Polyalkylene microporous diaphragm for lithium ion battery and manufacturing method thereof
A lithium-ion battery, microporous technology, applied in battery pack components, chemical instruments and methods, circuits, etc., can solve the problems of easy stretching of batteries, low production performance and use performance, and unsafety, so as to prevent fire and explosion accidents, improved mechanical properties, and simple manufacturing process
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Embodiment 1
[0054] In polypropylene (M w =4.8×10 5 , melt index is 2.1, melting point 170 ℃), add 30% ethylene-propylene copolymer for blending and granulation, and then add 25% weight unit ratio of this blend into one of the twin-screw extruders (Φ58mm, L / D=48, high shear form), and the liquid paraffin of 75% weight unit ratio is added to twin-screw extruder by side feeding, by making polypropylene blend in twin-screw extruder at 250 The liquid paraffin was melted and mixed under the conditions of ℃ and 200rpm to form a polypropylene blend solution, and the obtained solution was extruded from the two surface layers of the three-layer die through a metering pump, and the thickness of each layer was about 170 μm.
[0055] Simultaneously the high-density polyethylene (ρ=0.968g / cm 3 ,M w =3.5×10 5 ) into another twin-screw extruder (Φ58mm, L / D=48, high-shear form), and 75% liquid paraffin in the weight unit ratio is added to the twin-screw extruder by side feeding. In a screw extruder, ...
Embodiment 2
[0058] 25% by weight of polypropylene (M w =4.8×10 5, melt index is 2.1, fusing point 170 ℃) adds wherein a twin-screw extruder (Φ58mm, L / D=48, high-shear form), and the liquid paraffin of 75% weight unit ratio is added into by side feeding Twin-screw extruder, by melting polypropylene at 250°C and 200rpm in the twin-screw extruder and mixing liquid paraffin to form a polypropylene solution, the obtained solution is pumped from the two surface layers of the three-layer die through a metering pump Extrusion, the thickness of each layer is 170 μm.
[0059] At the same time in high-density polyethylene (ρ = 0.958g / cm 3 ,M w =6.8×10 5 ) into 35% ethylene-propylene copolymer for blending and granulation, and then 25% of this mixture by weight unit ratio is added into a twin-screw extruder (Φ58mm, L / D=48, high shear form), and 75 The liquid paraffin of % weight unit ratio is joined into twin-screw extruder by side feeding, by making polyethylene melt and mix liquid paraffin und...
Embodiment 3
[0062] 25% by weight of polypropylene (M w =4.8×10 5 , melt index is 2.1, fusing point 170 ℃) adds wherein a twin-screw extruder (Φ58mm, L / D=48, high-shear form), and the liquid paraffin of 75% weight unit ratio is added into by side feeding Twin-screw extruder, by melting polypropylene at 250°C and 200rpm in the twin-screw extruder and mixing liquid paraffin to form a polypropylene solution, the obtained solution is pumped from the two surface layers of the three-layer die through a metering pump Extrusion, the thickness of each layer is 170 μm.
[0063] At the same time in high-density polyethylene (ρ = 0.958g / cm 3 ,M w =6.8×10 5 ) into 30% ethylene-propylene copolymer for blending and granulation, and then 25% of this mixture by weight unit ratio is added to a twin-screw extruder (Φ58mm, L / D=48, high shear form), and 75 The liquid paraffin of % weight unit ratio is joined into twin-screw extruder by side feeding, by making polyethylene melt and mix liquid paraffin unde...
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