Transparent LLDPE (linear low density polyethylene) thin-film resin and thin film prepared from same
A film resin, transparent technology, applied in the field of transparent and easy-to-process LLDPE film resin, can solve the problems of low production cost, and achieve the effects of increasing molecular weight, refining crystals, and good transparency
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[0066] Catalyst preparation:
[0067] Using Al 2 o 3 , titanium and F modified porous inorganic carrier SiO 2 Carrier (the carrier can also be replaced by zirconia or thorium oxide), through the step-by-step or co-impregnation method, the vanadium source is impregnated in the porous inorganic carrier SiO 2 on a silica gel carrier to obtain the desired modified catalyst. Immerse about 10-15g of porous silica gel modified by Ti, Al, F, V in basic chromium acetate aqueous solution, wherein the chromium load is 0.1-1wt% of the total weight of the catalyst, after continuous stirring for 3-8 hours , heat up and dry, then roast the silica gel carrier loaded with basic chromium acetate in a fluidized bed at high temperature, remove the physical water of the carrier at the low temperature section, and remove the hydroxyl groups on the silica gel surface at the high temperature section of 500°C-900°C, This high temperature section is maintained for 5-8 hours, and finally under the p...
Embodiment 1
[0071] Add ethylene, 1-butene, 1-hexene, hydrogen, oxygen, nitrogen and a modified supported chromium-based catalyst into a single gas-phase fluidized bed reactor, according to 1-butene and 1-hexene / ethylene The molar ratio is 0.03:1, the molar ratio of 1-butene / 1-hexene is 1:1, the molar ratio of hydrogen to ethylene is 0.001, the oxygen concentration is 140ppb, the polymerization temperature is 80°C, the polymerization pressure is 1.8MPa, and the circulating gas The polymerization reaction was carried out under the technical conditions of speed of 0.60m / s, catalyst addition of 2g / h, and residence time of 2h.
Embodiment 2
[0073] Add ethylene, 1-butene, 1-hexene, hydrogen, oxygen, nitrogen and a modified supported chromium-based catalyst into a single gas-phase fluidized bed reactor, according to 1-butene and 1-hexene / ethylene The molar ratio is 0.03:1, the molar ratio of 1-butene / 1-hexene is 1:1.5, the molar ratio of hydrogen to ethylene is 0.002, the oxygen concentration is 120ppb, the polymerization temperature is 82°C, the polymerization pressure is 1.9MPa, and the circulating gas The polymerization reaction was carried out under the technical conditions of speed of 0.62m / s, catalyst addition of 2g / h, and residence time of 2h.
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