Catalyst for producing polybutylene succinate or copolyester thereof, and preparing mehtods of the catalyst

a technology of polybutylene succinate and catalyst, which is applied in the field of catalyst, can solve the problems of limited application of pbs or its copolyesters, high additional amount of catalyst, and inability to meet the production requirements of titanate-based catalysts alon

a technology of polybutylene succinate and catalyst, which is applied in the field of catalyst, can solve the problems of limited application of pbs or its copolyesters, high additional amount of catalyst, and inability to meet the production requirements of titanate-based catalysts alon

US20110162205A1Inactive Publication Date: 2011-07-07SHANGHAI HUAMING HI TECH GRP

Examples

Experimental program
Comparison scheme
Effect test

first embodiment

The First Embodiment

[0031]Consistent with this embodiment, the manufacturing method of the catalyst used in the production of PBS or its copolyesters comprises steps of:

(1) add 50 g of 1,4-butanediol (0.55 mol) into a 250 ml flask which is equipped with propeller and condensing unit, then add 1.73 g of calcium acetate (0.0098 mol) into the flask,

(2) after that, add 29 g of tetra-n-butyl titanate (0.0852 mol) and 31.51 g of ethanol (0.685 mol) into the flask, then conduct the reaction at a temperature of 80° C. for 2.5 hours,

(3) remove small molecular products in the reaction system obtained in step (2) by dilution,

(4) add 2.04 g of tetraethoxysilane (0.0098 mol) and 8.22 g of tartaric acid (0.0548 mol) into the reaction system in step (3) and conduct the reaction at a temperature at a temperature of 80° C. for 2.5 hours;

(5) remove small molecular products in the reaction system obtained in step (4) by dilution and then catalyst in liquid state which contains 5.12% of titanium by wei...

second embodiment

The Second Embodiment

[0032]Consistent with this embodiment, the manufacturing method of the catalyst used in the production of PBS or its copolyesters comprises steps of:

(1) add 50 g of 1,4-butanediol (0.55 mol) into a 250 ml flask which is equipped with propeller and condensing unit, then add 2.4 g of manganese acetate (0.0098 mol) into the flask,

(2) after that, add 19.44 g of tetra-isopropyl titanate (0.0685 mol) and 31.51 g of ethanol (0.685 mol) into the flask, then conduct the reaction at a temperature of 110° C. for 0.5 hours,

(3) remove small molecular products in the reaction system obtained in step (2) by dilution,

(4) add 1.02 g of tetraethoxysilane (0.0049 mol) and 12.76 g of trimethyl phosphite (0.1028 mol) into the reaction system in step (3) and conduct the reaction at a temperature at a temperature of 110° C. for 0.5 hours;

(5) remove small molecular products in the reaction system obtained in step (4) by dilution and then catalyst in fluid state which contains 4.14% of ...

third embodiment

The Third Embodiment

[0033]Consistent with this embodiment, the manufacturing method of the catalyst used in the production of PBS or its copolyesters comprises steps of:

(1) add 50 g of 1,4-butanediol (0.55 mol) into a 250 ml flask which is equipped with propeller and condensing unit, then add 2.2 g of zinc acetate (0.01 mol) into the flask,

(2) after that, add 22.80 g of tetra-n-butyl titanate (0.067 mol) and 92.46 g of ethanol (2.01 mol) into the flask, then conduct the reaction at a temperature of 180° C. for 1 hour,

(3) remove small molecular products in the reaction system obtained in step (2) by dilution,

(4) add 8.41 g of citric acid (0.04 mol), 5.10 g of tartaric acid (0.034 mol), 2.08 g of tetraethoxysilane (0.01 mol) and 6.74 g of triethyl phosphate (0.037 mol) into the reaction system in step (3) and conduct the reaction at a temperature at a temperature of 180° C. for 1 hour;

(5) remove small molecular products in the reaction system obtained in step (4) by dilution and then ...

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Abstract

The present invention provides a catalyst used in the production of PBS or its copolyesters and the preparation method thereof. The method comprises the following steps: (1) adding titanium alkoxide, silicon alkoxide, dihydric alcohol and metal co-catalyst into the solvent and conducting the reaction at a temperature of about 80° C. to 180° C., then removing the unreacted materials and small molecular products in the reaction system; (2) adding complexing agent into the reaction system, then collecting catalyst from the products obtained in this step. Moreover, the method may comprises steps of: (1) adding titanium alkoxide, dihydric alcohol and metal co-catalyst into the solvent and conducting the reaction at a temperature of about 80° C. to 180° C., then removing the unreacted materials and small molecular products in the reaction system; (2) adding silicon alkoxide and complexing agent into the reaction system, then collecting catalyst from the products obtained in this step. The catalyst in the present invention has higher activity and thus the catalyst additional amount is reduced which will improve the quality of the products. Moreover, the catalyst in the present invention could be used alone in the production of PBS or its copolyester without the need for other materials and it won't react with water and thus could be stored for a long time. In sum, the catalyst in the present invention has a broad prospect in industrial application.

Description

FIELD OF THE INVENTION[0001]The present invention relates to a catalyst used in the production of PBS or its copolyesters and the preparation method thereof.BACKGROUND OF THE INVENTION[0002]Aliphatic polyesters has aroused wide attention and research from domestic and foreign scholars because of their great biodegradable and environmentally non-persistent properties. Aliphatic polyesters and in particular poly (butylene succinate) (PBS) even have additional advantage features, such as good mechanical and processing properties. Therefore, PBS, which has enormous application prospect, becomes the focus of attention in industry recently.[0003]Previous attempts at the production of PBS or its copolyesters are generally fall into two kinds of production processes, chain extending process and direct polycondensation process. In the chain extending process, chain extender is added into the reaction system to react with the organic groups of the polyesters in order to increase molecular wei...

Claims

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Application Information

Patent Timeline
07 Jul 2011
Publication
US20110162205A1
IPC
B21D51/16
CPC
C01G23/00; Y10T29/49345; C08G63/85; C08G63/16
Inventors
KONG, FANTAO; YANG, JINGHUI