Straw chemical production method based on concentrated acid low-temperature hydrolysis and acid circulation
A chemical and hydrolysis reaction technology, applied in microorganism-based methods, biochemical equipment and methods, microorganisms, etc., can solve the problems of affecting microbial fermentation, high-cost toxic by-products, etc., and achieve the effect of avoiding high costs
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Embodiment 1
[0087] A pretreatment method for corn stover, comprising:
[0088] S1. Dissolve the lignocellulosic biomass with a sulfuric acid solution with a mass fraction of 70% at 30°C to obtain a soluble polysaccharide solution;
[0089] S2. in the soluble polysaccharide solution, add water to dilute to adjust the mass fraction of sulfuric acid in the soluble polysaccharide solution to 20%, and after the hydrolysis reaction, obtain a monosaccharide hydrolyzate; the mass ratio of lignocellulosic biomass to sulfuric acid solution is 1:1; the temperature of the hydrolysis reaction is 60°C; the hydrolysis time is 0.5 hours;
[0090] S3. decolorizing the monosaccharide hydrolyzate to obtain a decolorized monosaccharide hydrolyzate;
[0091] S4. The decolorized monosaccharide hydrolyzate is used to separate the acid and the sugar with a chromatographic separation column filled with a strong acid-resistant cation exchange resin, and the sugar liquid phase and the acid liquid phase are obtaine...
Embodiment 2
[0095] A pretreatment method for corn stover, comprising:
[0096] S1. Dissolve the lignocellulosic biomass with a sulfuric acid solution with a mass fraction of 80% at 60°C to obtain a soluble polysaccharide solution;
[0097] S2. adding water to the soluble polysaccharide solution for dilution to adjust the mass fraction of sulfuric acid in the soluble polysaccharide solution to 35%, and after the hydrolysis reaction, monosaccharide hydrolyzed solution is obtained; the mass ratio of lignocellulosic biomass to sulfuric acid solution is 1:2; the temperature of the hydrolysis reaction is 80°C; the hydrolysis time is 1.5 hours;
[0098] S3. decolorizing the monosaccharide hydrolyzate to obtain a decolorized monosaccharide hydrolyzate;
[0099] S4. The decolorized monosaccharide hydrolyzate is used to separate the acid and the sugar with a chromatographic separation column filled with a strong acid-resistant cation exchange resin, and the sugar liquid phase and the acid liquid p...
Embodiment 3
[0103] A pretreatment method for corn stover, comprising:
[0104] S1. Dissolve the lignocellulosic biomass with a sulfuric acid solution with a mass fraction of 75% at 50°C to obtain a soluble polysaccharide solution;
[0105] S2. adding water to the soluble polysaccharide solution for dilution to adjust the mass fraction of sulfuric acid in the soluble polysaccharide solution to 20-35%, and after the hydrolysis reaction, monosaccharide hydrolyzed solution is obtained; the mass of lignocellulosic biomass and sulfuric acid solution The ratio is 1:1.5; the temperature of the hydrolysis reaction is 75°C; the hydrolysis time is 1 hour;
[0106] S3. decolorizing the monosaccharide hydrolyzate to obtain a decolorized monosaccharide hydrolyzate;
[0107] S4. The decolorized monosaccharide hydrolyzate is used to separate the acid and the sugar with a chromatographic separation column filled with a strong acid-resistant cation exchange resin, and the sugar liquid phase and the acid l...
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