Method for preparing impact-resistant polypropylene material with high melt strength
A polypropylene material, high melt strength technology, applied in the field of polypropylene material preparation, can solve the problems of limiting polypropylene, insufficient toughness and impact resistance, etc., and achieve the effect of improving toughness and high melt strength
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Embodiment 1
[0068] The propylene polymerization reaction is carried out on a polypropylene unit, and the main equipment of the unit includes a prepolymerization reactor, a first loop reactor, a second loop reactor and a third gas phase reactor. The polymerization method and steps are as follows.
[0069] (1) Prepolymerization reaction
[0070] The main catalyst (DQC-401 catalyst, provided by Beijing Aoda Branch of Sinopec Catalyst Company), co-catalyst (triethylaluminum), and the first external electron donor (diisopropyldimethoxysilane, DIPMS) were tested at 6 °C , After 20min pre-contact, continuously add to the continuous stirred tank type pre-polymerization reactor for pre-polymerization reactor. The flow of triethylaluminum (TEA) entering the prepolymerization reactor is 6.33g / hr, the flow of diisopropyldimethoxysilane is 0.3g / hr, the flow of main catalyst is 0.6g / hr, and the ratio of TEA / DIPMS is 50 (mol / mol). The pre-polymerization is carried out in the bulk environment of the p...
Embodiment 2
[0078] The catalyst used in embodiment 2, pre-complexation, polymerization process conditions and auxiliary agent formula and add-on are the same as embodiment 1. The difference from Example 1 is that the comonomer ethylene in the first stage and the second stage in the first step is changed to 1-butene, and the addition amount of the first and second ring pipes is 10 mol%. The obtained polymer analysis results and polymer physical properties are listed in Table 1 and Table 2.
Embodiment 3
[0080] The catalyst used in embodiment 3, pre-complexation, polymerization process conditions and auxiliary agent formula and addition are the same as embodiment 1. Difference with embodiment 1 is: the comonomer ethylene of the first stage and the second stage in the first step is changed into ethylene+1-butene, the ethylene addition of the first and the second ring pipe is 6000ppm, The addition amount of 1-butene is 5mol%. . The obtained polymer analysis results and polymer physical properties are listed in Table 1 and Table 2.
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