Method for producing concentrated saccharified solution
US-2015354018-A1 · Dec 10, 2015 · US
US9441280B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9441280-B2 |
| Application number | US-201414909817-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 15, 2014 |
| Priority date | Sep 5, 2013 |
| Publication date | Sep 13, 2016 |
| Grant date | Sep 13, 2016 |
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A chromatographic method for separating a sugar from a sugar-containing liquid feed mixture by: contacting the liquid feed mixture with a stratum of cation exchange resin comprising a crosslinked copolymer matrix functionalized with sulfonic acid groups, and recovering a first product stream from the stratum that has a higher purity of the sugar than present in the liquid feed mixture. The method is characterized by the stratum of cation exchange resin including: i) at least 80 wt % of cation exchange resin including alkaline earth counter ions, and ii) at least 5 wt % of cation exchange resin including alkali earth counter ions.
Opening claim text (preview).
The invention claimed is: 1. A chromatographic method for separating a first sugar from a sugar-containing liquid feed mixture by: contacting the liquid feed mixture with a stratum of cation exchange resins comprising a crosslinked copolymer matrix functionalized with sulfonic acid groups, and recovering a first product stream from the stratum that has a higher purity of the first sugar than present in the liquid feed mixture, wherein the method is characterized by the stratum of cation exchange resins comprising: i) at least 75 wt of cation exchange resin comprising alkaline earth counter ions, and ii) at least 5 wt % of cation exchange resin comprising alkali metal counter ions. 2. The method of claim 1 wherein the alkaline earth counter ions are selected from at least one of: calcium, strontium and barium. 3. The method of claim 1 wherein the alkali metal counter ions are selected from a least of: lithium, sodium and potassium. 4. The method of claim 1 wherein the crosslinked copolymer matrix is derived from a monomer mixture comprising styrene and divinylbenzene. 5. The method of claim 1 wherein the cation exchange resins are provided in bead form having a particle size of from 100 to 1000 um. 6. The method of claim 1 wherein the stratum of cation exchange resins comprises: i) from 80 to 95 wt % of cation exchange resin comprising alkaline earth counter ions, and ii) from 5 to 20 wt % of cation exchange resin comprising alkali metal counter ions. 7. The method of claim 1 wherein the sugar-containing liquid feed mixture includes at a least two different types of sugar and wherein the first sugar is recovered in the first product stream, and the method further includes the step of recovering a second product stream wherein: i) the first product stream has a higher purity of the first sugar than the second product stream, and ii) the second product stream has a higher purity of the second sugar than the first product stream. 8. The method of claim 7 wherein the first and second sugars are selected from: glucose, fructose, lactose, sucrose, lactose, sucrose, maltose, glucose, galactose, sorbose, xylose, mannose, isomaltose, stachyose, arabinose, tagatose, and raffinose.
obtained by reactions only involving unsaturated carbon-to-carbon bonds · CPC title
in the strongly acidic form · CPC title
Purifying · CPC title
Separation of sugars provided for in subclass C13K (C13K3/00 takes precedence) · CPC title
Cation exchangers for chromatographic processes · CPC title
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