Supercharge Your Innovation With Domain-Expert AI Agents!

1, 2-propanediol copolyester polyterephthalate with high 1, 2-propanediol content and preparation method thereof

A technology of polyterephthalic acid and propylene glycol copolyester, which is applied in the field of polyterephthalic acid 1, can solve the problems of difficult to obtain high molecular weight polyester, high reactivity, and difficult polymers, etc., to meet high temperature requirements Use environment, stable molding size, good transparency

Active Publication Date: 2013-01-16
SHANGHAI GENIUS ADVANCED MATERIAL (GRP) CO LTD
View PDF1 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, the side chain methyl group on the 1,2-propanediol molecule increases the T of poly-1,2-propanediol ester g At the same time, it also reduces the reactivity of secondary hydroxyl groups, so it is difficult to polymerize with dibasic acids to obtain high molecular weight polymers
Propose 1 in U.S. Patent 4093603, the polyester of 2-propanediol and terephthalic acid is basically useless, because there are both primary hydroxyl groups and secondary hydroxyl groups on it, and the reactivity of secondary hydroxyl groups in the polycondensation process is lower than that of The primary hydroxyl group is much weaker, so it is difficult to obtain high molecular weight polyester from 1,2-propanediol with secondary hydroxyl groups
[0005] When utilizing 1,2-propanediol to carry out copolymerization with linear diols (such as ethylene glycol, butanediol, etc.) Hydroxyl, high reactivity, when the content of linear diol is less, it is easy to polymerize first and be located inside the polyester molecular chain, and then 1,2-propanediol is connected to the two ends of the molecular chain to form a capping effect, which also cannot be obtained High molecular weight polyester; when the content of linear diol is high, a large part of 1,2-propanediol, which accounts for less content, is extracted in the polycondensation stage, so the content in the final copolyester product is much lower than that in the raw material , no poly(trimethylene terephthalate) copolyester with high 1,2-propanediol content was obtained

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • 1, 2-propanediol copolyester polyterephthalate with high 1, 2-propanediol content and preparation method thereof
  • 1, 2-propanediol copolyester polyterephthalate with high 1, 2-propanediol content and preparation method thereof
  • 1, 2-propanediol copolyester polyterephthalate with high 1, 2-propanediol content and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] (1) Add 38.8g of dimethyl terephthalate (DMT), 27.3g of ethylene glycol and 0.04g of zinc acetate dihydrate into a three-necked flask equipped with a mechanical stirring device. After all the materials were added, equip the flask with a condensation device, vacuumize and fill with nitrogen three times to remove the oxygen in the reaction vessel. The transesterification reaction was stirred at 200°C for 1h and at 210°C for 1h. During this process, methanol was distilled out from the reaction mixture as a by-product with a yield of 98.9%, and the product was cooled under nitrogen protection for standby use to obtain diethylene glycol terephthalate with complete transesterification.

[0026] (2) Add 38.8 g of dimethyl terephthalate (DMT), 33.5 g of 1,2-propanediol and 0.05 g of tetra-n-butyl titanate into a three-necked flask equipped with a mechanical stirring device. After all the materials were added, equip the flask with a condensation device, vacuumize and fill with ...

Embodiment 2

[0029] (1) Add 19.4 g of dimethyl terephthalate (DMT), 19.8 g of 1,4-butanediol and 0.02 g of tetra-n-butyl titanate into a three-necked flask equipped with a mechanical stirring device. After all the materials were added, equip the flask with a condensation device, vacuumize and fill with nitrogen three times to remove the oxygen in the reaction vessel. The transesterification reaction was stirred at 200°C for 1h and at 210°C for 1h. During this process, methanol was distilled out from the reaction mixture as a by-product with a yield of 98.9%, and the product was cooled under the protection of nitrogen for standby use to obtain dibutylene terephthalate with complete transesterification.

[0030](2) Add 58g of dimethyl terephthalate (DMT), 50g of 1,2-propanediol and 0.05g of tetra-n-butyl titanate into a three-necked flask equipped with a mechanical stirring device. After all the materials were added, equip the flask with a condensation device, vacuumize and fill with nitrog...

Embodiment 3

[0033] (1) Add 194g of dimethyl terephthalate (DMT), 167.2g of 1,3-propanediol, 0.065g of tetra-n-butyl titanate, and 0.1g of manganese acetate into a three-necked flask equipped with a mechanical stirring device. After all the materials were added, equip the flask with a condensation device, vacuumize and fill with nitrogen three times to remove the oxygen in the reaction vessel. The transesterification reaction was stirred at 200°C for 1h and at 210°C for 1h. During this process, methanol was distilled out from the reaction mixture as a by-product with a yield of 98.9%, and the product was cooled under nitrogen protection for standby use to obtain dipropylene glycol terephthalate with complete transesterification.

[0034] (2) Add 332g of terephthalic acid (PTA), 228g of 1,2-propylene glycol and 0.3g of tetraisopropyl titanate into a 2L reaction kettle. After all the materials are added, fill with nitrogen and deflate , to remove the oxygen in the reactor. Fill with nitrog...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
glass transition temperatureaaaaaaaaaa
glass transition temperatureaaaaaaaaaa
glass transition temperatureaaaaaaaaaa
Login to View More

Abstract

The invention relates to 1, 2-propanediol copolyester polyterephthalate with high 1, 2-propanediol content and a preparation method thereof. The method comprises the following steps of: reacting a dimethyl terephthalate monomer with linear glycol under the catalysis of an ester exchange catalyst to obtain bilinear glycol ester terephthalate with complete ester exchange; reacting the dimethyl terephthalate monomer with a 1, 2-propanediol monomer under the catalysis of an ester exchange catalyst and a polycondensation catalyst; mixing the mixture and the bilinear glycol ester terephthalate; andperforming polycondensation under reduced pressure to obtain a sample. Compared with the prior art, the method has the advantage that: the problem of low copolyester content due to large reaction steric hindrance and low activity of 1, 2-propanediol in the process of reacting the 1, 2-propanediol and the linear glycol with terephthalic acid to form the copolyester is solved; and the obtained product has the advantages of meeting a high-temperature using environment along with stable forming size and high transparency.

Description

technical field [0001] The invention relates to a polyester and a preparation method thereof, in particular to a polyterephthalic acid 1,2-propylene glycol copolyester with high 1,2-propanediol content and a preparation method thereof. Background technique [0002] Polypropylene terephthalate (PTT) was first synthesized in 1941 by Whinfield and Dickson of the British Calico Printing and Dyeing Workers Association (CPA). However, it was not until the 1990s that the US Shell Company developed low-cost 1,3-propanediol, and the industrial production of PTT began. PTT is a new type of polyester with excellent performance. In addition to the chemical resistance of PET fiber, it also has excellent elastic recovery and recovery rate. Its inherent stain resistance, antistatic property and color fastness are also very good. , has a wide range of uses in fiber, manufacturing containers, films, etc. [0003] 1,2-propanediol is an isomer of 1,3-propanediol and has a similar structure t...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C08G63/183C08G63/78
Inventor 赵冬云杨桂生
Owner SHANGHAI GENIUS ADVANCED MATERIAL (GRP) CO LTD
Features
  • R&D
  • Intellectual Property
  • Life Sciences
  • Materials
  • Tech Scout
Why Patsnap Eureka
  • Unparalleled Data Quality
  • Higher Quality Content
  • 60% Fewer Hallucinations
Social media
Patsnap Eureka Blog
Learn More