pichia, Streptomyces, Bacillus, Lactobacillus and Clostridium.
8. The method of claim 1 wherein said at least one biocatalyst is selected from the group consisting of recombinant Escherichia coli, Zymomonas mobilis, Bacillus stearothermophilus, Saccharomyces cerevisiae, Clostridia thermocellum, Thermoanaerobacterium saccharolyticum , and Pichia stipitis.
9. The method of claim 1 wherein the pH of the biomass-aqueous ammonia mixture is greater than 8.
10. The method of claim 1 wherein vacuum is applied to the biomass prior to contacting the biomass with an aqueous solution comprising ammonia.
11. The method of claim 1 wherein said dry weight of biomass is at a solids concentration of from at least about 15% to about 80%.
12. The method of claim 11 wherein said dry weight of biomass is at a solids concentration of from at least about 15% to about 60%.
13. The method of claim 1 wherein said ammonia is present at less than about 10 weight percent relative to dry weight of biomass.
14. The method of claim 13 wherein said ammonia is present at about 6% or less weight percent relative to dry weight of biomass.
15. 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.
16. 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, barley, barley straw, rice straw, sugar cane bagasse, sorghum, soy, components obtained from processing of grains, trees, branches, roots, leaves, wood chips, sawdust, shrubs and bushes, vegetables, fruits, flowers and animal manure.
17. The method of claim 16 wherein biomass is selected from the group consisting of corn cobs, corn stover, corn husks, sugar cane bagasse, sawdust, switchgrass, wheat straw, hay, barley straw, rice straw, and grasses.
18. The method of claim 17 wherein biomass is selected from the group consisting of corn cobs, corn stover, sawdust, and sugar cane bagasse.
19. The method of claim 1 wherein ammonia selected from the group consisting of ammonia gas, ammonium hydroxide, urea, and combinations thereof.
20. The method of claim 1 wherein (a) is carried out at a temperature of from about 4° C. to about 200° C.
21. The method of claim 20 wherein (a) is carried out at a temperature of from about 75° C. to about 150° C.
22. The method of claim 21 wherein (a) is carried out at a temperature of from greater than 90° C. to about 150° C.
23. The method of claim 1 wherein (a) is carried out for a period of time of up to about 8 hours.
24. The method of claim 1 or claim 2 wherein at least a portion of the ammonia of (a) is removed prior to (b).
25. The method of claim 24 wherein ammonia from (a) is recycled.
26. The method of claim 1 wherein (a), (b) or (a) and (b) are repeated at least one time.
27. The method of claim 1 further comprising adding at least one plasticizer, softening agent or combination thereof in (a).
28. The method of claim 27 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.
29. The method of claim 1 further comprising applying energy for reducing the size of the biomass during (a), before or during (b), or a combination thereof.
30. The method of claim 29 wherein said energy is selected from the group consisting of milling, crushing, grinding, shredding, chopping, disk refining, ultrasound and microwave.
31. The method of claim 1 , wherein carbon dioxide from fermentation is used to adjust the pH of the pretreatment mixture prior to saccharification.
32. The method of claim 1 wherein said saccharification enzyme consortium comprises at least one glycosidase.
33. 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.
34. The method of claim 1 wherein said saccharification enzyme consortium comprises at least two enzymes selected from the group consisting of cellulases, endoglucanases, exoglucanases, cellobiohydrolases, “β-glucosidases”, xylanases, endoxylanases, exoxylanases, β-xylosidases, arabinoxylanases, mannases, galactases, pectinases, glucuronidases, amylases, α-amylases, β-amylases, glucoamylases, α-glucosidases and isoamylases.
35. The method of claim 1 wherein (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.