Method for extracting xylose from poly pentose acidolysis liquid
A technology of acid hydrolysis solution and extraction method of polypentose, which is applied in the direction of chemical instruments and methods, monosaccharides, sugar derivatives, etc., can solve the problems of "three wastes" discharge polluting the environment, inability to adapt, and large acid and alkali consumption, etc. Achieve the effects of cost reduction, low cost, and less acid and alkali usage
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Embodiment 1
[0026] Using corn cob as raw material, after removing impurities, rinsing, washing with hot water, washing with dilute sulfuric acid, hydrolyzing with sulfuric acid to obtain polypentose acid hydrolysis solution; its main components are xylose and a small amount of glucose, arabinose, etc. (Note: the following implementation The polypentose acid hydrolyzate in the example is the same as this).
[0027] 1. Heat 45L polypentose acid solution to 80°C, add 700g of light calcium carbonate, adjust pH=3.32, neutralize and remove part of the sulfate radical; keep warm at 80°C for 1 hour, filter, then add 220g Waste carbon (activated carbon used for decolorization of the previous acidolysis solution) was pre-decolorized and kept for 0.5h;
[0028] After decolorization, the sulfate radical content in the acidolysis solution is 1432mg / L, and the calcium ion content is 580mg / L;
[0029] 2. Then add 225g of powdered activated carbon and keep it warm for 0.5h at a temperature of 55°C; the ...
Embodiment 2
[0035] 1. Heat 45L polypentose acid solution to 80°C, add 700g of light calcium carbonate, adjust pH=3.24, remove part of the sulfate radical; keep warm at 80°C for 1 hour, filter, then add 225g of waste carbon ( The activated carbon used in the decolorization of the previous acidolysis solution) was pre-decolorized and kept for 0.5h;
[0036] After decolorization, the sulfate radical content in the acidolysis solution is 1495 mg / L, and the calcium ion content is 520 mg / L.
[0037] 2. Then add 225g of powdered activated carbon and keep it warm for 0.5h at a temperature of 55°C; the light transmittance of the acid solution after decolorization is 78%;
[0038]3. Perform ion exchange on the above-mentioned decolorized acid solution, first pass through the strong acid type cationic resin 001*7, so that the iron ion content in the acid solution is 2 mg / L; then pass through the weak base type anion resin D301, make the acid solution Sulfate content is 18mg / L;
[0039] Then concen...
Embodiment 3
[0043] 1. Heat 45L polypentose acid solution to 80°C, add 650g light calcium carbonate, adjust pH=3.14, remove part of the sulfate radical; keep warm at 80°C for 1 hour, filter, then add 225g waste carbon (The activated carbon used in the decolorization of the previous acidolysis solution) was pre-decolorized and kept warm for 0.5h;
[0044] After decolorization, the sulfate radical content in the acidolysis solution is 1452 mg / L, and the calcium ion content is 480 mg / L.
[0045] 2. Then add 225g of powdered activated carbon and keep it warm for 0.5h at a temperature of 55°C; the light transmittance of the acid solution after decolorization is 75%;
[0046] 3. Perform ion exchange on the decolorized acid solution, first pass through the strong acid cationic resin HZ-016, so that the iron ion content in the acid solution is 2mg / L; then pass through the weak base anion resin D315, make the acid solution Sulfate content is 14mg / L;
[0047] Then concentrated by reverse osmosis m...
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