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Continuous production system and preparation method of biodegradable copolyester and copolyester

A biodegradation and production system technology, applied in the field of polymer material synthesis, can solve the problems of large reaction temperature gradient, high content of terminal carboxyl groups, and reduced randomness of aliphatic-aromatic copolyesters, etc. The effect of low content of terminal carboxyl groups and high intrinsic viscosity

Active Publication Date: 2021-05-14
CHINESE TEXTILE ACAD
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Problems solved by technology

[0003] At present, the continuous polymerization production process of biodegradable aliphatic-aromatic copolyester mainly includes parallel esterification method and co-esterification method. Parallel esterification process refers to Aliphatic dibasic acids and aromatic dibasic acids are esterified separately in two esterification tanks, and the obtained polyester oligomers enter the polycondensation system together for pre-condensation reaction and final polycondensation reaction to obtain biodegradable fat The advantage of this esterification process is that it can effectively solve the problem of large temperature gradient in the esterification reaction of aliphatic dibasic acid and aromatic dibasic acid, and can realize the synthesis of aliphatic dibasic acid at low temperature. Esterification avoids high-temperature decarboxylation side reactions; however, aliphatic dibasic acids and aromatic dibasic acid esters tend to generate homopolymers with multiple degrees of polymerization in parallel and independent esterification processes, resulting in the final preparation of biodegradable fats The randomness of the aromatic-aromatic copolyester is reduced, and the content of the aromatic dibasic acid ester segment with a sequence length greater than 2 that is not degradable by microorganisms increases
[0004]The co-esterification process refers to the esterification reaction of aliphatic dibasic acid and aromatic dibasic acid in the same reactor and at the same esterification temperature. Then pre-condensation reaction and final polycondensation reaction are carried out sequentially to obtain biodegradable aliphatic-aromatic copolyester. The advantage of this esterification process is that the process is simple, but it is difficult to find a suitable matching temperature. Efficient esterification of acid and aromatic dibasic acid at the same time may easily cause sublimation or decarboxylation of aliphatic dibasic acid due to high esterification temperature or insufficient esterification of aromatic dibasic acid due to low esterification temperature, resulting in Pipeline clogging accidents are prone to occur during the continuous polymerization of biodegradable aliphatic-aromatic copolyesters, and the intrinsic viscosity of the produced sliced ​​products is low and the content of terminal carboxyl groups is high, which makes biodegradable aliphatic-aromatic copolyesters The processing use of polyester is limited

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  • Continuous production system and preparation method of biodegradable copolyester and copolyester
  • Continuous production system and preparation method of biodegradable copolyester and copolyester

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Embodiment 1

[0054] Such as figure 1 , shown in 2 and 4, the present embodiment provides a kind of continuous production system of biodegradable copolyester, comprises esterification system and polycondensation system, and described esterification system comprises the first esterification kettle and the second Esterification tank; the interior of the first esterification tank is separated into an inner and outer chamber structure by an annular partition 6 that is lower than the height of the still cavity and coaxial with the still cavity, and the reactants in the inner chamber 1 overflow from the top of the partition 6 to the outer chamber 2, and transported from the outer chamber 2 to the second esterification tank; the inside of the second esterification tank is separated into an inner and outer cavity structure by an annular partition 6 that is the same height as the tank cavity and coaxially arranged, and the inner cavity 4 The reactant is sent to the outer cavity 5 through the diversi...

Embodiment 2

[0064] In this embodiment, the production system as described in Example 1 is used to prepare biodegradable copolyester, which specifically includes the following steps:

[0065] (1) The succinic acid slurry prepared by adjusting succinic acid, butanediol and catalyst into an alkyd molar ratio of 2.0:1, wherein the catalyst is titanium, aluminum and phosphorus in a molar ratio of 1:0.5:0.2 The ternary complex, the catalyst is composed of tetrabutyl titanate, aluminum ethylene glycol, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite according to the moles of titanium, aluminum and phosphorus It is prepared after mixing at a ratio of 1:0.5:0.2 and reacting at 200°C for 5 hours; the succinic acid slurry is transported to the inner chamber of the first esterification kettle, and then overflows into the outer chamber to obtain the acid value Butylene succinate of 20mgKOH / g; wherein the reaction temperature of the first esterification tank is 180°C, the reaction pressure is...

Embodiment 3

[0069] In this embodiment, the production system as described in Example 1 is used to prepare biodegradable copolyester, which specifically includes the following steps:

[0070] (1) Adipic acid slurry prepared from adipic acid, butanediol and a catalyst with an alkyd molar ratio of 1.8:1, wherein the catalyst is titanium, aluminum and phosphorus in a molar ratio of 1:0.3:0.1 The ternary compound, this catalyst is to be 1 according to the mol ratio of titanium element, aluminum element and phosphorus element by tetrabutyl titanate, aluminum ethylate, three (2,4-di-tert-butylphenyl) phosphite: Prepared by mixing at a ratio of 0.3:0.1 and reacting at 180°C for 3 hours; transporting the adipic acid slurry to the inner chamber of the first esterification kettle, and then overflowing into the outer chamber to obtain an acid value of 10mgKOH / g butylene adipate; wherein the temperature of the first esterification tank is 220°C, the reaction pressure is 40kPa, the residence time of th...

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Abstract

The invention discloses a continuous production system and a preparation method of biodegradable copolyester and copolyester. An esterification system in the production system comprises a first esterification kettle and a second esterification kettle which are connected in sequence; the interiors of the first esterification kettle and the second esterification kettle are separated into inner and outer cavity structures by an annular partition plate which is coaxially arranged with a kettle cavity so that reactants in the inner cavity are conveyed to the outer cavity through the partition plate, and conveying outside the kettle is completed. According to the preparation method, sequential esterification of aliphatic dibasic acid and aromatic dibasic acid is realized by utilizing inner and outer chamber structures of the first esterification kettle and the second esterification kettle and a specific catalyst, decarboxylation side reaction is effectively avoided, and the sequence length of an aromatic dibasic acid ester chain segment can be effectively controlled not to be higher than 2, the continuously produced aliphatic-aromatic copolyester has the characteristics of good biodegradability, low terminal carboxyl group content and good hue.

Description

technical field [0001] The invention belongs to the technical field of polymer material synthesis, and in particular relates to a continuous production system and preparation method of biodegradable copolyester and copolyester. Background technique [0002] Biodegradable aliphatic-aromatic copolyester is a copolyester of aliphatic dibasic acid and aromatic dibasic acid and aliphatic diol, which has good biodegradability and flexibility of aliphatic polyester It has good heat resistance and mechanical properties with aromatic polyesters, and has been widely used in the production of shopping bags, agricultural mulch films, express packaging bags, garbage bags, disposable lunch boxes and paper cups, etc. [0003] At present, the continuous polymerization production process of biodegradable aliphatic-aromatic copolyester mainly includes parallel esterification method and co-esterification method. The obtained polyester oligomers enter the polycondensation system for pre-conden...

Claims

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Application Information

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IPC IPC(8): B01J19/00C08G63/183C08G63/85C08G63/83C08G63/87
CPCB01J19/00B01J19/0006B01J19/0053C08G63/183C08G63/85C08G63/83C08G63/87B01J2219/00033C08G2230/00Y02W90/10
Inventor 邱志成李鑫王颖金剑钟淑芳武术芳梁颖
Owner CHINESE TEXTILE ACAD
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