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A kind of preparation method and polymerization reaction system of biodegradable polyester

A technology for degrading polyester and polymerization, applied in chemical/physical/physical-chemical stationary reactors, chemical/physical/physical-chemical mobile reactors, etc., can solve the problems of high molecular weight and slow reaction rate, and achieve molecular weight High, simple method, uniform viscosity effect

Active Publication Date: 2022-06-21
HANGZHOU REJOIN MASTIN MEDICAL INSTR CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The purpose of the present invention is to solve the problem that the polymerization reaction system in the prior art is not suitable for synthesizing biodegradable polyesters with slow reaction rate and high molecular weight including polylactic acid, and to provide a method for biodegradable polyesters Preparation method and polymerization reaction system

Method used

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  • A kind of preparation method and polymerization reaction system of biodegradable polyester
  • A kind of preparation method and polymerization reaction system of biodegradable polyester
  • A kind of preparation method and polymerization reaction system of biodegradable polyester

Examples

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Effect test

Embodiment 1

[0050] A preparation method of a biodegradable polyester using the above-mentioned polymerization reaction system, wherein in the polymerization reaction system, the stirring form of the reaction kettle 1 is an anchor type, the reaction kettle 2 is a double-cone rotary dryer, and the cooling liquid is a temperature of 2 ° C. water;

[0051] Specific steps are as follows:

[0052] (1) adding stannous octoate, stearyl alcohol and reaction raw materials (mass ratio is the mixture of the L-lactide and glycolide of 2.19:0.31) after mixing and adding in the reactor 1, and sealing, the reactor 1 is pumped Vacuum, then fill with argon gas, and then vacuumize, do this for 3 times, and carry out the reaction to obtain a prepolymer with an intrinsic viscosity of 0.8dL / g; the addition of stannous octoate is 100ppm of the reaction raw materials; the addition of stearyl alcohol is 200 ppm of the reaction raw materials; the reaction temperature of the reaction raw materials in the reaction ...

Embodiment 2

[0057] A method for preparing a biodegradable polyester using the above-mentioned polymerization reaction system, wherein in the polymerization reaction system, the stirring form of the reaction kettle 1 is an anchor type, the reaction kettle 2 is a double-cone rotary dryer, and the cooling liquid is a temperature of -20 ℃ of ethanol;

[0058] Specific steps are as follows:

[0059] (1) adding stannous octoate, dodecanol and reaction raw materials (mass ratio is the mixture of the L-lactide and glycolide of 2.19:0.31) after mixing and adding in the reactor 1, and sealing, the reactor 1 is pumped Vacuum, then fill with argon, and then vacuumize again, and do this for 3 times, and carry out the reaction to obtain a prepolymer with an intrinsic viscosity of 2.2dL / g; the addition of stannous octoate is 30ppm of the reaction raw materials; the addition of dodecanol It is 150ppm of the reaction raw materials; the reaction temperature of the reaction raw materials in the reaction ke...

Embodiment 3

[0064] A preparation method of a biodegradable polyester using the above-mentioned polymerization reaction system, wherein in the polymerization reaction system, the stirring form of the reaction kettle 1 is a frame type, the reaction kettle 2 is a double-cone rotary dryer, and the cooling liquid is a temperature of 8 ° C. water;

[0065] Specific steps are as follows:

[0066] (1) adding stannous octoate, ethylene glycol and reaction raw materials (mass ratio is the mixture of L-lactide and caprolactone of 2:0.34) after mixing, join in reactor 1, and seal, and vacuumize reactor 1 , then filled with argon, and then evacuated, so operated 3 times, and reacted to obtain a prepolymer with an intrinsic viscosity of 1.6dL / g; the addition of stannous octoate was 100ppm of the reaction raw materials; the addition of ethylene glycol was 200ppm of the reaction raw materials; the reaction temperature of the reaction raw materials in the reaction kettle 1 is 180 ° C, the pressure is 1.2...

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Abstract

The invention relates to a preparation method of biodegradable polyester and a polymerization reaction system. The polymerization reaction system includes a reaction kettle 1, a low-temperature outer casing, a double-gear pulverizer and a reaction kettle 2; The position of the double gear pulverizer is respectively equipped with valve 2 and valve 3; the preparation method is: mix the catalyst, initiator and reaction raw materials and add them to the reaction kettle 1 for reaction to obtain prepolymerization with an intrinsic viscosity of 0.8-3.0dL / g Then the prepolymer is cooled to 80-130°C and crushed into particles, and finally the particles are transferred to the reactor 2 to continue the reaction to obtain biodegradable polyester; the reaction raw material is biodegradable cyclic lactone or lactide; The reaction temperature of the particles in the reactor 2 is higher than the melting point of the reaction raw materials and lower than the melting point of the prepolymer. The method of the invention is simple, and the obtained biodegradable polyester has high and uniform intrinsic viscosity; and the discharge of the biodegradable polyester is convenient when the polymerization reaction system of the invention is used to prepare the biodegradable polyester.

Description

technical field [0001] The invention belongs to the technical field of biodegradable polymer materials, and relates to a preparation method and a polymerization reaction system of a biodegradable polyester. Background technique [0002] Medical polylactic acid materials often require high molecular weight due to mechanical strength and degradation performance. However, due to the slow reaction rate, it is not easy to obtain high molecular weight products in a relatively short period of time. Moreover, its molecular weight is high. In view of the influence of various factors such as stirring, the products will have problems such as uneven viscosity and difficulty in discharging during the synthesis process. solved problem. [0003] U.S. Patent No. 5,484,882 discloses a polymerization reactor for cyclic ester and lactone production of copolyester, but it adopts solution polymerization, which requires the use of a large amount of solvent, causing serious environmental pollutio...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08G63/08C08G63/78B01J19/18B01J19/20B01J19/28
CPCC08G63/08C08G63/785B01J19/18B01J19/28B01J19/20C08G2230/00
Inventor 吴侃李若云朱莎莎李凌晨蒋冠森
Owner HANGZHOU REJOIN MASTIN MEDICAL INSTR CO LTD