A kind of propylene prepolymerization method
A technology of propylene polymerization and pre-polymerization, which is applied in the field of polyolefin polymerization, can solve the problems of high operating costs and large investment in equipment, achieve the effects of low operating costs, solve temperature fluctuations, and improve capacity
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Embodiment 1
[0029] Pre-polymerization conditions:
[0030] The pre-polymerization reactor is a stirred autoclave with a volume of 2L, and the fresh propylene flow rate is 12.5Kg / hr; the external electron donor adopts CHMDMS (methylcyclohexyldimethoxysilane), and the flow rate is 0.6g / hr; CN200510109095.1 prepared by the method of Example 5) feed rate 1.8g / hr (diluted to 30% white oil slurry); triethylaluminum feed rate 3.6g / hr, the material takes the way of top in and bottom out through the reactor.
[0031] 1) The catalyst, activator, and external electron donor continuously enter the reactor for liquid-phase bulk polymerization of propylene;
[0032] 2) The pre-polymerization temperature is 35°C;
[0033] 3) The pre-polymerization time is 5 minutes;
[0034] 4) The pressure of the polymerization reaction is greater than the saturated vapor pressure of propylene at the prepolymerization temperature, so as to maintain a full tank liquid phase operation.
[0035] The prepolymerization r...
Embodiment 2
[0047] Pre-polymerization conditions:
[0048] The pre-polymerization reactor is a stirred autoclave with a volume of 2L, and the fresh propylene flow rate is 12Kg / hr; the external electron donor adopts DIPDMS (diisopropyldimethoxysilane), and the flow rate is 0.55g / hr; the catalyst (according to CN200510109095 .1 prepared by the method of Example 5) feed rate 1.7g / hr (diluted to 30% white oil slurry); triethylaluminum feed rate 3.6g / hr, the material takes the mode of going in and out through the reactor.
[0049] 1) The catalyst, activator, and external electron donor continuously enter the reactor for liquid-phase bulk polymerization of propylene;
[0050] 2) The pre-polymerization temperature is 40°C;
[0051] 3) pre-polymerization time 3min;
[0052] 4) The pressure of the polymerization reaction is greater than the saturated vapor pressure of propylene at the prepolymerization temperature, so as to maintain a full tank liquid phase operation.
[0053] The prepolymeriza...
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