Methods for mitigating the inhibitory effects of lignin and soluble phenolics for enzymatic conversion of cellulose
Disclosed herein are methods for improving ethanol production from biomass sources by blocking cellulose from binding to lignin.
1. A method for improving enzymatic digestibility of lignocellulose, comprising:
pretreating a lignocellulose feedstock comprising cellulose, hemicellulose, and lignin with at least a two-step hydrothermal pretreatment to produce a pretreated lignocellulose feedstock, wherein the first hydrothermal pretreatment is conducted at a temperature above 140° C., and the second hydrothermal pretreatment is conducted at a temperature above 180° C., wherein the first and second hydrothermal pretreatments are each chosen from a liquid hot water treatment, a steam explosion treatment, and a dilute-acid treatment, and combinations thereof;
solubilizing at least 50% of the hemicellulose in the pretreated lignocellulose feedstock as xylo-oligosaccharides;
separating and washing the solids of the pretreated lignocellulose feedstock to thereby eliminate inhibition by soluble xylo-oligosaccharides and phenolic compounds released during pretreating;
forming a slurry of washed pretreated lignocellulose feedstock;
adding a lignin-blocking non-cellulolytic protein to the washed pretreated lignocellulose feedstock slurry to block the lignin retained in the washed pretreated lignocellulose feedstock from binding with a cellulase enzyme in an amount of at least 44 mg lignin-blocking non-cellulolytic protein/g glucan; and
adding a cellulase enzyme to the washed pretreated lignocellulose feedstock slurry in an amount of up to 6 mg cellulase/g glucan.
2. The method of claim 1 , wherein the lignocellulose feedstock comprises a component of corn.
3. The method of claim 1 , wherein the washing step further comprises using water of between about 0.5 to about 15 times the weight of the solids of the pretreated lignocellulose feedstock.
4. The method of claim 3 , wherein the water is recycled water.
5. The method of claim 4 , wherein the washing step further comprises using distillation column bottoms.
6. The method of claim 1 , wherein the washing step is conducted at room temperature.
7. The method of claim 1 , wherein the washing step is conducted at temperatures up to 140° C., wherein the washing step comprises pressure washing.
8. The method of claim 1 , wherein the washing step is conducted at temperatures up to 100° C.
9. The method of claim 1 , wherein the washing step is carried out in a plurality of stages, wherein the washed pretreated lignocellulose feedstock from the second washing stage is contacted counter-currently with wash water from the first washing stage.
10. The method of claim 1 , wherein the pretreating step comprises at least a three-step hydrothermal pretreatment, wherein the first hydrothermal pretreatment is conducted at a temperature above 140° C., and the second hydrothermal pretreatment and third hydrothermal pretreatment are conducted at temperatures above 180° C.
11. The method of claim 1 , wherein the lignin-blocking non-cellulolytic protein comprises bovine serum albumin (BSA).
12. The method of claim 1 , wherein the lignocellulose feedstock is selected from the group consisting of hardwood, corn stover, wheat straw, switchgrass, sugarcane bagasse, sorghum residues, corn pericarp, soybean residue, hay, and softwoods, and combinations thereof.
13. The method of claim 1 , wherein the lignocellulose feedstock comprises at least one of corn stover and corn pericarp.
14. The method of claim 1 , wherein the cellulase enzyme loading is in the range of 3-6 mg cellulase/g glucan and the lignin-blocking non-cellulolytic protein loading is in the range of 44-97 mg lignin-blocking non-cellulolytic protein/g glucan.
15. The method of claim 1 , wherein adding the lignin-blocking non-cellulolytic binding protein to the washed pretreated lignocellulose feedstock is in an amount of at least 50 mg lignin-blocking non-cellulolytic protein/g glucan.
16. The method of claim 1 , wherein during the adding steps the pH of the slurry is maintained in the range of 4.8 to 5.0.
17. The method of claim 1 , wherein said solubilizing is accomplished by pretreatment with liquid hot water under pressure to maintain the hot water in a liquid state.
18. The method of claim 17 , wherein said lignocellulose feedstock has a composition of 30-60% cellulose, 20 to 40% hemicellulose, and 15 to 30% lignin, with the balance extractives and ash to give a total of 100%.
19. The method of claim 18 , wherein said separating and washing the solids of the pretreated lignocellulose feedstock comprises separating and washing with 1 to 20 volumes of water per volume lignocellulose.
20. The method of claim 1 , wherein the first and second hydrothermal pretreatments are liquid hot water treatment.