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Method for hydrolyzing vegetable fibre by solid acid

A plant fiber and solid acid technology, which is applied in sugar production, food science, sugar production, etc., can solve the problems of high corrosion resistance requirements for equipment, high cost of enzyme preparations, loss of concentrated acid in catalysts, etc., and overcome economical problems. Low efficiency, low corrosion requirements, and the effect of reducing production costs

Inactive Publication Date: 2010-07-28
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The traditional acid hydrolysis process is concentrated acid hydrolysis and dilute acid hydrolysis. Dilute acid hydrolysis has high requirements on the process conditions, excessive energy consumption in the reaction, and low sugar conversion rate (about 25%). A large number of harmful intermediate products (such as furfural, organic acids) that inhibit microbial growth and other shortcomings; and concentrated acid hydrolysis, although the conversion rate of sugar is relatively high (90% or more), but the loss of concentrated acid of the catalyst is too serious, and the acid consumption is relatively large. The corrosion resistance requirements of the equipment are high, and the production cost is high; although the conversion rate of cellulase to the hydrolysis of cellulose is high, the cost of enzyme preparation is high, the pretreatment equipment is large, the operation cost is high, and the reaction cycle is relatively short. Long; ultra-low acid hydrolysis and supercritical water hydrolysis need to react under harsh conditions of high temperature and high pressure, the operation and process are difficult to control, and degradation products are easily produced, which affects subsequent fermentation

Method used

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  • Method for hydrolyzing vegetable fibre by solid acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] OCC fragments and carbon-based sulfonic acid catalysts were added to water for miscibility according to the mass percentage of water (as shown in Table 1), and reacted at different temperatures for 12 hours. The hydrolyzate is filtered, part of the resulting filtrate is used for sugar production analysis, part of it is used as a fermentation substrate, and the filter residue is used for recycling.

[0021] Table 1 Comparison of the hydrolysis effect of carbon-based solid sulfonic acid on OCC at different temperatures

[0022]

[0023] Table 2 Effect of reuse times on hydrolysis effect

[0024]

[0025] As can be seen from Table 1, with the change of temperature, the sugar yield increases first and then decreases. When the temperature is 150°C, the sugar yield reaches a maximum value of 22.16%, which is comparable to that of traditional dilute sulfuric acid hydrolysis (the maximum sugar yield is 25%). The comparison is very close; when the temperature is 180°C, th...

Embodiment 2

[0027] OCC fragments and carbon-based sulfonic acid catalysts were added to water for miscibility according to the mass percentage of water (as shown in Table 3), and reacted at 150° C. for different times. The hydrolyzate is filtered, part of the obtained filtrate is used for sugar production analysis, part is used for the fermentation of the hydrolyzate, and the filter residue is used for recycling.

[0028] Table 3 Comparison of the hydrolysis effect of carbon-based solid sulfonic acid on OCC at different times

[0029]

[0030] Table 4 Effect of reuse times on hydrolysis effect

[0031]

[0032] It can be seen from Table 3 that with the change of time, the sugar yield increased first and then decreased. At 8 hours, the sugar yield reached a maximum of 24.07%, and then from 8 to 12 hours, the sugar yield decreased by 7.61%. , indicating that in a mild hydrothermal environment, the catalyst has a high selectivity for sugar, and the sugar is further converted into by-p...

Embodiment 3

[0034] OCC fragments were added to water for miscibility according to the mass percentage of water (as shown in Table 5), carbon-based solid sulfonic acid catalysts were added to water for miscibility according to different concentrations, and reacted at 150°C for 8 hours. The hydrolyzate is filtered, part of the obtained filtrate is used for sugar production analysis, part is used for the fermentation of the hydrolyzate, and the filter residue is used for recycling.

[0035] Table 5 Comparison of the hydrolysis effects of different concentrations of carbon-based solid sulfonic acid on OCC

[0036]

[0037] Table 6 Effect of reuse times of different carbon-based solid sulfonic acid on hydrolysis effect

[0038]

[0039] It can be seen from Table 5 that with the change of the amount of catalyst added, the sugar yield increased first and then decreased. When the amount of catalyst added was 1.2%, the sugar yield reached a maximum value of 26.44%. The decrease in yield was...

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Abstract

The invention discloses a method for hydrolyzing vegetable fibre by solid acid, comprising the following steps: (1) adding smashed vegetable fibre and a solid-acid catalyst into water, mixing and dissolving; (2) carrying out hydro-thermal reaction at the temperature of 140-180DEG C for 6-10 hours after the smashed vegetable fibre and the solid-acid catalyst are evenly mixed and dissolved, and obtaining hydrolysate after the reaction; and (3) filtering the hydrolysate so as to separate target objects and the solid-acid catalyst, drying filter residues so as to be directly reused, and regulating the pH value of filter liquor to be within 6-8. The invention adopts solid sulfoacid with better hydrothermal stability and larger acid value to replace liquid acid, realizes the hydrolyzation of the cellulose under the moderate condition and solves the problem that the tradition catalyst is difficult to be separated from products; and after separation, the catalyst can be recycled, thereby avoiding lower economic benefit and acid contamination caused by the loss of liquid-acid catalysts.

Description

technical field [0001] The invention belongs to a method for preparing sugar by acid hydrolysis of plant fiber, and in particular relates to a method for hydrolyzing plant fiber with solid sulfonic acid. Background technique [0002] The use of biomass resources to produce liquid fuels and chemical products is to hydrolyze cellulose into sugars, such as oligosaccharides, monosaccharides, etc., and then use microorganisms (Candida, Saccharomyces cerevisiae, etc.) to produce liquid fuels and chemical products. Cellulose hydrolysis and saccharification methods mainly include dilute acid method, concentrated acid method, enzymatic method, and ultra-low acid hydrolysis and supercritical water hydrolysis, which are more popular in research. [0003] The traditional acid hydrolysis process is concentrated acid hydrolysis and dilute acid hydrolysis. Dilute acid hydrolysis has high requirements on the process conditions, excessive energy consumption in the reaction, and low sugar con...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C13K13/00
Inventor 万金泉王艳赵银中马邕文
Owner SOUTH CHINA UNIV OF TECH
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