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A method for extracting lignin from biomass

A technology of lignin and biomass, applied in papermaking, textile and papermaking, fiber raw material processing, etc., can solve the problems of unfavorable organic solvent recycling, difficulty in lignin extraction, unfavorable lignin depolymerization and modification work, etc. The effect of reducing oxidative condensation reaction, increasing penetration and maintaining integrity

Active Publication Date: 2019-11-12
QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the traditional organic solvent pulping process generally requires high temperature and high pressure environment, which will cause condensation reaction of lignin during the extraction process, which not only makes the extraction of lignin difficult, but also is not conducive to the subsequent depolymerization and modification of lignin.
At the same time, hydrochloric acid or sulfuric acid is needed for catalysis in the lignin extraction process, so it is not conducive to the recycling of organic solvents

Method used

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  • A method for extracting lignin from biomass
  • A method for extracting lignin from biomass
  • A method for extracting lignin from biomass

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Take 100 g of pulverized poplar wood powder and add it into a three-necked flask filled with 700 mL of dioxane, place the three-necked flask in an ultrasonic instrument with a power of 20 W, and oscillate ultrasonically at a frequency of 30 kHz for 20 min. Take 10g H 3 PO 4 -AC and 50 mL of dimethyl carbonate were added to the flask. The three-necked flask was heated to 120° C., condensed and refluxed for 1 h, and nitrogen was always fed as a protective gas during this period. After the reaction, solid-liquid separation was achieved by suction filtration. The filtrate is concentrated by rotary evaporation, and the evaporated organic solvent can be recycled, and the concentrated solution is dissolved in 200 mL of acetone solution. Then slowly add the acetone solution into 1L of 5°C cold water to precipitate the lignin. Finally, filter, wash, and vacuum dry to obtain lignin. The extraction rate and properties of lignin are shown in Table 1.

Embodiment 2

[0035] Take 100 g of pulverized poplar wood powder and add it into a three-necked flask containing 1000 mL of dioxane, place the three-necked flask in an ultrasonic instrument with a power of 40 W, and oscillate ultrasonically at a frequency of 30 kHz for 20 min. Take 10g H 3 PO 4 -AC and 70 mL of dimethyl carbonate were added to the flask. The three-necked flask was heated to 120° C., condensed and refluxed for 1 h, and nitrogen was always fed as a protective gas during this period. After the reaction, solid-liquid separation was achieved by suction filtration. The filtrate is concentrated by rotary evaporation, and the evaporated organic solvent can be recycled, and the concentrated solution is dissolved in 200 mL of acetone solution. Then slowly add the acetone solution into 1 L of cold water (1° C.) to precipitate lignin. Finally, lignin was obtained by filtering, washing, and vacuum drying. The extraction rate and properties of lignin are shown in Table 1.

Embodiment 3

[0037] Take 100 g of pulverized poplar wood powder and add it into a three-necked flask filled with 700 mL of dioxane, place the three-necked flask in an ultrasonic instrument with a power of 20 W, and ultrasonically vibrate at a frequency of 20 kHz for 20 min. Take 10g H 3 PO 4 -SiO2 and 50 mL of dimethyl carbonate were added to the flask. The three-necked flask was heated to 120° C., condensed and refluxed for 1 h, and nitrogen was always fed as a protective gas during this period. After the reaction, solid-liquid separation was achieved by suction filtration. The filtrate is concentrated by rotary evaporation, and the evaporated organic solvent can be recycled, and the concentrated solution is dissolved in 200 mL of acetone solution. Then slowly add the acetone solution into 1L of 4°C cold water to precipitate the lignin. Finally, lignin was obtained by filtering, washing, and vacuum drying. The extraction rate and properties of lignin are shown in Table 1.

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Abstract

The invention belongs to the field of biological energy sources, and particularly relates to a method for extracting lignin from biomass. The method comprises the steps that an organic solvent is adopted as an extracting agent, and under the catalysis effect of solid acid, lignin is extracted from biomass raw materials under the inert gas atmosphere. According to the method, the biomass obtained through ultrasonic oscillation pretreatment is digested through the organic solvent under the catalytic effect of solid acid for extracting the lignin. The method is environmentally friendly and low inenergy consumption, the lignin is complete in structure, and the extraction efficiency is high.

Description

technical field [0001] The invention belongs to the field of biological energy, in particular to a method for extracting lignin from biomass. Background technique [0002] The rapid development of the world economy has led to excessive use of energy, and the rapid development of modern industry has sharply consumed fossil resources and caused a series of environmental problems. Traditional fossil resources are non-renewable, so resource and environmental issues are the great challenges faced by human beings today, and the utilization of renewable biomass energy has become an inevitable choice for the sustainable development of society. Lignocellulosic biomass is rich in resources and can be regenerated repeatedly. At present, the use of biomass to produce fuels and chemicals has become a research hotspot. Lignocellulose is composed of cellulose, hemicellulose, and lignin. The lignin in the network structure acts as a supporting framework to surround and reinforce the cellul...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08H7/00D21C5/00
CPCD21B1/303D21C5/00
Inventor 李学兵王玉阳王达李小玉林冠楠王忠李双菊
Owner QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI