Method for extracting xylose from poly pentose acidolysis liquid
A technology of polypentose acid hydrolyzate and polypentose acid, which is applied in chemical instruments and methods, monosaccharides, sugar derivatives, etc., can solve the problem of "three wastes" discharge pollution to the environment, large consumption of acid and alkali, and inability to adapt and other problems, to achieve the effect of reducing costs, using less acid and alkali, and lowering costs
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Embodiment 1
[0026] Using corncob as raw material, after removing impurities, rinsing, washing with hot water, and washing with dilute sulfuric acid, it is hydrolyzed with sulfuric acid to obtain polypentose acid hydrolysate; its main components are xylose and a small amount of glucose, arabinose, etc. (Note: the following implementation The polypentose acid hydrolysate in the example is the same).
[0027] 1. Heat 45L polypentose acid hydrolysate to 80℃, add 700g light calcium carbonate, adjust pH=3.32, neutralize and remove some sulfate radicals; after keeping at 80℃ for 1h, filter, then add 220g Pre-decolorization of waste carbon (activated carbon used for decolorization of the previous acid hydrolysis solution) and heat preservation for 0.5h;
[0028] After decolorization, the sulfate content in the acid hydrolysis solution is 1432mg / L, and the calcium ion content is 580mg / L;
[0029] 2. Then add 225g powdered activated carbon and keep it at 55°C for 0.5h; the light transmittance of the acid...
Embodiment 2
[0035] 1. Heat 45L polypentose acid hydrolysate to 80℃, add 700g light calcium carbonate, adjust pH=3.24, remove part of sulfate radical; keep it at 80℃ for 1h, filter, then add 225g waste charcoal ( Activated carbon used for decolorization of the previous acid hydrolysis solution) is pre-decolorized and kept for 0.5h;
[0036] After decolorization, the sulfate content in the acid hydrolysis solution is 1495mg / L, and the calcium ion content is 520mg / L.
[0037] 2. Then add 225g powdered activated carbon and keep it at 55°C for 0.5h; the light transmittance of the acid hydrolyzate after decolorization is 78%;
[0038] 3. Perform ion exchange on the above-mentioned decolorized acid hydrolysate, first pass the strong acid type cationic resin 001*7 to make the iron ion content in the acid hydrolyzate 2mg / L; then pass the weak base anion resin D301 to make the acid hydrolysate The sulfate content is 18mg / L;
[0039] Then it is concentrated by a reverse osmosis membrane (standard desalinat...
Embodiment 3
[0043] 1. Heat 45L polypentose acid hydrolysate to 80℃, add 650g light calcium carbonate, adjust pH=3.14, remove part of sulfate radical; after keeping it at 80℃ for 1h, filter, then add 225g waste charcoal (Activated carbon used for the decolorization of the previous acid hydrolysis solution) Pre-decolorization and heat preservation for 0.5h;
[0044] After decolorization, the sulfate content in the acid hydrolysis solution was 1452 mg / L, and the calcium ion content was 480 mg / L.
[0045] 2. Then add 225g powdered activated carbon and keep it at 55°C for 0.5h; the light transmittance of the acid hydrolyzate after decolorization is 75%;
[0046] 3. Perform ion exchange on the above-mentioned decolorized acid hydrolysis solution, first pass the strong acid cation resin HZ-016 to make the iron ion content in the acid hydrolysis solution 2mg / L; then pass the weak base anion resin D315 to make the acid hydrolysis solution The sulfate content is 14mg / L;
[0047] Then it is concentrated by...
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