Ultrahigh molecular weight polyethylene resin with high impact strength and preparation method thereof
A polyethylene resin and ultra-high molecular weight technology, which is applied in the field of polymer materials, can solve the problems of reduced room for molecular chain segment activity, increased crystallinity, and reduced impact strength, and achieves excellent mechanical properties and impact resistance.
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Embodiment 1
[0029] Add about 3800g of heptane into a 10L polymerization kettle, set the stirring speed of the polymerization kettle to 400r / min, and fully replace it with high-purity nitrogen under stirring. Then the polymerization kettle was heated to about 60°C, and then 80ml of cocatalyst triethylaluminum and 10ml of diphenyldiethoxysilane were added, stirring was continued and the temperature was raised to 65°C, then 245mg of Z-N main catalyst was added, and the speed was increased to 800r / min, continue to add about 10g functional monomer 1-hexene, and then continuously feed ethylene. During the polymerization process, the temperature of the kettle was controlled at 68-70° C., the pressure of the kettle was maintained at 0.4 MPa, and the polymerization time was 2 hours. The obtained material was processed by distillation to remove the heptane to obtain 2.5 kg of the polymer product.
Embodiment 2
[0031] Add about 3800g of heptane into a 10L polymerization kettle, set the stirring speed of the polymerization kettle to 400r / min, and fully replace it with high-purity nitrogen under stirring. Then the polymerization kettle was heated to about 60°C, and then 80ml of cocatalyst triethylaluminum and 10ml of diphenyldiethoxysilane were added, stirring was continued and the temperature was raised to 65°C, then 245mg of Z-N main catalyst was added, and the speed was increased to 800r / min, first continuously feed about 6L propylene, and then continuously feed ethylene. During the polymerization process, the temperature of the kettle was controlled at 68-70° C., the pressure of the kettle was maintained at 0.4 MPa, and the polymerization time was 2.5 hours. The obtained material was processed by distillation to remove the heptane to obtain 3.0 kg of the polymer product.
Embodiment 3
[0033] Add about 3800g of heptane into a 10L polymerization kettle, set the stirring speed of the polymerization kettle to 400r / min, and fully replace it with high-purity nitrogen under stirring. Then the polymerization kettle was heated to about 60°C, and then 85ml of cocatalyst tripropylaluminum and 10ml of diphenyldimethoxysilane were added, and the stirring was continued and the temperature was raised to 65°C, then 260mg of Z-N main catalyst was added, and the speed was increased to 800r / min, first continuously feed about 6L propylene, and then continuously feed ethylene. During the polymerization process, the temperature of the kettle was controlled at 66-68° C., the pressure of the kettle was maintained at 0.4 MPa, and the polymerization time was 3 hours. The obtained material was processed by distillation to remove the heptane to obtain 2.6 kg of the polymer product.
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