Method for separating high-purity lignin

A separation method and lignin technology, applied in the field of bioenergy, can solve the problems of corrosion equipment environmental pollution, high reaction temperature, high cost, etc., and achieve the effects of reducing energy consumption, good biocompatibility, and mild treatment conditions

Inactive Publication Date: 2019-08-27
BEIJING FORESTRY UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, the above-mentioned prior art has at least the following disadvantages: when organic acid extracts and separates lignin, the danger of liquid strong acid is high, the requirements for corrosion resistance of reaction equipment are high, and the acidolysis solution after pretreatment requires a large amount of alkali to neutralize, and there is difficulty in recovery. And other issues
The cost of lignin extraction by ionic liquid is high and the raw material solvent needs to be pre-treated, which increases operating costs and limits its industrialization.
When extracting lignin with deep eutectic solvent, there are long reaction time, high reaction temperature, complicated separation procedure and the use of acid-base solution in the separation process, which will cause problems such as corrosion of equipment and environmental pollution.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Corncobs were pulverized, 1g of corncobs of 40-80 mesh was weighed, and 20mL of benzyltrimethylammonium chloride / lactic acid deep eutectic solvent (11.05g of benzyltrimethylammonium chloride and 8.94mL of lactic acid) was added, and Treat at 100° C. for 2 hours at a stirring speed of 400 rpm to obtain a mixed slurry of corn cobs and deep eutectic solvent. Use 400 mesh filter paper for solid-liquid separation under vacuum. The liquid is precipitated with deionized water, centrifuged, and freeze-dried to obtain high-purity lignin. The purity of lignin was determined according to the Technical Association of the American Pulp and Paper Industry (TAPPI) standard method, and the molecular weight and polydispersity were determined by gel permeation method. The yield of lignin was 52%, the purity was 96.84%, and the recovery rate of deep eutectic solvent was 91.3%.

Embodiment 2

[0026] Corncobs were pulverized, 1g of corncobs of 40-80 mesh was weighed, and 20mL benzyltriethylammonium chloride / lactic acid deep eutectic solvent (12.05g benzyltriethylammonium chloride and 7.94mL lactic acid) was added, Treat at 100° C. for 2 hours at a stirring speed of 400 rpm to obtain a mixed slurry of corn cobs and deep eutectic solvent. Use 400 mesh filter paper for solid-liquid separation under vacuum. The liquid is precipitated with deionized water, centrifuged, and freeze-dried to obtain high-purity lignin. The purity of lignin was determined according to the Technical Association of the American Pulp and Paper Industry (TAPPI) standard method, and the molecular weight and polydispersity were determined by gel permeation method. The yield of lignin was 50%, the purity was 96.83%, and the recovery rate of deep eutectic solvent was 95.6%.

Embodiment 3

[0028] Corncobs were pulverized, 1g of corncobs of 40-80 mesh was weighed, and 20mL of benzyltrimethylammonium chloride / lactic acid deep eutectic solvent (11.05g of benzyltrimethylammonium chloride and 8.94mL of lactic acid) was added, and Treat at 120° C. for 2 hours at a stirring speed of 400 rpm to obtain a mixed slurry of corn cobs and deep eutectic solvent. Use 400 mesh filter paper for solid-liquid separation under vacuum. The liquid is precipitated with deionized water, centrifuged, and freeze-dried to obtain high-purity lignin. The purity of lignin was determined according to the Technical Association of the American Pulp and Paper Industry (TAPPI) standard method, and the molecular weight and polydispersity were determined by gel permeation method. The yield of lignin was 66%, the purity was 97.54%, and the recovery rate of deep eutectic solvent was 92.1%.

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Abstract

The invention discloses a method for separating high-purity lignin by treating agricultural and forestry wastes with a green solvent. The method comprises the following steps that 1, a hydrogen bond acceptor and a hydrogen bond donor are heated and dissolved to obtain a low eutectic solvent system of a uniform transparent solution; 2, the agricultural and forestry wastes serve as raw materials, alow eutectic solvent serves as a reaction solvent, and the raw materials and the reaction solvent react in a reaction kettle; 3, after the reaction is completed, cooling is conducted, solid and liquidare centrifugally separated, and the separated liquid is precipitated through deionized water, centrifuged and freeze-dried to obtain the high-purity lignin; 4, rotary evaporation is carried out on the liquid obtained through centrifugation to recover the eutectic solvent. The reaction raw materials in the separation method are the agricultural and forestry wastes, low in cost and environmentallyfriendly, and the low eutectic solvent is easy to prepare, low in cost, free of toxins, recyclable and free of a complex preparation process. According to the method, the treatment conditions are mild, the extraction process is simple, the reaction is easy to control, and the energy consumption is effectively reduced. The obtained lignin is high in purity.

Description

technical field [0001] The invention belongs to the field of biological energy, and in particular relates to a method for separating high-purity lignin from agricultural and forestry wastes by using a green solvent. Background technique [0002] Lignin is the third largest natural organic polymer in the plant kingdom, only a small part is used to produce chemicals or polymer materials, and most of it is burned directly, causing serious resource waste and environmental pollution. If these lignins can be fully utilized to turn waste into treasure, it will not only solve the environmental problems caused by lignin combustion, but also solve the problems of high cost and low economic benefits in the current biomass refining process. Lignin is composed of phenylpropane structural units connected by ether bonds and carbon-carbon bonds. It contains a large number of active functional groups such as carbonyl groups, phenolic hydroxyl groups, and alcoholic hydroxyl groups. It has bro...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08H7/00
CPCC08H6/00
Inventor 许凤郭宗伟游婷婷张逊
Owner BEIJING FORESTRY UNIVERSITY
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