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Cracking lignin and preparation method of lignin-based polyurethane rigid foam

A rigid foam, lignin-based technology, applied in the polymer field, can solve the problems of complex composition, large difference in hydroxyl value, and small addition amount, and achieve the effects of simple synthesis method, stable performance and easy operation.

Active Publication Date: 2021-08-06
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of this method are: the biomass waste is mixed with corn stalks, rice straws, cotton stalks, etc., and its components are complex, which is not conducive to treatment, and the addition amount is small, which has a great impact on the performance of polyurethane foam; the liquefaction reagent for biomass materials is Concentrated hydrochloric acid or concentrated sulfuric acid, the temperature reaches 200 ℃, the energy consumption is large, which is not conducive to industrialization; not only biomass waste is added to polyurethane, but also lignosulfonate is added to industrial crude lignin, the particle size, molecular weight, The difference in hydroxyl value is large, which will cause complex effects on the blending and foaming of polyurethane components, and easily cause unstable product performance

Method used

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  • Cracking lignin and preparation method of lignin-based polyurethane rigid foam
  • Cracking lignin and preparation method of lignin-based polyurethane rigid foam
  • Cracking lignin and preparation method of lignin-based polyurethane rigid foam

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] The wood fiber was pulverized and passed through an 80-mesh standard sieve to obtain wood fiber with uniform particle size. The pulverized wood fiber was dried at 60°C for 3 hours in a vacuum constant temperature drying oven. Get quantitative wood fiber and put it into an autoclave, check the airtightness of the autoclave before the reaction, then seal it, and then use 1MPa H 2 Pressurize to make the pressure of the whole system reach 2MPa, and slowly heat to 250°C. The reaction uses a supported ruthenium metal catalyst, reacts for 4 hours, and uses methanol as a solvent to carry out the catalytic cracking reaction. Take the liquid lignin and methanol in the upper layer of the product, and rotate it under reduced pressure at 40°C to remove methanol to obtain liquid cracked lignin.

[0035] Add 2g of the prepared cracked lignin into the beaker, add the corresponding polyether polyol 5110 according to the mass ratio of 1:9, and add 0.5g catalyst A33, 0.5g stannous octoat...

Embodiment 2

[0037] The wood fiber was pulverized and passed through a 100-mesh standard sieve to obtain wood fiber with uniform particle size. The pulverized wood fiber was dried at 100°C for 2 hours in a vacuum constant temperature drying oven. Take a certain amount of wood fiber and put it into the autoclave, check the airtightness of the autoclave before the reaction, then seal it, then pressurize with 1MPa H2 to make the pressure of the whole system reach 3MPa, and slowly heat to 240°C. The reaction uses a supported ruthenium metal catalyst, reacts for 5 hours, and uses methanol as a solvent to carry out catalytic cracking reaction. The liquid lignin and methanol in the upper layer of the product were taken and rotated at 40°C under reduced pressure to remove the methanol to obtain liquid cracked lignin.

[0038] Add 6g of the prepared cracked lignin into the beaker, add the corresponding PEG (polyethylene glycol) in a mass ratio of 3:7, and add 0.5g catalyst A33, 0.5g stannous octoat...

Embodiment 3

[0040]The wood fiber was pulverized and passed through a 40-mesh standard sieve to obtain wood fiber with uniform particle size. The pulverized wood fiber was dried at 80°C for 3 hours in a vacuum constant temperature drying oven. Take a certain amount of wood fiber and put it into the autoclave, check the airtightness of the autoclave before the reaction, then seal it, then pressurize with 1MPa H2, make the pressure of the whole system reach 1MPa, and slowly heat to 230°C. The reaction uses a supported ruthenium metal catalyst, reacts for 3 hours, and uses methanol as a solvent to carry out catalytic cracking reaction. The liquid lignin and methanol in the upper layer of the product were taken and rotated at 40°C under reduced pressure to remove the methanol to obtain liquid cracked lignin.

[0041] Add 10g of the prepared cracked lignin in the beaker, add the corresponding PPG-1000 (polypropylene glycol) in a mass ratio of 1:1, and add 0.5g catalyst A33, 0.5g stannous octoat...

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Abstract

The invention provides cracked lignin, which is obtained by hydrogenating and catalytically cracking wood fiber. The invention also provides a preparation method of lignin-based polyurethane rigid foam, wherein the split lignin provided by the invention can replace part of petroleum-based polyols. The lignin-based polyurethane rigid foam obtained by the preparation method of the invention not only has excellent performance, but also has degradable and renewable environmental protection performance, and has great industrial application prospects.

Description

technical field [0001] The invention belongs to the field of macromolecules, in particular to a method for cracking lignin and lignin-based polyurethane rigid foam. Background technique [0002] Since polyurethane rigid foam has excellent thermal insulation properties, it is generally widely used as thermal insulation materials for general buildings. Usually, polyurethane rigid foam is prepared by the following method: first prepare polyisocyanate component liquid and mixed liquid, the mixed liquid contains polyether polyol and / or polyester polyol, foaming agent, and also mixed with catalyst and Foam stabilizer, etc., and then mix the polyisocyanate component liquid and the mixed liquid, and cure it after foaming for a short time. [0003] As the total amount of inefficient renewable resources such as petroleum and coal is decreasing day by day, it is becoming a development trend to transform plant and microbial resources into new materials, high calorific value energy and ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08G18/76C08G18/64C08G18/48C08J9/08C08H7/00C08G101/00
CPCC08G18/4081C08G18/48C08G18/4825C08G18/4833C08G18/6492C08G18/7614C08G18/7664C08G18/7671C08G2230/00C08H6/00C08G2110/0025C08G2110/0083
Inventor 谭天伟段伊静曹辉方云明邱石姜志国张成彬
Owner BEIJING UNIV OF CHEM TECH