Starch-derived clathrate-forming compositions
US-11959114-B2 · Apr 16, 2024 · US
US9988658B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9988658-B2 |
| Application number | US-201414917943-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 15, 2014 |
| Priority date | Oct 18, 2013 |
| Publication date | Jun 5, 2018 |
| Grant date | Jun 5, 2018 |
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The present invention is directed to a process for the hydrolysis of biomass as well as the saccharide-containing permeate product and the protein-containing product produced by this process. In a further aspect, the present invention is directed to a process for the production of organic compounds from the saccharide-containing product. In an additional aspect the present invention is directed to the use of the protein-containing product for the production of a fermentation medium.
Opening claim text (preview).
What is claimed is: 1. A process for the hydrolysis of biomass comprising: a) Contacting the biomass with an enzyme-composition containing at least one enzyme selected from the class of hydrolases in a vessel; b) Eliminating at least part of said biomass; c) Subjecting said at least part of said biomass to a filtration and removing the permeate; and d) Backfeeding of at least part of the filtrated biomass to the vessel; wherein step b) is carried out in an outer circuit; wherein step c) is carried out in an inner circuit; wherein said outer circuit and said inner circuit are different; wherein the outer circuit is in closer proximity to step a) than the inner circuit; wherein filtration is carried out by use of at least one filtration module comprising at least one ceramic membrane; wherein dry matter content of the biomass is from 5 to 40 wt.-%; wherein each circuit is equipped with a pump; and wherein at least two of steps a) to d) are carried out simultaneously; and wherein after step d), the filtrated biomass that is not backfed to the vessel is circulated back to the at least one filtration module. 2. The process according to claim 1 , wherein the enzyme-composition contains cellulases, hemicellulases and/or pectinases. 3. The process according to claim 2 , wherein the enzyme-composition further contains at least one enzyme selected from pectinmethylesterases, rhamnogalacturonases, 1,3-/1,6-beta-D-glucanases and xylanases. 4. The process according to claim 1 , wherein the biomass is selected from cellulose, hemicellulose and/or lignin-containing biomass. 5. The process according to claim 4 , wherein the biomass is selected from sugar-beet, sugar-cane, straw, corn, wood, oilseed and mixtures thereof. 6. The process according to claim 1 , further comprising: e) adding an amount of liquid corresponding to the amount removed by filtration according to step c). 7. The process according to claim 6 , further comprising: f) Adding an amount of fresh biomass. 8. The process according to claim 7 , wherein steps b) to e) or b) to f) are repeated at least once. 9. The process according to claim 6 , wherein each of steps a) to e) are carried out simultaneously. 10. The process according to claim 1 , wherein dry matter content of the biomass is from 15 to 30 wt.-%. 11. The process according to claim 1 , wherein dry matter content of the biomass is 22 wt.-%.
produced by the action of a carbohydrase {(EC 3.2.x)}, e.g. by alpha-amylase {, e.g. by cellulase, hemicellulase} · CPC title
Monosaccharides (2-ketogulonic acid C12P7/60) · CPC title
using membranes, e.g. osmosis, ultrafiltration (electrodialysis C13B20/18) · CPC title
obtained by saccharification of cellulosic materials (manufacture of fodder A23K10/32) · CPC title
Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms · CPC title
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