Method for preparing polypropylene with high melt strength
A high melt strength, polypropylene technology, applied in the field of polyolefins, can solve the problems of uneven product thickness, poor transparency, easy cracking, etc., and achieve the effects of increasing molecular weight, economical manufacturing cost, and improving melt strength
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Embodiment 1
[0034] Propylene and α-olefins are used to remove impurities such as sulfur, oxygen, water and carbon monoxide.
[0035] at 23m 3 In the polymerization kettle, put 11.8m 3 Propylene, 0.74m 3 Butene-1, 110g hydrogen, and activator triethylaluminum 2500ml, DDS (diphenyldimethoxysilane) 150ml, high melt strength polypropylene catalyst (1,3 glycol ester electron donor type) Z-N catalyst system) 190g, copolymerization catalyst (diether electron donor type Z-N catalyst system) 40g, the temperature of the kettle is controlled at 68°C, the pressure inside the kettle is maintained at 2.8MPa, and the polymerization time is 3h. The reacted monomer and polypropylene are separated to obtain polypropylene powder without propylene and α-olefin, and then air is introduced to deactivate the polypropylene powder. Flash deactivation, open the lower valve of the flash tank, and pass through the screen with a vacuum After the powder is sucked into the storage tank, it is packaged into the wareh...
Embodiment 2
[0039] Propylene and α-olefins are used to remove impurities such as sulfur, oxygen, water and carbon monoxide.
[0040] at 23m 3 In the polymerization kettle, put 11.7m 3 Propylene, 0.89m 3Butene-1, 360g hydrogen, and accordingly add activator triethylaluminum 2000ml, DDS 150ml, high melt strength polypropylene catalyst (1,3 glycol ester electron donor type Z-N catalyst system) 180g, copolymerization catalyst (two Ether electron donor type Z-N catalyst system) 40g, the temperature of the kettle is controlled at 72°C, the pressure inside the kettle is kept at 3.2MPa, and the polymerization time is 2.5h. After the polymerization reaction is stopped, after the raw materials are recovered, the unreacted monomer and polypropylene are separated The polypropylene powder without propylene is obtained, and then air is introduced to deactivate the polypropylene powder. The flash deactivation is performed, and the lower valve of the flash kettle is opened, and the powder is sucked int...
Embodiment 3
[0044] Propylene and α-olefins are used to remove impurities such as sulfur, oxygen, water and carbon monoxide.
[0045] at 23m 3 In the polymerization kettle, put 11.3m 3 Propylene, 0.94m 3 Butene-1, 300g hydrogen, and accordingly add activator triethylaluminum 2000ml, DDS 180ml, high melt strength polypropylene catalyst (1,3 glycol ester electron donor type Z-N catalyst system) 160g, copolymerization catalyst (two Ether electron donor type Z-N catalyst system) 40g, the temperature of the kettle was controlled at 75°C, the pressure inside the kettle was maintained at 3.2MPa, and the polymerization time was 2.8h, after the polymerization reaction was stopped. After raw material recovery, the unreacted monomer and polypropylene are separated to obtain polypropylene powder without propylene, and then air is introduced to deactivate the polypropylene powder by flash deactivation, the lower valve of the flash tank is opened, and the The net uses vacuum to suck the powder into t...
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