Methods of processing lignocellulosic biomass using single-stage autohydrolysis pretreatment and enzymatic hydrolysis
Methods of processing lignocellulosic biomass to fermentable sugars are provided which rely on hydrothermal pretreatment. Soft lignocellulosic biomass feedstock is pretreated in a single-stage pressurized hydrothermal pretreatment to very low severity. The pre-treated biomass is hydrolysed, typically as a whole slurry, using enzymatic hydrolysis catalysed by an enzyme mixture comprising endoglucanase, exoglucanase, β-glucosidase, endoxylanase, and β-xylosidase activities at activity levels in nkat/g glucan of endoglucanase of at least 1100, exoglucanase of at least 280, β-glucosidase of at least 3000, endoxylanase of at least 1400, and β-xylosidase of at least 75, so as to produce a hydrolysate in which the yield of C5 monomers is at least 55% of the original xylose and arabinose content of the feedstock prior to pretreatment.
1. A method of processing lignocellulosic biomass comprising:
Pretreating soft lignocellulosic biomass feedstock at pH within the range 3.5 to 9.0 in a single-stage pressurized hydrothermal pretreatment reactor at a temperature of at least 140° C. for 1 to 60 minutes to log severity Ro 3.75 or lower to produce a pretreated biomass slurry in which the undissolved solids comprise at least 5.0% by weight xylan, and
Hydrolysing the pretreated biomass slurry as a whole slurry with or without additional water content using enzymatic hydrolysis for at least 24 hours catalysed by an enzyme mixture comprising endoglucanase, exoglucanase, β-glucosidase, endoxylanase, and β-xylosidase activities at activity levels measured in nkat/g glucan, wherein endoglucanase is at least 1100 nkat/g glucan, exoglucanase is at least 280 nkat/g glucan, β-glucosidase is at least 3000 nkat/g glucan, endoxylanase isat least 1400 nkat/g glucan, and β-xylosidase is at least 75 nkat/g glucan, to produce a hydrolysate in which the yield of C5 monomers is at least 55% of the original xylose and arabinose content of the soft lignocellulosic biomass feedstock prior to pretreatment.
2. The method of claim 1 , wherein the hydrothermal pretreatment is conducted as an autohydrolysis, in which acetic acid liberated by hemicellulose hydrolysis during pretreatment further catalyzes hemicellulose hydrolysis.
3. The method of claim 1 , wherein the feedstock is subject to pressurized pretreatment at a dry matter content of at least 35% or at temperature between 160 and 200° C.
4. The method of claim 1 , wherein the whole slurry hydrolysate is used as a biomethane substrate.
5. The method of claim 1 , wherein the enzymatic hydrolysis is conducted at dry matter content between 8 and 19%.
6. The method of claim 4 , wherein the enzymatic hydrolysis is conducted at dry matter content of 20% or greater.
7. The method of claim 1 , wherein the endoglucanase activity is within the range 1100-30000 nkat/g glucan, the exoglucanase activity is within the range 280-20000 nkat/g glucan, the β-glucosidase activity is within the range 3000-50000 nkat/g glucan, the endoxylanase activity is within the range 1400-70000 nkat/g glucan and/or the β-xylosidase activity is within the range 75-20000 nkat/g glucan.
8. The method of claim 7 , wherein the β-glucosidase activity is within the range 4000-50000 nkat/g glucan, the endoxylanase activity is within the range 4000-70000 nkat/g glucan and/or the β-xylosidase activity is within the range 250-20000 nkat/g glucan.
9. The method of claim 1 , wherein the pretreated biomass has a fiber structure that is preserved during pretreatment.
10. The method of claim 1 , wherein the biomass feedstock is subject to particle size reduction and/or other mechanical processing prior to hydrothermal pretreatment.
11. The method of claim 1 , wherein the pretreated biomass is subject to a solid/liquid separation step to produce a liquid fraction and a solid fraction having a dry matter content of at least 40% by weight and the solid fraction is hydrolysed.
12. The method of claim 4 , wherein the separated liquid fraction is added back into the hydrolysis mixture, after enzymatic hydrolysis of the solid fraction has reached a desired degree of glucan conversion.
13. The method of claim 1 , wherein the feedstock is wheat straw, corn stover, sugar cane bagasse, sweet sorghum bagasse, or empty fruit bunches.
14. The method of claim 1 , wherein pressurized pretreatment is conducted at a pressure of 10 bar or lower.
15. The method of claim 1 , further comprising removing the feedstock from the pressurized hydrothermal pretreatment reactor using a hydrocyclone system.
16. The method of claim 1 , wherein enzymatic hydrolysis is conducted for at least 96 hours.
17. The method of claim 1 , further characterized in that the hydrolysate is a C5/C6 hydrolysate and the C5/C6 hydrolysate is directly fermented to ethanol.
18. The method of claim 17 , wherein the ethanol fermentation uses one or more modified yeast strains.