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Method used for extracting lignin from lignocelluloses raw material and preparing p-hydroxy benzaldehyde via catalytic conversion

A technology of p-hydroxybenzaldehyde and lignocellulose, which is applied in the preparation of carbon-based compounds, chemical instruments and methods, and the preparation of organic compounds, can solve problems such as easy repolymerization and complexation reactions, complex structures, etc. Low, high catalytic activity, high activity effect

Inactive Publication Date: 2016-03-30
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the complex structure of lignin itself and the tendency of repolymerization and complexation reactions during the degradation process, it is extremely important to develop a process route for the efficient catalytic conversion of lignin to prepare p-hydroxybenzaldehyde

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Take corn stover as raw material, use 40% 1,4-butanediol aqueous solution as solvent, solid-to-liquid ratio 1:4, temperature 220°C, cool after 2h reaction, filter, and weigh the filter cake; add three times the volume of the filtrate Deionized water is allowed to stand overnight and filtered, and the obtained filter residue is washed and vacuum dried to obtain corn stover to extract lignin. The lignin is used in the catalytic conversion system, the reaction conditions: lignin concentration 20g / L, LaFe 0.2 Cu 0.8 O 3 Concentration 2g / L, use NaOH solution to adjust the pH value of the system to 13, temperature 160℃, charge O 2 Pressure 8bar, reaction for 2h, take it out and centrifuge to get the catalyst, the supernatant is adjusted to pH 1-2 with concentrated HCl, and unreacted lignin is precipitated; filtered, lignin washed and weighed, the volume of the filtrate is recorded, sampled, and analyzed by HPLC The yield of p-hydroxybenzaldehyde was 3.06%.

Embodiment 2

[0023] Using walnut shell as raw material, 60% 1,4-butanediol aqueous solution is used as solvent, solid-liquid ratio is 1:8, temperature is 180℃, after 2.5 hours of reaction, cooled, filtered, and the filter cake is recovered and weighed; the filtrate is added to three times the volume The deionized water is allowed to stand overnight and filtered. The obtained filter residue is washed and vacuum dried to obtain lignin from walnut shells. The lignin is used in the catalytic conversion system, the reaction conditions: lignin concentration 2g / L, LaNi 0.2 Cu 0.8 O 3 Concentration 2g / L, adjust the pH value of the system to 11 with NaOH solution, temperature 180℃, charge O 2 Pressure 2bar, reaction for 2h, take it out and centrifuge to obtain the catalyst, the supernatant is adjusted to pH 1-2 with concentrated HCl, and unreacted lignin is precipitated; filtered, lignin washed and weighed, the volume of the filtrate is recorded, sampled, and analyzed by HPLC The yield of p-hydroxybe...

Embodiment 3

[0025] Using coconut shell as raw material, using 80% 1,4-butanediol aqueous solution as solvent, solid-liquid ratio 1:10, temperature 200℃, cooling after 4h reaction, filtering, filter cake recovery and weighing; adding three times the volume of the filtrate Deionized water is allowed to stand overnight and filtered, and the obtained filter residue is washed and vacuum dried to obtain lignin from walnut shells. The lignin was used in the catalytic conversion system, the reaction conditions: lignin concentration 10g / L, 5% loading The molecular sieve concentration is 1g / L, the pH value of the system is adjusted to 9 with NaOH solution, the temperature is 140℃, and O is charged 2 The pressure is 6bar, the reaction is 1.5h, and the catalyst is obtained by centrifugation after removal. The supernatant is adjusted to pH 1-2 with concentrated HCl to precipitate unreacted lignin; filtered, washed with lignin and weighed, the volume of the filtrate is recorded, sampled, and analyzed by ...

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PUM

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Abstract

The invention discloses a method used for extracting lignin from lignocelluloses raw material and preparing p-hydroxy benzaldehyde via catalytic conversion. The method mainly comprises following steps: 1) a high boiling alcohol solvent is used for extracting lignin from lignocelluloses of agricultural wastes such as nut shell and straw 2) perovskite oxides LaNi<1-x>Cu<x>O<3> and LaFe<1-x>Cu<x>O<3> are prepared, carriers such as 5 angstrom molecular sieve and MCM-22 molecular sieve are loaded with the perovskite oxides so as to obtain heterogeneous perovskite-type oxide catalysts; 3) the obtained heterogeneous perovskite-type oxide catalysts are applied to preparation of p-hydroxy benzaldehyde via catalytic oxidation of lignin; and 4) after reaction, an obtained product is filtered, the heterogeneous catalysts are separated, and are recycled after reduction regeneration.

Description

Technical field [0001] The invention belongs to the technical field of biomass extraction and conversion, and relates to a method for preparing p-hydroxybenzaldehyde by catalytic conversion of lignin extracted from lignocellulose raw materials. The method can significantly improve the conversion rate of lignin and the p-hydroxybenzaldehyde The yield provides more possibilities for the high-value conversion and utilization of lignin. Background technique [0002] Biomass is a renewable resource widely existing in nature. As one of the three main components, lignin is formed by connecting three structural monomers of p-hydroxyphenyl, guaiacyl and syringyl, and has a variety of active groups. Groups and complex three-dimensional network structure, in which the main groups are phenolic hydroxyl, alcoholic hydroxyl, active hydrogen, ether bond and carboxyl. These functional group lignins can be used in the preparation and production of soil amendments, adhesives, slow-release nitroge...

Claims

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Application Information

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IPC IPC(8): C07C47/565C07C45/00B01J29/76B01J23/83
CPCC07C45/00B01J23/002B01J23/83B01J29/76B01J29/7676B01J2229/20B01J2523/00C07C47/565B01J2523/17B01J2523/3706B01J2523/847B01J2523/842
Inventor 徐建曲永水李莉李宏强
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI