Process for the preparation of a catalyst component and components therefrom obtained
A catalyst and solid catalyst technology, applied in the field of catalyst components, can solve the problems of not being able to function as a solvent, changing the performance of catalyst components, and not being able to prepare them.
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Embodiment 1-12
[0080] A series of catalyst components were formulated using different electron donating compounds (ED). Using spherical MgCl containing 25 wt% EtOH prepared as described above 2 (EtOH) adduct to prepare the catalyst, first follow the above steps with TiCl 4 Treatment to produce an intermediate which is then contacted with the specific ED compound employed in the feed ratios shown in Table 1 following the general procedure.
[0081]The catalysts thus prepared were then used in the copolymerization of ethylene carried out following the general procedure described above under the specific conditions shown in Table 2, which also contains data on the characteristics of the polymers.
Embodiment 13-14
[0083] The catalyst was prepared according to the same procedure as described in Examples 1-12 using AcOEt as the electron donor, except that the molar feed ratio ED / Ti was 8, 4 and 1, respectively. The catalysts thus prepared were then used in the copolymerization of ethylene carried out following the general procedure described above under the specific conditions shown in Table 4, which also contains data on the characteristics of the polymers.
Embodiment 15
[0085] The prepared solid intermediate was injected into an autoclave according to the general procedure and kept stirring in anhydrous hexane (solid concentration 40 g / L) at 30° C. under nitrogen atmosphere. The suspension was treated with an amount of a 10 wt% solution of triethylaluminum (TEA) in hexane such that the ratio TEA / solid = 0.5 wt / wt. Propylene was then slowly added in an amount equal to 0.7 times the initial amount of solids at a rate suitable to keep the temperature constant at 30°C. Polymerization was stopped after 30 minutes. The solid was washed 3 times with anhydrous hexane at 25°C, resuspended in hexane and treated with AcOEt as the ED compound following the general procedure except that the molar AcOEt / Ti feed ratio was 8. The characteristics of the catalyst components are reported in Table 3 and the results of the copolymerization in Table 4.
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