Propylene resin composition with melt flowability and impact resistance
A technology of polypropylene resin and composition, which is applied in the field of polypropylene resin molded products, can solve problems such as not satisfying NB characteristics, and achieve excellent melt fluidity and impact resistance
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[0033] In a specific embodiment of the present invention, the ethylene-propylene block copolymer can be prepared by a production method comprising the steps of: a first polymerization step of polymerizing a propylene homopolymer in two or more continuous reactors; and The ethylene-propylene rubber copolymer component is copolymerized by adding ethylene and propylene in the presence of polymerized propylene homopolymer to obtain a second polymerization step of ethylene-propylene block copolymer resin.
[0034] At this time, each polymerization can use methods and reaction conditions known in the technical field of the present invention, such as slurry polymerization method, bulk polymerization method, solution polymerization method, gas phase polymerization method and the like.
[0035] In a specific embodiment of the present invention, each of the above polymerization steps can be carried out in the presence of a Ziegler-Natta catalyst or a metallocene catalyst. In order to maxi...
Embodiment
[0062] Hereinafter, the present invention will be described in more detail through examples and comparative examples. However, the following examples are only for illustrating the present invention, and the scope of the present invention is not limited thereto.
[0063] Preparation of polypropylene resin composition
[0064] In magnesium chloride (MgCl 2 ) Carriers loaded with titanium chloride (TiCl 4 ), and then add dicyclopentyldimethoxysilane as an exogenous electron donor and cocatalyst triethylaluminum for activating the catalyst, thereby obtaining a Ziegler-Natta catalyst.
[0065] The ethylene-propylene block copolymer was polymerized using Mitsui's Hypol process, which can connect 2 slurry reactors and 2 gas phase reactors in series for continuous polymerization. The operating temperature and pressure of the first to third stage reactors are 60 to 80°C and 15 to 40 bar, respectively. The operating temperature and pressure of the fourth stage reactor are 67 to 72 ...
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