Polypropylene modified composition and modified polypropylene
A technology of polypropylene and composition, applied in the field of polypropylene modified composition, which can solve the problems of poor thermal stability and achieve good thermal stability and good comprehensive performance
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[0026] According to a preferred embodiment of the present invention, the composition content of the mixed C4 may be 5-10% by weight of 1-butene, 5-15% by weight of isobutene, 10-20% by weight of 1,3-butadiene, 1 , 5-15% by weight of 2-butadiene, 0.5-5% by weight of n-butane, 0.5-2% by weight of isobutane, 20-40% by weight of cis-2-butene, 2-10% by weight of trans-2-butene %, vinyl acetylene 5 to 20% by weight.
[0027] According to another preferred embodiment of the present invention, the composition content of the mixed C4 may be 0.1-2% by weight of 1-butene, 10-30% by weight of isobutene, 0.01-0.1% by weight of 1,3-butadiene, 0.5 to 5% by weight of n-butane, 30 to 40% by weight of isobutane, 20 to 40% by weight of cis-2-butene, and 5 to 20% by weight of trans-2-butene.
[0028] According to another preferred embodiment of the present invention, the composition content of the mixed C4 may be 5-15% by weight of 1-butene, 0.5-3% by weight of isobutene, 20-30% by weight of n-b...
Embodiment 1-5
[0065] Embodiment 1-5, optimization example 1-3
[0066] (1) Preparation of butene-maleic anhydride copolymerized microspheres:
[0067] Under nitrogen protection, 14kg of mixed C4A is passed into a 200L reactor containing 20kg of maleic anhydride, 2.4kg of azobisisobutyronitrile and 100L of isoamyl acetate to carry out a copolymerization reaction. The reaction pressure is 0.9MPa, the copolymerization reaction temperature is 70°C, and the copolymerization reaction time is 6h;
[0068] Pass the copolymerization reaction product into the flash separator for gas-liquid separation at 25°C and 0MPa. The obtained liquid-solid mixture continues to be separated in the centrifuge at 4000rpm and centrifuged for 20min to obtain a solid product. Wash with hexane, filter the obtained filter cake through a sand core funnel and vacuum dry at 90° C. for 8 hours to obtain a copolymer powder. The copolymer powder was tested, wherein the content of maleic anhydride structural units was 48 mol ...
Embodiment 6-9
[0071] Embodiment 6-9, optimization example 4-5
[0072] (1) Preparation of butene-maleic anhydride copolymerized microspheres:
[0073] Under nitrogen protection, 13.5kg of mixed C4B is passed into a 200L reactor containing 20kg of maleic anhydride, 4kg of dibenzoyl peroxide and 100L of isoamyl acetate in an organic reaction tank for copolymerization. The reaction pressure is 1MPa, the copolymerization reaction temperature is 80°C, and the copolymerization reaction time is 6h;
[0074]Pass the copolymerization reaction product into the flash separator to carry out gas-liquid separation at 30°C and 0MPa conditions, and the obtained liquid-solid mixture continues to carry out liquid-solid separation in the centrifuge at 4000rpm and centrifugation for 20min to obtain a solid product, which is then used After washing with hexane, the filter cake was vacuum-dried at 90° C. for 8 hours to obtain a copolymer powder. The copolymer powder was tested, wherein the content of maleic an...
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