Polypropylene compositions
A polypropylene composition and propylene polymer technology, applied in the field of thermoforming products, can solve the problem that the overall balance of properties cannot be completely satisfied.
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Embodiment 1-7 and Embodiment 10C-12
[0098] Embodiment 1-7 and embodiment 10C-12C (comparative example)
[0099] Catalyst preparation and prepolymerization
[0100] The Ziegler-Natta catalyst component was prepared according to Example 5 of European Patent EP728769, lines 48-55. The catalyst components thus prepared were contacted with triethylaluminum (TEAL) and dicyclopentyldimethoxysilane (DCPMS) as external electron donor components at 12° C. for 24 minutes. The weight ratio between TEAL and solid catalyst component was 11, and the weight ratio between TEAL and DCPMS was 10. The catalyst system thus obtained was prepolymerized by keeping it suspended in liquid propylene at 20° C. for about 5 minutes before introducing it into the first polymerization reactor.
[0101] polymerization
[0102] A propylene homopolymer as component (a) is produced in the first reactor and an ethylene-propylene copolymer as component (b) is produced in the second reactor. Throughout the reaction, constant temperature and p...
Embodiment 8-9 and Embodiment 13C-17
[0105] Embodiment 8-9 and embodiment 13C-17C (comparative example)
Embodiment 1
[0106] The procedures described in Examples 1-7 and Examples 10C-12C are repeated, and the difference is that the Ziegler-Natta catalyst is prepared according to Example 1 of the international application WO2009 / 050045, only for the first temperature rise For example, the temperature is raised to 110°C instead of 100°C. Data on the characterization of the polymers obtained are shown in Table 1. Data on the physical-mechanical properties of the final polymer composition are shown in Table 2, obtained from measurements carried out on the polymer as extruded.
[0107] Table 1
[0108] Example
1
2
3
4
5
6
7
8
9
10C
11C
12C
13C
14C
15C
16C
17C
(a) C2 [wt%]
0
1.0
1.9
0
1.0
1.0
1.0
1.9
1.9
1.9
1.9
1.9
1.5
3.0
0
1.0
1.9
(b) C2 [wt%]
80
80
80
78
78
85
80
79
79
73
72
75
73
79
79
79
79
XSIV[dl / g]
1.0
...
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