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A method for wood acetylation and co-production of acetate

A technology of acetylation and acetate, which is applied in the field of acetylated wood preparation, can solve the problems of high corrosion resistance, complicated acetylation process, increased energy consumption and cost, etc., achieve the effect of increasing efficiency and reducing consumption, and increase the added value of acetic acid Value, the effect of optimizing the production process

Active Publication Date: 2018-02-13
JIANGSU JINJU ALLOY MATERIAL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] In order to speed up the acetylation reaction rate and ensure the wood weight gain rate in the final product, an excess of acetic anhydride is usually required to participate in the reaction, which in turn leads to increased energy consumption and cost in the subsequent rectification and separation of unreacted acetic anhydride and by-product acetic acid
On the other hand, the wood acetylation process is complex and requires high corrosion resistance of equipment, resulting in high cost and price of acetylated wood despite its excellent performance. Added value of the product acetic acid, a new technological process to reduce the cost of acetylated wood

Method used

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Embodiment 1

[0024] A method for wood acetylation and co-production of acetate, the preparation steps are as follows: (1) wood drying treatment: first, the wood (length x width x height = 10cm x 10cm x 3m, radiata pine) is steamed and dried until the moisture content is 8%; (2) wood acetylation: put an appropriate amount of wood in the reaction tank, and add acetylation reagent acetic anhydride, so that the wood is completely immersed in acetic anhydride, the volume ratio of wood to acetic anhydride 1:2, then heated to 120°C, the reaction time is 8h, pressurized to 0.5MPa, the wood acetylation reaction; (3) Esterification and co-production of acetate: step (2) by-product acetic acid enters in gas phase At the bottom of the reactive distillation tower, methanol is pumped from the middle and lower part of the reactive distillation tower at the same time, and the SO2 filled in the reactive distillation tower 4 2- / ZrO 2Under the catalysis of the solid superacid catalyst, the reaction temper...

Embodiment 2

[0026] A method for wood acetylation and co-production of acetate, the preparation steps are as follows: (1) wood drying treatment: first, the wood square (length×width×height=10cm×10cm×3m, pine sylvestris) is steamed, Dry to a moisture content of 10%; (2) Acetylation of wood: put an appropriate amount of wood in a reaction tank, and add acetylation reagent acetic anhydride to completely immerse the wood in acetic anhydride, the volume of wood and acetic anhydride The ratio is 1:2.5, then heated to 130°C, the reaction time is 6h, and the pressure is increased to 0.3MPa, so that the wood is acetylated; (3) Esterification and co-production of acetate: the by-product acetic acid in step (2) is in the form of gas phase Enter the bottom of the reactive distillation column, and pump ethanol from the middle and lower part of the reactive distillation column at the same time. 4 2- Under the catalysis of / Zr-ZSM-5 solid superacid catalyst, under the conditions of reaction temperature ...

Embodiment 3

[0028] A method for wood acetylation and co-production of acetate, the preparation steps are as follows: (1) Wood drying treatment: first, the wood square (length×width×height=10cm×10cm×3m, poplar) is steamed, dried To the moisture content of 12%; (2) Wood acetylation: put an appropriate amount of wood in the reaction tank, and add the acetylating reagent acetic anhydride, so that the wood is completely immersed in acetic anhydride, the volume ratio of wood to acetic anhydride 1:3, then heated to 140°C, reaction time 4h, pressurized to 0.1MPa to make wood acetylated; (3) Esterification and co-production of acetate: the by-product acetic acid in step (2) enters in the form of gas phase At the bottom of the reactive distillation column, at the same time, n-butanol is pumped from the middle and lower part of the reactive distillation column, and the two are filled with SO in the reactive distillation column 4 2- / TiO 2 Under the catalysis of solid super acid catalyst, under the...

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Abstract

The invention discloses a wood acetylation and acetate cooperative production method. The technological process that a byproduct of acetic acid is subjected to rectification separation in a traditional wood acetylation process so as to be cycled to be used for acetic anhydride reproduction is changed. A wood acetylation technology is innovatively combined with an esterifying acetate preparing technology, the byproduct of acetic acid in the wood acetylation process is moved out through continuous rectification, the acetylation reaction speed is increased, the use amount of acetic anhydride is obviously reduced, meanwhile, the energy generated in the process of moving out the byproduct of acetic acid through rectification is fully utilized and reacts with low-carbon alcohol to be prepared into an acetate product, so that cooperative production of acetylation wood and an acetate product is achieved, the production technological processes are optimized and completed, product structures are enriched, the additional value of the byproduct of acetic acid is improved, and the production cost of the acetylation wood and the acetate is obviously reduced. In addition, the wood acetylation and acetate cooperative production method is simple and easy to implement and can be easily used for industrial application.

Description

technical field [0001] The invention relates to a method for wood acetylation and co-production of acetate, belonging to the technical field of acetylated wood preparation. Background technique [0002] Wood is the material with the longest history among the four major building materials (steel, cement, plastic, and wood) in the world today, and it is also the only natural biological material that is renewable, recyclable, and naturally degradable. my country is one of the countries lacking in forests and materials, and the supply of timber depends heavily on imports. At present, my country's timber consumption is nearly 500 million cubic meters per year, and the dependence on foreign countries is as high as 50%. By 2020, my country's timber demand will reach about 800 million cubic meters per year. year. As the contradiction between the effective supply of forests in my country and the growing social demand continues to intensify, the dependence on foreign timber in my coun...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C67/08C07C69/14B27K5/04B27K3/34
CPCB27K3/34B27K5/04C07C51/087C07C67/08C07C69/14C07C53/08Y02P20/10
Inventor 吴晓金吴维果陈加波张涛刘志刚
Owner JIANGSU JINJU ALLOY MATERIAL
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