Preparation method of heat-resistant polyethylene, heat-resistant polyethylene prepared therefrom, and composition thereof
A technology of heat-resistant polyethylene and its composition, which is applied in the field of heat-resistant polyethylene and its composition, and can solve the problem of narrow molecular weight distribution of polyethylene, unsuitability for industrial applications, poor balance between production cost and high temperature creep resistance of products Performance and other issues
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[0023] As described in the background art section, the existing methods for preparing heat-resistant polyethylene cannot effectively solve the problems of complex preparation process, complicated operation and unsuitable for industrial application. In order to solve the above problems, the present invention provides a method for preparing heat-resistant polyethylene, which includes the following steps: (a) conducting a first polymerization reaction of ethylene, hydrogen and a catalyst in the presence of a first solvent to form a first polymerization reaction. a polymerization solution; (b) adding ethylene, hydrogen, 1-butene and 1-hexene to the first polymerization solution to carry out a second polymerization reaction to form a second polymerization solution; and (c) in the second polymerization solution In the liquid, ethylene, hydrogen, 1-butene and 1-hexene are further added to carry out the third polymerization reaction to obtain this heat-resistant polyethylene, wherein t...
Embodiment 1
[0040] In the presence of n-hexane, a Ziegler-Natta catalyst (made of titanium tetrachloride-triethylaluminum [TiCl 4 -Al(C 2 H 5 ) 3 ] formed catalyst), ethylene and hydrogen were added to the first reactor, the ethylene addition accounted for 60% of the total addition (36t / h), the reactor temperature was 75°C, the reaction pressure was 0.8MPa, the hydrogen ethylene partial pressure The ratio was 4.0 and the reaction time was 2.5h. Subsequently, the slurry was discharged into the second reaction kettle. In the second reaction kettle, the added amount of ethylene accounted for 25% of the total added amount (36t / h). For 0.3, 1-butene and 1-hexene were added in an amount of 5% by weight of ethylene in three reactors, wherein the mass ratio of 1-butene and 1-hexene was 9:1, and the reaction time was 2h. Subsequently, the slurry was discharged into the third reaction kettle. In the third reaction kettle, the added amount of ethylene accounted for 15% of the total added amount ...
Embodiment 2
[0043] In the presence of n-hexane, a Ziegler-Natta catalyst (made of titanium tetrachloride-triethylaluminum [TiCl 4 -Al(C 2 H 5 ) 3 ] formed catalyst), ethylene and hydrogen were added to the first reactor, the ethylene addition accounted for 45% of the total addition (36t / h), the reactor temperature was 80°C, the reaction pressure was 0.9MPa, and the hydrogen ethylene partial pressure The ratio was 3.5, and the reaction time was 2h. Subsequently, the slurry was discharged into the second reaction kettle. In the second reaction kettle, the added amount of ethylene accounted for 30% of the total added amount (36t / h). For 0.4, 1-butene and 1-hexene were added in an amount of 8% by weight of ethylene in three reactors, wherein the mass ratio of 1-butene and 1-hexene was 8:2, and the reaction time was 2.4h. Subsequently, the slurry was discharged into the third reaction kettle. In the third reaction kettle, the added amount of ethylene accounted for 25% of the total added am...
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