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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

Pending Publication Date: 2022-05-27
SICHUAN UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] In order to solve the technical problems of high cost of lignocellulosic biomass pretreatment in the prior art or many toxic by-products in the pretreatment process affecting subsequent microbial fermentation, the embodiment of the present invention provides a lignocellulosic biomass pretreatment Treatment methods and chemical preparation methods

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  • Straw chemical production method based on concentrated acid low-temperature hydrolysis and acid circulation

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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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Abstract

The embodiment of the invention provides a pretreatment method of lignocellulose biomass and a chemical preparation method, and aims to solve the technical problem that subsequent microbial fermentation is affected by high cost or many toxic and side products in the pretreatment process of the lignocellulose biomass in the prior art. Comprising the following steps: S1, dissolving lignocellulose biomass with a sulfuric acid solution with the mass fraction of 70-80% at 30-60 DEG C to obtain a soluble polysaccharide solution; s2, water is added into the soluble polysaccharide solution for dilution so as to adjust the mass fraction of sulfuric acid in the soluble polysaccharide solution to 20-35%, and monosaccharide hydrolysate is obtained after hydrolysis reaction. According to the embodiment of the invention, the defect that the subsequent microbial fermentation is influenced by high cost or more toxic and side products in the pretreatment process in the pretreatment of lignocellulose biomass in the prior art is overcome.

Description

technical field [0001] The invention relates to a pretreatment method for lignocellulosic biomass and a chemical preparation method. Background technique [0002] Replacing traditional fossil resources with biomass resources and realizing resource substitution is the key to solving problems such as environmental pollution and resource shortages and achieving sustainable social and economic development. Lignocellulosic biomass represented by straw with huge reserves and annual output is the main biomass resource on earth. The development of technologies for producing bioenergy and important small molecule platform compounds using lignocellulosic biomass as raw materials is the basis for realizing resource substitution. [0003] Lignocellulosic biomass such as straw contains three major components: cellulose, hemicellulose and lignin, of which cellulose and hemicellulose account for 60%-70%, and after hydrolysis, monosaccharides such as glucose and xylose are generated , usi...

Claims

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Application Information

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IPC IPC(8): C12P7/10C12P7/18C12R1/865
CPCC12P7/10C12P7/18C12P2201/00C12P2203/00Y02E50/10
Inventor 汤岳琴吴晓磊柳泽深孙照勇谢采芸
Owner SICHUAN UNIV
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