Process for the rapid hydrolysis of high solids biomass
The process for the hydrolysis of ligno-cellulosic biomass comprises the steps of A) Contacting a ligno-cellulosic feedstock, the feedstock comprised of biomass having a dry content and water with at least a portion of a solvent, the solvent comprised of water soluble hydrolyzed species; wherein at least some of the water soluble hydrolyzed species are the same as the water soluble hydrolyzed species obtainable from the hydrolysis of the biomass in the feedstock; B) maintaining the contact between the feedstock of the feedstock stream and the solvent at a temperature in the range of 20° C. to 200° C. for a time in the range of 5 minutes to 72 hours to create a hydrolyzed product from the biomass in the feedstock.
1. A process for the hydrolysis of ligno-cellulosic biomass comprising the steps of
A) contacting a ligno-cellulosic feedstock of a feedstock stream, the ligno-cellulosic feedstock comprised of a ligno-cellulosic biomass having a dry content and water, with at least a portion of a solvent, wherein the dry content comprises cellulose, hemicellulose, and the weight percent of the cellulose in the dry content is greater than 5 weight percent of the dry content, the solvent comprises water soluble hydrolyzed species; wherein at least some of the water soluble hydrolyzed species are the same as the water soluble hydrolyzed species obtainable from the hydrolysis of the cellulose in the feedstock;
B) maintaining the contact between the feedstock of the feedstock stream and the solvent in the presence of a catalyst composition for the hydrolysis of the cellulose comprising at least one cellulase enzyme, at a temperature in the range of 20° C. to 100° C. for a time in the range of 5 minutes to 72 hours to create a hydrolyzed product from the biomass in the feedstock
wherein the process is conducted without adding inorganic acid.
2. The process of claim 1 , wherein the ratio of the weight of the solvent contacted with the feedstock to the weight of the feedstock is in the range of 40:60 to 90:10.
3. The process of claim 2 , wherein the ratio of the weight of the solvent contacted with the feedstock to the weight of the feedstock is greater than 0.8:1.
4. The process of claim 1 , wherein the ratio of the weight of the cellulose plus hydrolysis products of cellulose in the solvent to the weight of the cellulose in the ligno-cellulosic feedstock is greater than the ratio of 1:1.
5. The process of claim 2 , wherein at least a portion of the catalyst composition is contacted with the feedstock before contacting the feedstock with at least a portion of the solvent.
6. The process of claim 4 , wherein at least a portion of the catalyst composition is contacted with the feedstock before contacting the feedstock with at least a portion of the solvent.
7. The process of claim 2 , wherein at least a portion of the catalyst composition is contacted with the feedstock after contacting the feedstock with at least a portion of the solvent.
8. The process of claim 4 , wherein at least a portion of the catalyst composition is contacted with the feedstock after contacting the feedstock with at least a portion of the solvent.
9. The process of claim 2 , wherein at least a portion of the catalyst composition is contacted with the feedstock simultaneously with contacting the feedstock with at least a portion of the solvent.
10. The process of claim 4 , wherein at least a portion of the catalyst composition is contacted with the feedstock simultaneously with contacting the feedstock with at least a portion of the solvent.
11. The process of claim 2 , wherein the ratio of the biomass to water of the feedstock is greater than the ratio of 1:0.9.