Preparation method of high-isotacticity alloy material
A technology of high-isotactic polybutene and polybutene alloy, which is applied in the production of bulk chemicals and energy input, can solve the problems of not meeting the development prospect of green synthetic chemistry, low polymerization temperature, etc. The effect of uniform diameter distribution and less public works
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Embodiment 1
[0041] The entire polymerization system was evacuated and replaced with vacuum nitrogen.
[0042] 1) Propylene prepolymerization:
[0043] The catalyst used is a titanium tetrachloride catalyst supported by magnesium dichloride, wherein the catalyst has a titanium loading amount of 2.8 wt%, and contains 10 wt% of internal electron donor diisobutyl phthalate.
[0044] Polymerization grade liquid phase propylene monomer (feed rate is 1.6kg / hr), triethylaluminum (feed rate is 20g / hr), external electron donor cyclohexylmethyldimethoxysilane (feed rate is 0.8g / hr), hydrogen (feed amount is 22g / hr), main catalyst (feed amount is 2g / hr) enter the high-speed mixer, and the material enters the pipe at a speed of 3L / hr after mixing. A pre-polymerization tubular reactor with a volume of 3 L, a pre-polymerization temperature of 50° C., and a residence time of 1 h. Then the unreacted propylene monomer and hydrogen are separated by a separation device to obtain active polypropylene partic...
Embodiment 2
[0050] The entire polymerization system was evacuated and replaced with vacuum nitrogen.
[0051] 1) Propylene prepolymerization:
[0052] The catalyst used is a titanium tetrachloride catalyst supported by magnesium dichloride, wherein the catalyst has a titanium loading amount of 2.8 wt%, and contains 10 wt% of internal electron donor diisobutyl phthalate.
[0053] Polymerization grade liquid phase propylene monomer (feed amount is 12kg / hr), triethylaluminum (feed amount is 15g / hr), external electron donor dicyclohexyldimethoxysilane (feed amount is 0.4g / hr), the main catalyst (feed rate is 5g / hr) enters the high-speed mixer, and the mixed material enters the prepolymerization tubular reactor that the tube length is 100 meters and the volume is 20L at a speed of 100mL / m, and the prepolymerization temperature is 20L. 90°C, the residence time is 2h. Then the unreacted propylene monomer and hydrogen are separated by a separation device to obtain active polypropylene particle...
Embodiment 3
[0059] The entire polymerization system was evacuated and replaced with vacuum nitrogen.
[0060] 1) Propylene prepolymerization:
[0061] The aluminum alkyl used is diethylaluminum chloride, hydrogen gas (feed rate is 2g / hr), and the prepolymerization temperature is 10°C, and the others are the same as in Example 2.
[0062] 2) Polymerization of butene:
[0063] The polymerization temperature of the tubular reactor is 50°C, the mass ratio of hydrogen to butene is 0.3:100, the polymerization temperature of the horizontal self-cleaning reactor is 50°C, and the others are the same as in Example 2.
[0064] 3) Extrusion:
[0065] 100g anti-aging agent DLTDP, the length-to-diameter ratio of the twin-screw extruder used is 50:1, the extrusion and granulation conditions are: 140°C in zone 1, 160°C in zone 2, 170°C in zone 3, 185°C in zone 4, 190°C in zone 5 , head 190 ℃, rotating speed 10r / min, others are the same as embodiment 2. The experimental results are listed in Table 1. ...
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