Method for producing aliphatic polyester and the aliphatic polyester
A technology of aliphatic polyester and aliphatic dicarboxylic acid, applied in the field of aliphatic polyester, can solve the problems of reduced biodegradability of polyester, weak thermal stability, difficult to use catalyst, etc., to achieve thermal stability and tensile strength. Excellent elongation, effect of reducing thermal decomposition and thermal deterioration
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[0135] During the preparation process of the present invention or for the obtained polyester, various additives such as heat stabilizers, antioxidants, crystallization nucleating agents, flame retardants, antistatic agents can be added within the range of not destroying properties during polymerization , Demolding, UV absorbers, etc.
[0136] Moreover, when molding, in addition to the above-mentioned various additives, reinforcing agents and fillers can be added, such as glass fiber, carbon fiber, titanium whisker, mica, talc, CaCO 3 、TiO 2 or silica, which can then be molded.
[0137] Since the polyester obtained by the method of the present invention is excellent in heat resistance and color tone, and is also excellent in hydrolysis resistance and biodegradability, and can be produced at low cost, it is suitable for various Applications for film and injection molded products.
[0138] Specific applications include injection molded products (such as trays for fresh food, c...
Embodiment 1
[0146] Catalyst preparation
[0147] Weigh 300ml of ion-exchanged water in a 1L beaker. After the beaker was cooled in an ice bath, 20ml of titanium tetrachloride (TiCl 4 ). After the dropwise addition, when the generation of hydrogen chloride ceased, the beaker was removed from the ice bath. Add 4.1 g of magnesium chloride hexahydrate (MgCl 2 ·6H 2 O), and dissolve it. Furthermore, 22.2 g of tetraethoxysilane (Si(OC 2 h 5 ) 4 ). Then, under the stirring beaker, 4N ammonia water was added dropwise until the pH of the liquid in the beaker reached 7.4. The precipitate formed by the dropwise addition was suction-filtered, washed, dried at 80° C. under reduced pressure, and pulverized to 100 μm or less to obtain a composite oxide catalyst. The Ti:Mg:Si atomic ratio of the feed in this example was 60:7:33.
[0148] melt polycondensation
[0149] Add 100.3g (0.85mol) of succinic acid, 81.9g (0.91mol) of 1,4-butanediol, 0.37g (2.8 ×10 -3 mol, 0.33 mol% relative to succi...
Embodiment 2
[0152] Catalyst preparation
[0153] In addition to using titanium tetrachloride (TiCl 4 ), using magnesium chloride hexahydrate (MgCl 2 ·6H 2 O) and tetraethoxysilane (Si(OC 2 h 5 ) 4 ), carry out the same operation as in Example 1. The Ti:Mg:Si atomic ratio of the feed in this example was 14:14:72. The average particle diameter of the obtained composite oxide catalyst was 44 μm.
[0154] melt polycondensation
[0155] Except for using 0.18 g of the composite oxide catalyst prepared in Example 2 as a catalyst, the same operations as in Example 1 were performed for the starting material charge. Then, the internal system was made into a nitrogen atmosphere by nitrogen substitution under reduced pressure.
[0156] Then, the internal system was heated to 220° C. with stirring, and reacted at this temperature for 1 hour. Then, the temperature was raised to 230 °C within 30 minutes, and at the same time the pressure was reduced to 0.07×10 within 1 hour and 30 minutes 3 P...
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