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Method for preparing aromatic-aliphatic copolyester

An aliphatic copolyester and aromatic technology, which is applied in the field of preparing degradable aromatic-aliphatic copolyester, can solve the problems of easy pollution to the environment, not a synthetic process method, and difficult degradation, so as to reduce the sequence length, Good mechanical behavior, cheap and easy-to-obtain raw materials

Inactive Publication Date: 2009-04-22
NINGBO INST OF TECH ZHEJIANG UNIV ZHEJIANG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

From the descriptions of these patents, it can be learned that the synthesis process for obtaining aromatic-aliphatic copolyesters is mainly divided into two types: one is to use aromatic dibasic acid methyl ester as a reaction monomer and aliphatic dibasic acid And dibasic alcohol carries out co-condensation reaction to obtain copolyester product, and this process will release toxic methanol molecules during operation, which is easy to cause pollution to the environment, and is not an environmentally friendly synthetic process method; the other is to directly synthesize aromatic polyester Copolyester products are obtained by reactive blending with aliphatic polyesters. Although the process is simple to operate, the resulting products are often block copolymers, and the aromatic segments still exist in the molecular chain in the form of longer segments. In the same way as ordinary aromatic polyester, this part of the segment still has the disadvantage of being difficult to degrade
Therefore, both methods have certain limitations

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] 4.15g (0.025mol) terephthalic acid, 9.01g (0.1mol) 1,4-butanediol and 3wt% Ti[OBu] 4 Add it into a 50ml flask, stir it under normal pressure at 200°C for 1 hour, then raise the temperature to 210°C, stir it under normal pressure for 0.5 hour, then stir it under normal pressure at 220°C for 0.5 hour, keep the temperature constant and lower the pressure to 20000Pa, continue After 3 hours of reaction, dibutylene terephthalate can be obtained.

[0016] Add 3.45g of polylactic acid prepolymer (obtained by direct dehydration of lactic acid at 150°C, the amount of lactic acid is 0.0083mol) to dibutylene terephthalate, gradually reduce the pressure to 50Pa at 230°C, and stir for 6h. A degradable copolyester is obtained.

Embodiment 2

[0018] 4.15g (0.025mol) terephthalic acid, 7.20g (0.08mol) 1,4-butanediol, 2.88g (0.02mol) cyclohexanedimethanol and 5wt% Ti[OBu] 4 Add it into a 50ml flask, stir it under normal pressure at 210°C for 1 hour, then raise the temperature to 220°C, stir it under normal pressure for 0.5 hour, then stir it under normal pressure at 230°C for 0.5 hour, keep the temperature constant and lower the pressure to 20000Pa, continue After 4 hours of reaction, dibutylene terephthalate can be obtained.

[0019] Add 3.45g of polylactic acid prepolymer (obtained by direct dehydration of lactic acid at 150°C, the amount of lactic acid is 0.0083mol) to dibutylene glycol cyclohexanedimethanol terephthalate, and gradually reduce the pressure to 50Pa at 250°C , stirring for 6 hours to obtain a degradable copolyester.

Embodiment 3

[0021] With 4.15g (0.025mol) terephthalic acid, 10.61g (0.1mol) diethylene glycol and 3wt%Ti[OBu] 4 Add it into a 50ml flask, stir it under normal pressure at 200°C for 1 hour, then raise the temperature to 210°C, stir it under normal pressure for 0.5 hour, then stir it under normal pressure at 220°C for 0.5 hour, keep the temperature constant and lower the pressure to 20000Pa, continue After 3 hours of reaction, dibutylene terephthalate can be obtained.

[0022] Add 3.45g of polylactic acid prepolymer (obtained by direct dehydration of lactic acid at 150°C, the amount of lactic acid is 0.0083mol) to dibutylene terephthalate, gradually reduce the pressure to 50Pa at 230°C, and stir for 6h. A degradable copolyester is obtained.

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PUM

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Abstract

The invention relates to a method for preparing aromatic-aliphatic copolyester. In the method, aromatic binary acid, dihydric alcohol and aliphatic hydroxy acid are used as a copolymerization system to prepare the aromatic-aliphatic copolyester by direct melt polycondensation under the action of a catalyst, wherein the dihydric alcohol is one or both of aliphatic dihydric alcohol and cyclized aliphatic dihydric alcohol. The method overcomes the defect of the generation of poisonous methanol in the prior ester exchange process. By the random copolymerization, a polylactic acid chain segment can be introduced to an aromatic polyester chain segment, and the sequence length of an aromatic component is reduced, thereby improving the degradation property of the copolyester and keeping better mechanical behavior; moreover, the method also has the advantages of simple synthesis process, easy reaction operation and low-priced and easily obtained materials, and the obtained copolyester has certain degradation property.

Description

technical field [0001] The invention relates to a method for preparing aromatic-aliphatic copolyester, in particular to a method for preparing degradable aromatic-aliphatic copolyester. Background technique [0002] With the development of the economy and the continuous improvement of people's living standards, plastics, especially disposable plastic packaging materials, daily necessities and mulch waste, are increasingly polluting the environment. On the other hand, the dwindling petroleum resources also pose a corresponding threat to the sustainable development of the global plastics industry, and plastic materials derived from petroleum resources have penetrated into various fields of the national economy. The technological progress of various sectors of the national economy and the people's Life is inseparable from plastic materials, so how to reduce dependence on petroleum resources is the key to the sustainable development of the plastics industry and even the global e...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G63/60C08G63/78
Inventor 张艳方征平王炳涛郭正虹程捷
Owner NINGBO INST OF TECH ZHEJIANG UNIV ZHEJIANG
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