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
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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
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