A method for separating highly active lignin from agricultural and forestry biomass
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A biomass and high activity technology, applied in the field of biomass refining and resource utilization, can solve the problems of less than 20% effective utilization rate and reducing the potential for high-value separation of lignin
Inactive Publication Date: 2020-12-01
YANCHENG INST OF TECH
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However, the annual output of 11 million tons of lignin in my country has an effective utilization rate of less than 20% (Mahmood, N., Yuan, Z.S., Schmidt, J. et al., 2016. Depolymerization of lignins and their applications for the preparation of polyols and rigid polyurethane foams: a review. Renewable & Sustainable Energy Reviews, 60, 317-329.)
However, Chen et al. found in their research that TsOH separated lignin still has a large number of C-C condensation structures at the 2, 5, and 6 positions of its benzene ring, which reduces the high-value potential of separated lignin
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Embodiment 1
[0037] The wheat straw used in the experiment was produced in Shuyang, Jiangsu. Cut the raw material to about 3 cm in length, then crush the wheat straw stalks with a plant grinder and sieve, take 20-80 mesh (accounting for 80% of the raw material) wheat straw powder, air-dry and set aside.
[0038] (1) Extract 20-80 mesh wheat grass powder with benzene alcohol (2:1, v / v) in a Soxhlet extractor at 85°C for 8 hours to remove lipids and Waxy, after extraction, the raw material is air-dried for later use.
[0039] (2) Both p-toluenesulfonic acid and ethanol are purchased from Aladdin reagents. Before preparing p-toluenesulfonic acid / ethanol solvent, p-toluenesulfonic acid must be dissolved in absolute ethanol, and the rotary evaporator should be used to remove them as much as possible. After crystallization water, compound with absolute ethanol to form the target solvent. Before and after the solution is prepared, the change of moisture is measured by a Karl Fischer moisture an...
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Abstract
The invention discloses a method for separating high-activity lignin from agriculture and forestry biomasses. The method comprises the following steps: (1) smashing and sieving a biomass raw material,performing degreasing and dewaxing treatment and then drying and standing by; (2) adding the biomass raw material acquired in the step (1) into a prepared toluenesulfonic acid / ethyl alcohol system, and controlling reaction temperature at 40-100 DEG C and reaction time within 10-120min, thereby acquiring a mixture; (3) adding hot water into the mixture acquired in the step (2) and performing suction filtration, thereby acquiring a component rich in cellulose, and then cleaning, drying and standing by; (4) continuously adding water into the rest liquid part acquired in the step (3) till the concentration of p-toluenesulfonic acid is below 11.5%, centrifugally separating, separating the solid part and then drying and standing by, performing rotary evaporation concentration on the rest liquidpart, recycling p-toluenesulfonic acid by re-crystallizing, and lastly acquiring the remained hemicellulose and degradation product thereof. The invention mainly concerns the separation of high-activity lignin from agriculture and forestry biomasses and meanwhile realizes the all-component separation of cell walls of agriculture and forestry biomasses.
Description
technical field [0001] The invention belongs to the field of biomass refining and resource utilization, and in particular relates to a method for separating high-activity lignin from agricultural and forestry biomass. Background technique [0002] The utilization of lignocellulose has long had the problem of resource utilization of a single component (Wen, J., Yuan, T., Sun, R., 2017. Biorefining and multistage utilization of lignocellular biomass. Biotechnology and Business, 3, 94-99) Among them, cellulose and hemicellulose (accounting for about 70%) have a relatively simple structure. After separation, paper products, nano-cellulose materials, ethanol, furfural, and hydroxymethylfurfural can be obtained through chemical catalysis or biological fermentation. The remaining 30% lignin, due to its complex structure, cannot achieve effective separation and high value under the existing industrial separation conditions (Sun, S.N., Sun, S.L., Cao, X.F., et al., 2016, The role of...
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