Hydrolyzing method of cellulose and hemicellulose in waste plant

A technology of waste plants and hemicellulose, applied in the field of renewable resources - waste plant utilization, can solve the problems of low conversion rate, high production cost, low production efficiency, etc., to avoid deterioration of working environment, speed up hydrolysis, expand The effect of size

Active Publication Date: 2013-01-30
张浪
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, many departments in our country are developing and utilizing renewable resources—especially waste plants—to produce fuel ethanol, and some large enterprises are conducting trial production, but the problem in the existing technology is the cellulose and hemifibers in waste plants The process cost of converting ketones into glucose and xylose is too high, which affects the production cost of the entire fuel ethanol, so that it cannot be put into mass production
[0003] Most of the methods of prior art experiments and trial production use dilute sulfuric acid to hydrolyze hemicellulose to obtain xylose, and then add cellulase to the residue containing cellulose and lignin to hydrolyze cellulose (also known as enzymatic process) , but under the current conditions, the enzymatic process requires very harsh process conditions, and expensive cellulase preparations must be purchased, so the production cost is very high
[0004] Another method of hydrolyzing cellulose, which is also the most classic method, is to hydrolyze cellulose and hemicellulose with concentrated sulfuric acid. This method is simple and technically reliable. However, due to the similar molecular weights of glucose and sulfuric acid, it is impossible to recover sulfuric acid with a diffusion dialyzer. , instead of producing polysaccharides first and then separating them, the production efficiency of this method is very low, so it cannot be used in production
[0005] Recently, a dilute acid high-temperature hydrolysis method has been developed, but it is found that the converted glucose decomposes in large quantities at high temperature, so the conversion rate is not high

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] 1. Take sawdust as the waste plant of this embodiment 1, first carry out delignification treatment: take 454g of sawdust, add 10 times the volume of ethanol, then keep it under the air pressure of 1.2-1.35MPa for 2 hours, dissolve the woodiness therein lignin, then filtered, and the remaining sawdust was weighed, which was 312g, and 142g lignin was removed. The amount of ethanol used in this step is usually more than 6 times the plant weight.

[0020] 2. Take 20g of sawdust from the lignin-removed sawdust, add hydrochloric acid with a concentration of 20% by weight to the sawdust, the amount of hydrochloric acid is based on submerging the sawdust, and then microwave for 1 hour at a temperature of 110°C , When heating, the maximum temperature cannot exceed 110°C.

[0021] 3. Pour the microwave-treated sawdust and hydrochloric acid obtained in step 2 into a high-pressure reactor, heat up to 130° C. under an air pressure of 1.2-1.35 MPa, and maintain the temperature and p...

Embodiment 2

[0026] 1. Take sawdust as the waste plant in Example 2, and first perform delignification treatment: take 800 g of sawdust, add 10 times the volume of ethanol, and then keep it under an air pressure of 1.2-1.35 MPa for 2 hours to dissolve the woodiness therein. lignin, then filtered, and the remaining sawdust was weighed, which was 560g, and 240g lignin was removed. The amount of ethanol used in this step is usually more than 6 times the plant weight.

[0027] 2. Take 20g of sawdust from the lignin-removed sawdust, and add hydrochloric acid with a concentration of 15% by weight to the sawdust. The amount of hydrochloric acid is based on submerging the sawdust, and then microwave for 1.5 hours at a temperature of 100°C. , When heating, the maximum temperature cannot exceed 110°C.

[0028] 3. Pour the microwave-treated sawdust and hydrochloric acid obtained in step 2 into a high-pressure reactor, raise the temperature to 140° C. under an air pressure of 1.2-1.35 MPa, and mainta...

Embodiment 3

[0033] 1. Break 20g of straw with a grinder, and the length of the straw is less than 1mm;

[0034] 2. Add hydrochloric acid with a percentage by weight of 18%, the amount of hydrochloric acid is based on submerging the broken rice straw, and then heat with microwave for 2 hours at a heating temperature of 105°C (the maximum heating temperature is 110°C);

[0035] 3. Add the microwave-treated substance in step 2 into a high-pressure reactor, and hydrolyze it for 1.5 hours at an air pressure of 1.2-1.35MPa and a temperature of 135°C;

[0036] 4. Filter the substance obtained in step 3 according to the method in Example 1, separate the hydrolyzate and residue, and obtain the hydrolyzate.

[0037] Check the content of monosaccharides in the hydrolyzed solution according to the Pei's method of the prior art, as can be seen, through the hydrolysis method of the present embodiment, 63% of the cellulose and hemicellulose in the rice straw are converted into monosaccharides (glucose a...

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Abstract

A hydrolyzing method of cellulose and hemicellulose in waste plant, comprises the following steps: adding hydrochloric acid in 15-20wt% concentration into finely divided waste plant in a sufficient amount to flood the waste plant, heating the mixture by microwave for 1-2h at the temperature of 100-110 DEG C, putting the waste plant and hydrochloric acid processed by microwave into a high pressurereaction vessel to maintain for 1-2h at the air pressure of 1.2-1.35MPa and the temperature of 120-140 DEG C to hydrolyze, then filtering the prepared substance, separating hydrolysate and residue toobtain a hydrolysate. The obtained hydrolysate is subject to hydrochloric acid recycling to separate hydrochloric acid and monosaccharide liquid, the monosaccharide liquid can be further used for theproduction of fuel ethanol. The hydrolyzing method has the advantages of low cost, simple technology, convenient for the recovery of hydrochloric acid, and preventing the deterioration of working environment.

Description

technical field [0001] The invention relates to the field of renewable resources—the utilization of waste plants, in particular to a method for hydrolyzing various waste plants containing cellulose and hemicellulose into glucose and xylose. Background technique [0002] At present, many departments in our country are developing and utilizing renewable resources—especially waste plants—to produce fuel ethanol, and some large enterprises are conducting trial production, but the problem in the existing technology is the cellulose and hemifibers in waste plants The cost of the process of turning cellulose into glucose and xylose is too high, which affects the production cost of the entire fuel ethanol, so that it cannot be put into mass production. [0003] Most of the methods of prior art experiments and trial production use dilute sulfuric acid to hydrolyze hemicellulose to obtain xylose, and then add cellulase to the residue containing cellulose and lignin to hydrolyze cellul...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C12P7/10C13K1/02C13K13/00
CPCY02E50/10
Inventor 张羡信孙维民张浪张欢
Owner 张浪
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