Preparation method of polypropylene with high melt strength
A high melt strength, polypropylene technology, applied in the field of polypropylene preparation, can solve problems such as strong complexing ability, and achieve the effects of easy operation, broad application prospects, and high melt strength
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[0043] Example 1:
[0044] The polymerization reaction was carried out on a set of 25Kg / hr polypropylene pilot plant. Its main equipment includes a prepolymerization reactor, a first loop reactor and a second loop reactor. The polymerization method and steps are as follows:
[0045] Step ⅰ
[0046] Pre-polymerization reaction:
[0047] Main catalyst (DQ-III catalyst, provided by Sinopec Catalyst Company Beijing Aoda Branch), co-catalyst (triethylaluminum), first external electron donor (dicyclopentyldimethoxysilane) at 6℃, 20min After the pre-contact, the continuous stirred tank pre-polymerization reactor is continuously added to the pre-polymerization reactor. The flow of triethyl aluminum (TEA) entering the pre-polymerization reactor is 6.33 g / hr, dicyclopentyl dimethoxy silane The (DCPMS) flow rate is 0.63 g / hr, the main catalyst flow rate is 0.01 g / hr, and the TEA / DCPMS ratio is 20 (molar ratio), where DCPMS is the first external electron donor. The prepolymerization is carrie...
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[0055] Example 2:
[0056] The steps are the same as in Example 1, except that a small amount of hydrogen is added to the first loop reactor in step i, the hydrogen concentration detected by online chromatography is 300 ppmV, and the hydrogen concentration in the second loop reactor in step iii is changed It is 1000ppmV. The polymerization process conditions, the analysis results of the obtained polymer and the physical properties of the polymer are listed in Tables 1 to 3.
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[0057] Example 3:
[0058] The steps are the same as in Example 2, except that the ratio of aluminum alkyl to external electron donor in the two steps is adjusted, and the TEA / DCPMS in the first reactor of step i is adjusted to 60 (molar ratio ), the TEA / DIBMP in the second reactor is adjusted to 10 (molar ratio), and the hydrogen concentration in the second loop reactor in step iii is changed to 5000 ppmV. The polymerization process conditions, the analysis results of the obtained polymer and the physical properties of the polymer are listed in Tables 1 to 3.
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