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Utilizing amphoteric surfactant to promote enzymatic hydrolysis of lignocellulose and cooling method for recovering cellulase

A technology of lignocellulosic enzymes and surfactants, applied in the direction of biochemical equipment and methods, enzymes, enzymes, etc., can solve the problems of easy inactivation of cellulase and affect the activity of enzyme systems, and achieve simple operation and avoid high temperature loss The effect of liveliness and low energy consumption

Active Publication Date: 2020-11-24
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] However, the temperature-sensitive polymer-loaded cellulase still faces some problems: 1. The cellulase is easily inactivated when the cellulase is recovered at a higher temperature; 2. When the cellulase is grafted on the polymer, the fiber Sulfase is easily inactivated. 3. Cellulase is a multi-component enzyme system, and its grafting reaction and recovery rate are not the same. Recovery affects the activity of the enzyme system.

Method used

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  • Utilizing amphoteric surfactant to promote enzymatic hydrolysis of lignocellulose and cooling method for recovering cellulase
  • Utilizing amphoteric surfactant to promote enzymatic hydrolysis of lignocellulose and cooling method for recovering cellulase
  • Utilizing amphoteric surfactant to promote enzymatic hydrolysis of lignocellulose and cooling method for recovering cellulase

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Experimental program
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Effect test

Embodiment 1

[0030] Such as figure 2As shown, take 100 parts by mass of microcrystalline cellulose, add it to 5000 parts by mass of acetic acid-sodium acetate buffer solution with a pH of 4.8 and an ionic strength of 50 mmol / L, add 50 parts by mass of SB3-16, and then add 10 FPU / g to The cellulase of the microcrystalline cellulose mass meter was reacted at 50°C for 48 hours. After the reaction, centrifuged to obtain the enzymolysis liquid, lowered the temperature of the enzymolysis liquid to 0°C, and centrifuged when a large amount of precipitation appeared in the solution , then add the obtained solid to the same sample as the initial enzymatic hydrolysis conditions (substrate and buffer) and enzymatically hydrolyze it again for 48h (without supplementing cellulase and amphoteric surfactant), and measure twice by biosensor analyzer The enzymatically hydrolyzed glucose content, the statistical results are shown in Table 1.

Embodiment 2

[0032] Such as figure 2 As shown, take 100 parts by mass of Eucalyptus-DA, add it to 5000 parts by mass of citric acid-sodium citrate buffer solution with a pH of 5.0 and an ionic strength of 25mmol / L, add 50 parts by mass of SB3-16, and then add 5FPU / g Cellulase, counted as dextran in the substrate, reacted at 50°C for 48 hours. After the reaction, centrifuged to obtain the enzymolysis liquid, lower the temperature of the enzymolysis liquid to 0°C, and when a large amount of precipitation appeared in the solution Carry out centrifugation, then add the obtained solid to the same sample as the initial enzymatic hydrolysis conditions (substrate and buffer) and enzymatic hydrolyze again for 48h (without supplementing cellulase and amphoteric surfactant), and pass through the biosensing analyzer The glucose content of the two enzymatic hydrolysis was measured, and the statistical results are shown in Table 1.

Embodiment 3

[0034] Such as figure 2 As shown, take 250 parts by mass of pine wood-SPORL, add it to 5000 parts by mass of a phosphate buffer solution with a pH of 5.5 and an ionic strength of 100 mmol / L, and add 100 parts by mass of C 12 PPS, then add 10FPU / g cellulase based on glucan in the substrate, react at 50°C for 72h, after the reaction, centrifuge to obtain the enzymolysis liquid, reduce the temperature of the enzymolysis liquid to 0°C, and wait When there is a large amount of precipitation in the solution, perform centrifugation, and then add the obtained solid to the same sample as the initial enzymatic hydrolysis conditions (substrate and buffer) for another 72 hours of enzymatic hydrolysis (without supplementing cellulase and amphoteric surfactant), The glucose content of the two enzymatic hydrolysis was measured by a biosensor analyzer, and the statistical results are shown in Table 1.

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Abstract

The invention discloses a method for promoting enzymatic hydrolysis of lignocelluloses and cooling and recycling cellulase by the aid of ampholytic surfactants. The method includes adding the lignocelluloses into buffer solution, adding the ampholytic surfactants and the cellulase into the lignocelluloses and carrying out heating reaction to obtain saccharification hydrolysate with the lignocelluloses; carrying out solid and liquid separation to obtain enzymatic hydrolysate; reducing the temperature of the enzymatic hydrolysate and simultaneously precipitating the ampholytic surfactants and the cellulase so as to recycle the ampholytic surfactants and the cellulase. The method has the advantages that the simple method for cooling and recycling the cellulase by the aid of critical dissolving temperature characteristics of the ampholytic surfactants is proposed for the first time; the lignocelluloses enzymatic hydrolysis efficiency can be effectively improved by the aid of the method, the certain cellulase can be recycled, the method is easy to implement and is green and environmentally friendly, extra equipment can be omitted, and the high activity of the recycled cellulase can be reserved.

Description

technical field [0001] The invention relates to the technical field of lignocellulose enzymatic hydrolysis, in particular to a method for promoting enzymatic hydrolysis of lignocellulose and recovering cellulase by using an amphoteric surfactant. Background technique [0002] Lignocellulosic biorefinery of fuel ethanol is one of the effective and feasible technologies to replace gasoline. In this refining process, whether cellulase can efficiently enzymatically hydrolyze lignocellulosic substrates is a key technical bottleneck. At the same time, cellulase directly hinders the industrialization of cellulosic ethanol because of its low activity, high consumption and high price. The efficient recycling of cellulase is an important way to reduce the cost of bioethanol. At present, cellulase recovery and utilization technologies include ultrafiltration membrane recovery and fresh substrate resorption recovery. The immobilization of cellulase is also an effective way to increas...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C12P19/14C12P19/02C12N9/42
CPCC12N9/2437C12P19/02C12P19/14C13K1/02
Inventor 楼宏铭蔡诚邱学青詹雪娟杨东杰庞煜霞
Owner SOUTH CHINA UNIV OF TECH