Polyalkylene microporous diaphragm for lithiam ion battery and manufacturing method thereof
A lithium-ion battery, microporous technology, applied in battery pack parts, chemical instruments and methods, circuits, etc., can solve the problem of poor elastic recovery of single-layer microporous polyethylene film, low production performance and use performance, and easy generation of batteries. Stretching and other problems, to achieve the effect of improving heat resistance, simple manufacturing process, and not easy to curl
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Embodiment 1
[0055] In polypropylene (M w =4.8×10 5 , The melt index is 2.1, the melting point is 170°C), 30% of the ethylene-propylene copolymer is added for blending and granulation, and then 25% of the weight unit ratio of this blend is added to one of the twin-screw extruders (Φ58mm, L / D=48, high-shear form), and 75% of the weight unit ratio of liquid paraffin is added to the twin-screw extruder through lateral feeding, and the polypropylene blend is made at 250 in the twin-screw extruder. The liquid paraffin was melted and mixed under the conditions of ℃ and 200 rpm to form a polypropylene blend solution. 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.
[0056] At the same time, 25% weight unit proportion of high-density polyethylene (ρ = 0.968g / cm 3 , M w =3.5×10 5 ) Add another twin-screw extruder (Φ58mm, L / D=48, high-shear form), and 75% of the weight unit ratio of liquid pa...
Embodiment 2
[0059] The polypropylene (M w =4.8×10 5, Melt index 2.1, melting point 170℃) was added to one of the twin-screw extruders (Φ58mm, L / D=48, high-shear mode), and 75% of the weight unit ratio of liquid paraffin was added through lateral feeding Twin-screw extruder, by melting polypropylene at 250℃ and 200rpm and mixing liquid paraffin in the twin-screw extruder to form a polypropylene solution. The obtained solution is passed from the two surface layers of the three-layer die through a metering pump Extrusion, the thickness of each layer is 170μm.
[0060] At the same time in the high-density polyethylene (ρ = 0.958g / cm 3 , M w =6.8×10 5 ) Was added 35% of ethylene-propylene copolymer for blending and granulation, and then 25% of the weight unit ratio of this mixture was added to a twin-screw extruder (Φ58mm, L / D=48, high shear mode), and 75 The liquid paraffin of the percentage by weight is added to the twin-screw extruder through lateral feeding, and the polyethylene is melted and ...
Embodiment 3
[0063] The polypropylene (M w =4.8×10 5 , Melt index 2.1, melting point 170℃) was added to one of the twin-screw extruders (Φ58mm, L / D=48, high-shear mode), and 75% of the weight unit ratio of liquid paraffin was added through lateral feeding Twin-screw extruder, by melting polypropylene at 250℃ and 200rpm and mixing liquid paraffin in the twin-screw extruder to form a polypropylene solution. The obtained solution is passed from the two surface layers of the three-layer die through a metering pump Extrusion, the thickness of each layer is 170μm.
[0064] At the same time in the high-density polyethylene (ρ = 0.958g / cm 3 , M w =6.8×10 5 ) Was added 30% of ethylene-propylene copolymer for blending and granulation, and then 25% of the weight unit ratio of this mixture was added to a twin-screw extruder (Φ58mm, L / D=48, high shear mode), and 75 The liquid paraffin of the percentage by weight is added to the twin-screw extruder through lateral feeding, and the polyethylene is melted and...
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