Starch-derived clathrate-forming compositions
US-11959114-B2 · Apr 16, 2024 · US
US10087476B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10087476-B2 |
| Application number | US-201415034867-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 4, 2014 |
| Priority date | Dec 6, 2013 |
| Publication date | Oct 2, 2018 |
| Grant date | Oct 2, 2018 |
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A process for hydrolyzing a pretreated lignocellulosic feedstock is disclosed herein. The process comprises hydrolyzing the pretreated lignocellulosic feedstock with an enzyme mixture comprising at least cellulase enzymes to produce a hydrolyzed slurry comprising glucose and lignin solids. The hydrolyzing is conducted in the presence of a polymer, such as an aliphatic polyether. A solids-liquid separation is conducted to recover lignin solids from a process stream comprising the lignin solids and the polymer. A process stream is then obtained comprising recovered lignin solids resulting from the solids-liquid separation. Also provided are processes for recovering the polymer from the lignin solids and/or from solution.
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The invention claimed is: 1. A process for hydrolyzing a pretreated lignocellulosic feedstock and recovering lignin solids comprising: (i) hydrolyzing the pretreated lignocellulosic feedstock with an enzyme mixture comprising at least cellulase enzymes to produce a hydrolyzed slurry comprising glucose and lignin solids, said hydrolyzing being conducted in the presence of a polymer that binds or associates with the lignin solids; (ii) conducting a solids-liquid separation to recover lignin solids from a process stream comprising the lignin solids and the polymer; (iii) obtaining a process stream comprising recovered lignin solids resulting from the solids-liquid separation of step (ii), and (iv) recovering at least a portion of the polymer from the recovered lignin solids of step (iii) comprising adding a chemical extractant selected from alcohol or alkali for extracting the at least a portion of the polymer, and further recovering the chemical extractant and recycling both the recovered polymer and the chemical extractant in the process. 2. The process of claim 1 , wherein the polymer that binds or associates with the lignin solids is a non-ionic polymer. 3. The process of claim 2 , wherein the non-ionic polymer is a water-soluble polymer. 4. The process of claim 3 , wherein the water-soluble polymer is a polyether or a surfactant comprising a polyether. 5. The process of claim 4 , wherein the polyether is paraformaldehyde, polyethylene glycol, polypropylene glycol, polytetramethylene glycol or a substituted aliphatic polyether. 6. The process of claim 1 , wherein the polymer is added at a concentration of 2% to 20% by weight based on the weight of undissolved pretreated solids. 7. The process of claim 1 , wherein in the step of conducting a solids-liquid separation to recover the lignin solids from a process stream comprising the lignin solids and the polymer, at least 50 wt % of the process stream is fed to the solids-liquid separation. 8. The process of claim 1 , wherein the solids-liquid separation is filtration. 9. The process of claim 1 , wherein the process stream of step (ii) is a fermentation broth or a still bottoms stream. 10. The process of claim 1 , wherein the lignin solids in the process stream of step (ii) comprises dissolved lignin. 11. The process of claim 1 , wherein the chemical extractant in step (iv) is an alcohol. 12. The process of claim 11 , wherein the process stream comprising the lignin solids and the polymer is heat treated, treated with lime, or a combination thereof, prior to recovery of the polymer. 13. The process of claim 1 , further comprising recovering at least another portion of the polymer from solution of an aqueous process stream, said aqueous process stream obtained from the solids-liquid separation in step (ii). 14. The process of claim 1 , wherein conducting the solids-liquid separation comprises filtering the process stream when the process stream is at a temperature between 55° C. and 200° C. 15. The process of claim 1 , wherein the polymer comprises polyethylene glycol. 16. The process of claim 11 , wherein the alcohol is ethanol. 17. The process of claim 11 , wherein the alcohol is methanol. 18. The process of claim 14 , wherein the temperature is at least 80° C. and less than 200° C. 19. A process for producing an alcohol from a lignocellulosic feedstock comprising: hydrolyzing a pretreated lignocellulosic feedstock with an enzyme mixture comprising at least cellulase enzymes to produce a hydrolyzed slurry comprising glucose and lignin solids, said hydrolyzing being conducted in the presence of a polymer that binds or associates with the lignin solids; (ii) fermenting the glucose to produce a fermentation beer comprising the alcohol and then concentrating the alcohol; (iii) conducting a solids-liquid separation to recover the lignin solids from a process stream comprising the lignin solids and the polymer; (iv) obtaining a process stream comprising recovered lignin solids resulting from the solids-liquid separation of step (iii), and (v) recovering at least a portion of the polymer from the recovered lignin solids of step (iii) comprising adding a chemical extractant selected from an alcohol or alkali for extracting the at least a portion of the polymer, further recovering the chemical extractant and recycling both the recovered polymer and the chemical extractant in the process. 20. The process of claim 19 , wherein the process stream comprising the lignin solids and the polymer in step (iii) is the hydrolyzed slurry, the fermentation beer, a still bottoms stream remaining from concentrating the alcohol, or a combination thereof.
Monosaccharides (2-ketogulonic acid C12P7/60) · CPC title
with acids, acid salts or acid anhydrides {(D21C3/003 and D21C3/222 take precedence)} · CPC title
Macromolecular compounds derived from lignin, e.g. tannins, humic acids · CPC title
Cross-Sectional Technologies · mapped topic
Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for (volatile compounds obtained by decomposition of spent liquors in order to regenerate them D21C11/125; compounds obtained by fractionating the liquors in order to regenerate them D21C11/0042) · CPC title
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