Method for synthesizing polyethylene
A technology of polyethylene and comonomer, applied in the field of olefin polymerization, can solve the problems of detonation, unstable performance of special materials, equipment shutdown, etc., and achieve the effect of reducing detonation
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Embodiment 1
[0029] On the 50kg / h gas-phase fluidized bed process device, a dry powder metallocene catalyst (being a carrier type metallocene catalyst, with silica gel as a carrier, an active center metal zirconium content of 0.35wt%, and a cocatalyst of triisobutylaluminum / boron) is adopted. Acid salt, Al / Zr molar ratio is 142), active 18000gPE / gcat, catalyst initiation temperature 55 ℃, comonomer 1-hexene, its concentration 16% mol, target product is 0.910-0.914g / cm 3 VLDPE products.
[0030] The setting method of catalyst addition is as follows:
[0031] (1) Before the catalyst is injected, set the system temperature to 48°C; (2) The catalyst is transported by nitrogen flow, the catalyst feed rate is 0.8g / h, and the heating rate is 1.0°C / h; (3) When the reactor inlet temperature reaches 60°C , the reactor bed pressure difference reaches the following range: 0.2KPa-0.4KPa for the first stage, 0.4KPa-0.6KPa for the second stage, 0.8KPa-1.8KPa for the third stage, 1.0KPa-1.4KPa for the fo...
Embodiment 2
[0038] On the 50kg / h gas-phase fluidized bed process device, a dry powder metallocene catalyst (being a carrier type metallocene catalyst, with silica gel as a carrier, an active center metal zirconium content of 0.35wt%, and a cocatalyst of triisobutylaluminum, Al / Zr molar ratio is 160), activity 20000gPE / gcat, catalyst initiation temperature 50 ℃, comonomer 1-hexene, concentration 18% mol, target product is 0.890-0.912g / cm 3 VLDPE and POE mixed products.
[0039] The setting method of catalyst addition is as follows:
[0040] (1) Before the catalyst is injected, set the system temperature to 45°C; (2) The catalyst is transported by nitrogen flow, the catalyst feed rate is 0.7g / h, and the heating rate is 0.8°C / h; (3) When the reactor inlet temperature is 58°C, The pressure difference of the reactor bed reaches the range: the first stage is 0.2KPa-0.4KPa, the second stage is 0.4KPa-0.6KPa, the third stage is 0.8KPa-1.8KPa, the fourth stage is 1.0KPa-1.4KPa, and the fifth sta...
Embodiment 3
[0047] On the 50kg / h gas-phase fluidized bed process device, dry powder Z-N catalyst (Al / Ti molar ratio is 180, Mg / Ti molar ratio is 2.2, internal electron donor is diisooctyl phthalate, D50 is 34μm) , activity 8000gPE / gcat, catalyst initiation temperature 70°C, comonomer 1-butene, concentration 12% mol, target product 0.915-0.935g / cm 3 LLDPE products.
[0048] The setting method of catalyst addition is as follows:
[0049] (1) Before the catalyst is injected, set the system temperature to 65°C; (2) The catalyst is transported by nitrogen flow, the catalyst feed rate is 1.2g / h, and the heating rate is 2°C / h; (3) When the reactor inlet temperature is 60°C, The pressure difference of the reactor bed reaches the range: the first stage is 0.2KPa-0.4KPa, the second stage is 0.4KPa-0.6KPa, the third stage is 0.8KPa-1.8KPa, the fourth stage is 1.0KPa-1.4KPa, and the fifth stage is 10.2KPa-12.4KPa. The feed rate of the catalyst is set at 2.0-3.2g / h, and the heating rate is 2.5°C / h; ...
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