Polyethylene microporous membrane, preparation method and lithium ion battery
A technology of polyethylene microporous membrane and lithium-ion battery, which is applied to battery components, circuits, electrical components, etc., can solve problems such as poor air permeability and cycle performance, accelerated self-discharge speed, and slow self-discharge speed, and achieves Enhanced puncture resistance, good self-discharge performance, and the effect of preventing short circuits
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[0041] 2. Preparation method of polyethylene microporous membrane
[0042] Description of raw materials and process parameters
[0043] The present invention has no special limitation on the polyethylene resin used, generally a single resin can be used, or two or more resins can be used in combination.
[0044] In the present invention, the weight-average molecular weight of the polyethylene resin used is not particularly limited, generally speaking, it is 10,000-5 million, preferably 100,000-3 million, and more preferably 300,000-2 million.
[0045] The present invention has no special limitation on the pore-forming agent used, usually liquid paraffin, solid paraffin, dioctyl phthalate, dibutyl phthalate and other solvents that have a pore-forming effect on polyolefin resins. The pore forming agent may be used alone or in combination of two or more. Liquid paraffin and dioctyl phthalate are preferred.
[0046] The present invention is not particularly limited to the ...
Embodiment 1
[0062] (1) Extrusion casting: inject polyethylene resin and liquid paraffin into a twin-screw extruder, and melt and knead them into a uniform melt in the twin-screw. Then the melt is continuously extruded from the die, and rapidly cooled and shaped by cooling rollers to obtain thick sheets. Wherein, the weight average molecular weight of the polyethylene resin is 500,000, and the viscosity grade of the liquid paraffin is 40. The mass ratio of polyolefin resin to liquid paraffin is 1:3, the melting temperature is 200°C, and the temperature of the cooling roll is 30°C.
[0063] (2) Biaxial stretching: stretch the thick sheet in a stretching machine after preheating. Among them, the stretching temperature of the upper chamber is 120°C, the stretching temperature of the lower chamber is 115°C, and the temperature difference between the upper and lower chambers is 5°C to obtain an oily film;
[0064] (3) Extraction: Extract the liquid paraffin in the oily film with dichlorometha...
Embodiment 2
[0069] (1) Extrusion casting: inject polyethylene resin and liquid paraffin into a twin-screw extruder, and melt and knead them into a uniform melt in the twin-screw. Then the melt is continuously extruded from the die, and rapidly cooled and shaped by cooling rollers to obtain thick sheets. Wherein, the weight average molecular weight of the polyethylene resin is 1 million, and the viscosity grade of the liquid paraffin is 40. The mass ratio of polyolefin resin to liquid paraffin is 1:4, the melting temperature is 200°C, and the temperature of the cooling roll is 30°C.
[0070] (2) Biaxial stretching: stretch the thick sheet in a stretching machine after preheating. Among them, the stretching temperature of the upper chamber is 125°C, the stretching temperature of the lower chamber is 115°C, and the temperature difference between the upper and lower chambers is 10°C to obtain an oily film;
[0071] (3) Extraction: Extract the liquid paraffin in the oily film with dichlorome...
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