Method for producing concentrated saccharified solution
US-2015354018-A1 · Dec 10, 2015 · US
US10793927B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10793927-B2 |
| Application number | US-201615550288-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 16, 2016 |
| Priority date | Feb 16, 2015 |
| Publication date | Oct 6, 2020 |
| Grant date | Oct 6, 2020 |
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The invention relates to an improved process for separating lignin and monomeric sugars from a liquor comprising lignin and monomeric sugars in a solvent mixture of water and at least one organic solvent, which employs membrane filtration techniques such as nanofiltration and selective water removal, preferably by permeation through a membrane which is selective for water molecules. The invention further relates to a modular system for executing the process according to the invention. The process and system according to the invention are particularly suitable to be incorporated with pre-treatment of lignocellulosic biomass, in particular by organosolv fractionation or solvolysis.
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The invention claimed is: 1. A process for separating lignin and monomeric sugars from a biomass pre-treatment liquor comprising lignin and monomeric sugars in a solvent mixture comprising water and an organic solvent, the process comprising: (a) subjecting the liquor to nanofiltration over a membrane capable of retaining lignin and permeating monomeric sugars; and (b) subjecting a permeate originating from step (a) to selective water removal to obtain a suspension comprising precipitated monomeric sugars; (c) precipitating lignin from a retentate originating from step (a), and (d) isolating precipitated monomeric sugars from the suspension of step (b). 2. The process according to claim 1 , wherein the liquor is an organosolv liquor or a solvolysis liquor. 3. The process according to claim 1 , wherein the liquor is an organosolv liquor. 4. The process according to claim 2 , wherein the organosolv liquor is obtained by subjecting a lignocellulosic biomass to organosolv prior to step (a). 5. The process according to claim 4 , wherein the organosolv is performed using a ketone organic solvent. 6. The process according to claim 5 , wherein the ketone organic solvent is acetone. 7. The process according to claim 1 , wherein the liquor has a temperature of 100 - 280° C. at the beginning of step (a). 8. The process according to claim 1 , wherein the nanofiltration membrane has a molecular weight cut-off of 200 - 2500 Da. 9. The process according to claim 8 , wherein the nanofiltration membrane has a molecular weight cut-off of 300 - 2000 Da. 10. The process according to claim 1 , wherein the selective water removal is accomplished by selective permeation using a membrane selective for permeation of water molecules. 11. The process according to claim 10 , wherein the selective permeation is accomplished by vapour permeation. 12. The process according to claim 10 , wherein the membrane selective for permeation of water molecules comprises organosilane moieties represented by Si p O q ((CH 2 ) n ) r , wherein n=1−7, p=1.6 −2.4, q =2.5−3.5, and r =0.6 −1.4. 13. The process according to claim 1 , which does not comprise active cooling and/or heating a solution or suspension. 14. The process according to claim 1 , which does not comprise a distillation step.
Biofuels, e.g. bio-diesel · CPC title
Low-molecular-weight derivatives of lignin (high-molecular-weight derivatives of lignin {C08H6/00}) · CPC title
Polyetherketone, polyetheretherketone, or polyaryletherketone · CPC title
Macromolecular compounds derived from lignin, e.g. tannins, humic acids · CPC title
Lignin · CPC title
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