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Method for synthesizing glycolide

A technology of glycolide and glycolate, applied in chemical instruments and methods, organic chemistry, chemical/physical/physicochemical processes, etc., can solve the problems of high depolymerization temperature, affecting the purity of glycolide, and the molecular weight distribution of oligomers Width and other issues

Pending Publication Date: 2022-06-28
SHANGHAI ZHONGHUA TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the process of oligomerization, because of the limited mass and heat transfer conditions, long reaction time, and wide molecular weight distribution of oligomers generated, in the process of depolymerization of oligomers to generate glycolide, low molecular weight oligomers It is easy to distill directly, which affects the purity of glycolide. The depolymerization temperature of high molecular weight oligomers is high. At high temperatures, oligomers are easy to carbonize and coke

Method used

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  • Method for synthesizing glycolide
  • Method for synthesizing glycolide
  • Method for synthesizing glycolide

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0082] Add 500g methyl glycolate and 2g catalyst stannous octoate into a 1000mL reaction flask, and stir in the reaction flask for 30min, the catalyst and the raw materials are mixed evenly, and then enter the reactive distillation tower at 2mL / min through the feed pump, and the reaction is refined. The upper end of the distillation column is kept at 75°C, and the lower end is kept at two sections: the first section is 150°C and the second section is 230°C. During the reaction, the methanol removal amount is monitored in real time, and the reaction residence time is about 15min; Do GPC analysis of molecular weight) through the material pump into the scraper reactor for depolymerization, the scraper reactor chamber temperature is 260 ℃, the vacuum degree is 1.1kPa, and the generated glycolide is collected.

[0083] During the reaction, 168.3 g of methanol was separated, the theoretical methanol removal amount was 177.8 g, and the average degree of polymerization of the oligomer ...

Embodiment 2

[0086] Add 500g glycolic acid and 1.5g catalyst zinc acetate dihydrate into a 1000mL reaction flask, heat the reaction flask to 100°C, and stir in the reaction flask for 30min, the catalyst and the raw materials are mixed evenly, and then enter through the feed pump at 3mL / min. In the reactive distillation column, the upper end of the reactive distillation column is kept at 110°C, and the bottom end is kept at 230°C. During the reaction, the water removal amount is monitored in real time, and the reaction residence time is about 10 minutes; The material pump enters the scraper reactor for depolymerization. The temperature of the scraper reactor chamber is 260°C and the vacuum degree is 0.9kPa, and the generated glycolide is collected.

[0087] During the reaction, 110.2 g of water was separated, the theoretical water removal amount was 118.5 g, and the average degree of polymerization of the oligomer was 14.3. Collect 378g of glycolide, 8.7g of still residue, and 4.6g of mater...

Embodiment 3

[0090] Add 500g methyl glycolate and 2g catalyst stannous octoate into a 1000mL reaction flask, and stir in the reaction flask for 30min, the catalyst and the raw materials are mixed evenly, and then enter the reactive distillation tower at 3mL / min through the feed pump, and the reaction is refined. The upper end of the distillation column is kept at 75°C, and the lower end is kept at two sections: the first section is 150°C and the second section is 220°C. During the reaction, the methanol removal amount is monitored in real time, and the reaction residence time is about 10min; Do GPC analysis of molecular weight) through the material pump into the scraper reactor for depolymerization, the scraper reactor chamber temperature is 255 ℃, the vacuum degree is 1.1kPa, and the generated glycolide is collected.

[0091] During the reaction, 164.3 g of methanol was separated, the theoretical methanol removal amount was 177.8 g, and the average degree of polymerization of the oligomer ...

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Abstract

The invention discloses a method for synthesizing glycolide, which comprises the following steps: (1) uniformly mixing glycolic acid and / or glycolic acid ester with a catalyst to obtain a mixture of glycolic acid and / or glycolic acid ester with the catalyst; (2) reacting the mixture of glycollic acid and / or ester thereof obtained in the step (1) and a catalyst in a reactive distillation device to obtain an oligomer with an average polymerization degree of 5-30; and (3) depolymerizing the oligomer obtained in the step (2) to obtain glycolide. According to the method, the phenomena of carbonization and coking in the depolymerization process are greatly reduced, meanwhile, continuous industrial production of the glycolide is facilitated, and the production efficiency of the glycolide is improved.

Description

technical field [0001] The invention belongs to the technical field of glycolide, in particular to a method for synthesizing glycolide. Background technique [0002] Polyglycolic acid (PGA) is a linear aliphatic polyester with the simplest structure. It is a new polymer material with good biocompatibility, gas barrier properties, machinability and degradability. It is also the earliest commercialized in vivo absorbable material. Polymer Materials. Due to its excellent biodegradability and tissue compatibility, it is widely used in biodegradable materials, absorbable sutures, suture reinforcement materials, fracture fixation materials, drug controlled release systems, tissue engineering scaffold materials and other fields. In principle, polyglycolic acid can be prepared from glycolic acid and its esters by direct polycondensation, but it is difficult to prepare higher molecular weight polymers by direct polycondensation. High molecular weight polyglycolic acid can be synthe...

Claims

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Application Information

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IPC IPC(8): C07D319/12B01J19/00
CPCC07D319/12B01J19/00Y02P20/10
Inventor 王涛李永刚李志坚崔磊明汤易天
Owner SHANGHAI ZHONGHUA TECH CO LTD