Preparation method of propene polymer composition
A technology of propylene polymer and composition, which is applied in the field of preparation of propylene polymer composition, can solve problems such as low isotacticity, food contamination, and limited application range, so as to reduce possibility, facilitate processing, and smooth production Effect
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Embodiment 1
[0022] Example 1: In the reactor fully replaced by high-purity nitrogen, 60kg of magnesium chloride, 112L of toluene, 50L of epichlorohydrin, and 157L of tributyl phosphate (TBP) were added in sequence. The temperature was raised to 50°C with stirring and maintained for 2.5 hours, and the solid was completely dissolved. Add 17.5 kg of phthalic anhydride and continue to maintain for 1 hour. Cool the solution to below -25°C and add TiCl dropwise within 1 hour 4 700L. The temperature was raised slowly to 80°C, and solids were gradually precipitated during the heating process. Add 75mol of 2,4-pentanediol dibenzoate to 80°C, and maintain the temperature for 1 hour. After filtration, 700 l of toluene was added and washed twice to obtain a solid precipitate. Then add toluene 750L, TiCl 4 500L, heated up to 100°C, treated for two hours, drained the filtrate, then added 750L of toluene, TiCl 4 500L, heated up to 100°C, treated for two hours, and drained the filtrate. Then add...
Embodiment 2
[0023] Example 2: Replace 2,4-pentanediol dibenzoate with 3,5-heptanediol dibenzoate, and add 75mol of 3,5-heptanediol dibenzoate at 80°C, other conditions are the same as the implementation example 1.
Embodiment 3
[0026] Example 3 : A continuous test was carried out on a Mitsui Hypol process unit containing two liquid phase tanks and two gas phase tanks, each with a volume of 32m 3 , 32 m 3 , 105m 3 and 165 m 3 . First, the catalyst prepared in Example 1 was prepolymerized with propylene in a hexane solution at a temperature lower than 15°C and the molar ratio of triethylaluminum to titanium in the main catalyst was 3 to obtain a prepolymer with a prepolymerization ratio of 3. , and then it is continuously added to the reaction device, and according to the activity, the addition amount of the catalyst is adjusted to keep the production load of the device at 10 tons of polymer / hour. The molar ratio of main catalyst (based on titanium content), co-catalyst component triethylaluminum and methylcyclohexyldimethoxysilane is 1 / 50 / 8, only ethylene is added to the fourth reactor, ethylene The addition amount is 48kg / h, and the reaction temperatures of the four tanks are 70°C, 65°C, 75°C, ...
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