Method for producing sugar solution
US-9212377-B2 · Dec 15, 2015 · US
US11028455B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11028455-B2 |
| Application number | US-201916594815-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 7, 2019 |
| Priority date | Feb 3, 2015 |
| Publication date | Jun 8, 2021 |
| Grant date | Jun 8, 2021 |
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A method of generating a refined a sugar stream that comprises xylose from a biomass hydrolysis solution, including contacting a biomass hydrolysis solution that includes a population of mixed sugars comprising xylose, an acid, and impurities, with a thermally-phase separable solvent such as a glycol solvent to form an extraction mixture; and separating from said extraction mixture a first stream including the thermally-phase separable solvent, acid, and impurities and a second, refined sugar stream that comprises xylose.
Opening claim text (preview).
The invention claimed is: 1. An extraction mixture comprising: a biomass hydrolysis solution that comprises water, a population of mixed sugars comprising xylose, an acid, and impurities; and a thermally phase separable solvent relative to the water of the biomass hydrolysis solution, wherein the extraction mixture is configured to separate into two phases with an increased temperature, wherein a first phase comprises the water of the biomass hydrolysis solution and a second phase comprises the thermally-phase separable solvent. 2. The extraction mixture of claim 1 , wherein the thermally-phase separable solvent includes 2-butoxyethanol, or 1-propoxy-2-propanol, or any combination thereof. 3. The extraction mixture of claim 1 , further comprising an alkanol. 4. The extraction mixture of claim 3 , wherein said alkanol is hexanol. 5. The extraction mixture of claim 3 , wherein said alkanol is 2-ethylhexanol. 6. The extraction mixture of claim 1 , wherein the thermally-phase separable solvent comprises a 2-butoxyethanol. 7. The extraction mixture of claim 1 , wherein the thermally-phase separable solvent comprises a 1-propoxy-2-propanol. 8. The extraction mixture of claim 1 , wherein the thermally-phase separable solvent is a glycol solvent.
Evaporation of components of the mixture to be separated · CPC title
Cation-exchange · CPC title
Xylose · CPC title
of solutions which are liquid · CPC title
Simulated moving beds · CPC title
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