Process for concentrated biomass saccharification
View Patent ↗Processes for saccharification of pretreated biomass to obtain high concentrations of fermentable sugars are provided. Specifically, a process was developed that uses a fed batch approach with particle size reduction to provide a high dry weight of biomass content enzymatic saccharification reaction, which produces a high sugars concentration hydrolysate, using a low cost reactor system.
1. A process for producing high-sugar content hydrolysate from biomass comprising:
a) providing a portion of reaction components in a vertical stirred tank reactor having a particle size reduction mechanism, said reaction components comprising:
i) a portion of a mixable pretreated biomass slurry; and
ii) a saccharification enzyme consortium comprising at least one enzyme capable of hydrolyzing cellulose;
b) reacting said slurry and enzymes under suitable conditions;
c) applying the particle size reduction mechanism;
d) adding an additional portion of pretreated biomass producing a higher solids biomass slurry;
e) optionally adding an additional portion of (ii) or another saccharification enzyme consortium comprising cellulases, hemicellulases, or mixtures thereof;
f) reacting said higher solids biomass slurry under suitable conditions; and
g) optionally repeating one or more steps (c), (d), (e), and (f) one or more times,
whereby a high sugar content hydrolysate is produced, wherein the concentration of total soluble sugars produced is at least about 100 g/L, and wherein the yield stress of the slurry is maintained at less than 30 Pa.
2. The process of claim 1 , wherein the mixable portion of a pretreated biomass slurry of step (a) (i) is provided by combining a heel of low viscosity component and a portion of pretreated biomass in the vertical stirred tank reactor and adjusting the temperature and pH prior to adding enzyme.
3. The process of claim 1 wherein the portions of biomass are added continuously.
4. The process of claim 1 wherein the dry weight of biomass in all pretreated biomass portions combined is greater than 20% of the weight of the final hydrolysate product.
5. The process of claim 1 wherein applying the particle size reduction mechanism is performed one or more times before, during, or after step (b), or any combination thereof.
6. The process of claim 1 wherein said size reduction mechanism comprises mechanical size reduction.
7. The process of claim 6 wherein said mechanical size reduction mechanism is immersed in the reactor tank or incorporated in a recycle loop.
8. The process of claim 1 wherein pH and temperature are controlled following adding an additional portion of pretreated biomass.
9. The process of claim 2 or 8 wherein the pH is adjusted to between about 4 and about 10.
10. The process of claim 9 wherein the pH is adjusted to be between about 4.5 and about 6.
11. The process of claim 2 or 8 where the temperature is adjusted to between about 20° C. and about 80° C.
12. The process of claim 11 wherein the temperature is adjusted to be between about 25° C. and about 60° C.
13. The process of claim 4 wherein the dry weight of biomass is at least about 24%.
14. The process of claim 13 wherein the dry weight of biomass is at least about 30%.
15. The process of claim 1 wherein one enzyme capable of hydrolyzing cellulose is selected from the group consisting of cellulases, endoglucanases, exoglucanases, cellobiohydrolases, -glucosidases.
16. The process of claim 1 wherein the first saccharification enzyme consortium of (a) (ii), the additional saccharification enzyme consortium of (e), and additional saccharification enzyme consortia of other optional repetitions may be comprised of the same or different enzymes.
17. The saccharification enzyme consortia of claim 16 wherein each consortium comprises cellulases, hemicellulases, or mixtures thereof.
18. The process of claim 1 wherein said biomass is selected from the group consisting of switchgrass, waste paper, sludge from paper manufacture, corn grain, corn cobs, corn husks, corn stover, corn fiber, grasses, wheat, wheat straw, hay, barley, barley straw, rice straw, sugar cane bagasse, sorghum, soy, components obtained from milling of grains, trees, branches, roots, leaves, wood chips, sawdust, shrubs and bushes, vegetables, fruits, flowers and animal manure.
19. The process of claim 18 wherein biomass is selected from the group consisting of corn cobs, corn stover, corn fiber, corn husks, sugar cane bagasse, sawdust, switchgrass, wheat straw, hay, rice straw, and grasses.
20. The process of claim 18 wherein biomass is selected from the group consisting of corn cobs, corn stover, corn fiber, sawdust, and sugar cane bagasse.
21. The process of claim 1 wherein said biomass is derived from multiple feedstocks.
22. The process of claim 1 wherein said high sugar content hydrolysate comprises monosaccharides and oligosaccharides.
23. The process of claim 22 , wherein the concentration of sugars in said hydrolysate is at least about 100 g/L.
24. The hydrolysate produced by the process of claim 1 .