Process for producing alpha-olefin polymerization catalyst
An olefin polymerization and catalyst technology, applied in the field of preparing α-olefin polymerization catalyst, can solve the problems of high rigidity, poor responsiveness, low molecular weight, etc.
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[0157] Examples of the α-olefin polymer produced by the production method of the present invention are propylene homopolymer, 1-butene homopolymer, propylene-ethylene copolymer, propylene-1-butene copolymer, propylene-1-hexene Copolymer, and propylene-1-octene copolymer.
[0158] The process for preparing the α-olefin polymers of the present invention is preferably used for the preparation of isotactic stereoregular α-olefin polymers, and particularly preferably for the preparation of isotactic stereoregular propylene polymer.
[0159] Examples of isotactic propylene polymers are propylene homopolymers; copolymers of propylene with ethylene and / or comonomers such as alpha-olefins having 4 to 12 carbon atoms, wherein ethylene and / or comonomers The amount of monomer used is such that the obtained copolymer has crystallization properties; and the block copolymer obtained according to the preparation method comprising the following steps: (i) homopolymerizing propylene, or combin...
Embodiment 1
[0170]A 300 liter stainless steel reaction vessel equipped with a stirrer was dried under reduced pressure and then purged with argon. Cool the autoclave, then evacuate. To a glass charger containing heptane, add 2.6 mmol of triethylaluminum (organoaluminum compound), 0.52 mmol of cyclohexyltriethoxysilane (external electron donor), and 6.39 mg of 182981A, the solid catalyst components prepared in Example 1(2), in this order, thereby bringing them into contact with each other in a glass filler to form a polymerization catalyst-containing mixture.
[0171] The mixture was added to the autoclave all at once. Then, 780 g of liquefied propylene (α-olefin) and 5.1 NL of hydrogen were charged into the reactor in this order. The autoclave was heated to 70°C, whereby polymerization was initiated.
[0172] After 1 hour of polymerization, unreacted propylene remaining in the reactor was purged to obtain a polymer. The polymer was dried at 60° C. for 1 hour under reduced pressure, th...
Embodiment 2
[0196] Example 1 was repeated except that (1) the amount of the solid catalyst component was changed to 5.44 mg, and (2) the amount of added hydrogen was changed to 15.4 NL, whereby a propylene homopolymer powder was obtained. The yield of propylene homopolymer per 1 g of solid catalyst component was 25,500 g-polymer / g-solid catalyst component (polymerization activity).
[0197] The propylene homopolymer was found to have a soluble fraction (CXS) in xylene at 20° C. of 0.90 wt %; an intrinsic viscosity ([η]) of 0.75 dl / g; and an isotactic pentad fraction of 0.9829 [ mmmm], the total amount of homopolymer is 100 wt%. The results are summarized in Table 1.
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