Catalyst for preparing polybutylene succinate and copolyesters thereof and preparation method thereof

A technology of polybutylene succinate and catalyst, applied in chemical instruments and methods, inorganic chemistry, titanium compounds, etc., can solve the problems of inconvenient use of catalysts, low catalyst activity, high addition amount, etc., and achieve good industrial application prospects and value, easy long-term storage, high catalytic activity effect

Active Publication Date: 2010-03-17
SHANGHAI HUAMING HI TECH GRP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In actual production, a single titanate catalyst often cannot fully meet the requirements, and needs to be compounded with other compounds to form a composite catalyst
[0005] There are certain technical defects in the above-mentioned catalyst systems, which are mainly manifested in: (1) The activity of the catalyst is low, and the addition amount is high, which affects the quality of the final product
Titanium alkoxide catalysts are usually used, and the addition concentration of its active ingredient (titanium element) exceeds 500ppm in terms of polybutylene succinate (that is, 500×10 -6 gTi / gPBS, the same below), sometimes even more than 700ppm, such a high addition will cause more side reactions and increase the melt mass flow rate of the product, decrease the mechanical properties, and seriously yellow the color
(2) The catalyst is inconvenient to use, which brings difficulties to the production operation
Titanium alkoxides will precipitate when they meet water at room temperature, and in the synthesis process of PBS, the product of the esterification stage is water, so titanium alkoxides as catalysts can only be added after esterification and not after esterification. On the other hand, multiple substances are used as catalysts at the same time, which also causes certain difficulties in addition. Operators need to prepare catalysts in advance, and the process is far less convenient than using a single catalyst

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Add 50g1,4-butanediol (0.55mol) in the 250ml flask that stirring paddle and condensing device are housed, dissolve 1.73g calcium acetate (0.0098mol) wherein, then add 29g n-butyl titanate ( 0.0852mol) and 31.51g ethanol (0.685mol), react at 80°C for 2.5h, after distilling off small molecules, add 2.04g orthosilicate ethyl ester (0.0098mol) and 8.22g tartaric acid (0.0548mol) to the reaction system , reacted at 80°C for 2.5h, and after distilling off small molecules, a liquid catalyst containing 5.12% titanium was prepared.

Embodiment 2

[0037] Add 50g of 1,4-butanediol (0.55mol) to a 250ml flask equipped with a stirring paddle and a condensing device, dissolve 2.4g of manganese acetate (0.0098mol) into it, then add 19.44g of isopropyl titanate to the solution (0.0685mol) and 31.51g ethanol (0.685mol), react at 110°C for 0.5h. After distilling off small molecules, add 1.02g tetraethyl orthosilicate (0.0049mol) and 12.76g trimethyl phosphite (0.1028mol) to the reaction system, react at 110°C for 0.5h, and distill off small molecules, that is A liquid catalyst containing 4.14% titanium was prepared.

Embodiment 3

[0039]Add 50g of 1,4-butanediol (0.55mol) to a 250ml flask equipped with a stirring blade and a condensing device, dissolve 2.2g of zinc acetate (0.01mol) into it, and then add 22.80g of n-butyl titanate to the solution (0.067mol) and 92.46g ethanol (2.01mol), react at 180°C for 1h. After the small molecule was removed by distillation, 8.41g citric acid (0.04mol), 5.10g tartaric acid (0.034mol), 2.08g tetraethyl orthosilicate (0.01mol) and 6.74g triethyl phosphate (0.037mol) were added to the reaction system ), reacted at 180° C. for 1 h, and distilled off small molecules to obtain a liquid catalyst containing 4.02% titanium.

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Abstract

The invention provides a catalyst for preparing polybutylene succinate and copolyesters thereof and a preparation method thereof. The preparation method comprises the following steps: (1) adding titanium alkoxides, silica-alkoxides, dibastic alcohol and a metal cocatalyst into solution for reaction at a temperature of between 80 and 180DEG C, and separating and removing unreacted substances and micromolecular products in a reaction system; and (2) adding a complexing agent for continuous reaction and collecting the catalyst in reaction products. Or the preparation method comprises the following steps: (1) adding titanium alkoxides, dibastic alcohol and a metal cocatalyst into solution for reaction at a temperature of between 80 and 180DEG C, and separating and removing unreacted substancesand micromolecular products in a reaction system; and (2) adding silica-alkoxides and a complexing agent for continuous reaction and collecting the catalyst in reaction products. The catalyst has high catalytic activity, low addition volume, good product quality, no reaction when meeting water at normal temperature, easy long-term storage and good industrial application prospect and value.

Description

technical field [0001] The invention relates to catalysts for the preparation of polybutylene succinate and its copolyesters. Background technique [0002] Aliphatic polyester has attracted extensive attention and research because of its good biodegradability and no pollution to the environment. Among them, polybutylene succinate (PBS) and its copolyester have become the easiest kind of aliphatic polyester to realize practical application due to their good mechanical properties and processing properties, and are currently the focus of attention in the industry. . [0003] The production of polybutylene succinate and its copolyester generally adopts two methods: chain extension method and direct polycondensation method. The chain extension method is to use the chain extender to react with the organic groups of the polyester to increase the molecular weight of the polyester. The main chain extender used at present is the substance of diisocyanocyanate alkoxide, because this...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G63/82C08G63/16
CPCC08G63/85C01G23/00C08G63/16Y10T29/49345
Inventor 孔凡滔杨景辉吴秋芳马新胜李福清
Owner SHANGHAI HUAMING HI TECH GRP
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