Polymer composition and article
A technology of polymers and compositions, applied in the fields of polyolefin compositions, cables and production cables, can solve problems such as problems of processability
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Embodiment 1
[0250] Invention Embodiment 1 (IE1)
[0251] The volume is 50dm 3 The loop reactor was operated at a temperature of 70 °C and a pressure of 63 bar. Ethylene, 1-butene, propane diluent and hydrogen were added to the reactor so that the feed rate of ethylene was 1.0 kg / h, the feed rate of hydrogen was 5.0 g / h, and the feed rate of 1-butene was 80 g / h, the feed rate of propane was 50 kg / h. In addition, 11 g / h of the solid Ziegler polymerization catalyst component was introduced into the reactor together with the triethylaluminum cocatalyst so that the molar ratio of Al / Ti was about 15. The production rate is 1 kg / h.
[0252] The slurry stream is continuously drawn and directed to a volume of 150dm 3 and a loop reactor operating at a temperature of 85°C and a pressure of 61 bar. Additional ethylene, propane diluent, 1-butene comonomer and hydrogen were further added to the reactor such that the ethylene concentration in the fluid mixture was 4.5 mol%, the hydrogen to ethyle...
Embodiment 2 to 10
[0256] Invention Embodiments 2 to 10 (IE2 to IE10)
[0257] The procedure of Example 1 was followed except that the operating conditions in the loop reactor and the gas phase reactor were modified as shown in Table 1. IE10 was performed without adding carbon black in the extrusion step.
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