Polypropylene alloy and preparation method thereof
A polypropylene and random polypropylene technology, applied in the field of polypropylene alloys and their preparation, can solve the problems of decreased rigidity, difficulty in taking into account the rigidity and toughness of alloys at the same time, achieve high flexural modulus, reduce product costs, and simplify process flow Effect
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Embodiment 1
[0016] (1) Pre-polymerization process
[0017] Preliminary polymerization was carried out on a 5L bulk polymerization evaluation apparatus. Firstly, the reaction system was evacuated for 5 times with high-purity nitrogen, and then replaced with propylene for 3 times. Add molecular weight modifier 100mmol in the system, with the Ziegler-Natta spherical catalyst 20mg of activation (main composition has: titanium content is 2.5%, chlorine 58%, magnesium 15%, diester or diether 14.0%, particle diameter 20~150μ Spherical particles), cocatalyst Al(C 2 h 5 ) 3 (the molar ratio of the aluminum in the cocatalyst to the titanium in the Zeigler-Natta catalyst is 1000), the external electron donor diphenyldimethoxysilane, (silicon in the diphenyldimethoxysilane and the Zeigler-Natta catalyst The molar ratio of titanium is 100), add in the catalyst feed tank. The catalyst is flushed into the reaction system with liquid propylene, and the amount of propylene added is 1300 g. The react...
Embodiment 3、4、5、6、7、8
[0023] In Examples 3, 4, 5, 6, 7, and 8, the catalyst ratio is a homogeneous single titanocene catalyst 1-phenyl-2,3,4,5-tetramethylcyclopentadienyl-(2, The weight ratio of 4,6-tri-tert-butylphenoxy)-titanium dichloride to Ziegler-Natta catalyst (industrial DQ-2) is 1:1.5; 1:4; 1:6; 1:8; 1 : 10; 0: 1, the molecular weight modifier hydrogen is fixed at 100mmol, and other operating conditions are exactly the same as in Example 1, and the results are listed in Table 1.
[0024] Example
[0025] From the results of propylene polymerization catalyzed by catalysts with different proportions, the impact performance of the polymer decreases with the decrease of the metallocene catalyst addition. This is because the high molecular weight random polypropylene in the polymer The content is reduced; compared with pure isotactic polypropylene, the impact strength is increased by 2-4 times.
Embodiment 9、10、11、12、13、14、15
[0027] In Examples 9, 10, 11, 12, 13, 14, 15, the fixed catalyst ratio is 1-phenyl-2,3,4,5-tetramethylcyclopentadienyl-(2,4,6 -tri-tert-butylphenoxy group)-titanium dichloride catalyst and Ziegler-Natta catalyst weight ratio are 1: 4, the add-on of molecular weight modifier hydrogen is respectively 0,60,100,130,160,200,260mmol, Other operating conditions are identical with embodiment 1, and the results are listed in table 2.
[0028] Example
[0029] From the results of the examples, as the amount of hydrogen added increases, the melt flow index of the polymer increases, the average molecular weight decreases, the improvement of the impact resistance of the polymer gradually decreases, and the impact performance of low-index products increases. Very large, the hydrogen tuning sensitivity of the alloy catalyst system is very good.
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