Battery diaphragm and preparation method thereof, battery and terminal
A battery diaphragm and diaphragm technology, applied in secondary batteries, battery pack components, circuits, etc., can solve problems such as easy puncture of the diaphragm, out-of-control failure of the battery cell, and poor ductility, so as to reduce the risk of puncture, Improve safety and benefit cost control
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[0065] Such as image 3 As shown, the embodiment of the present application also provides the preparation method of the above-mentioned battery separator, including:
[0066] S101. Mixing polyolefin resin raw materials and a solvent to obtain a mixed solution, where the polyolefin resin raw materials include polyethylene resin raw materials; the degree of crystallinity measured after mixing the polyethylene resin raw materials is <55%;
[0067] S102, extruding the mixed solution, cooling and casting it into a sheet;
[0068] S103, stretching, extracting, and drying the sheet once to form a porous film;
[0069] S104. The porous film is subjected to secondary stretching and heat setting to obtain a polyolefin porous diaphragm substrate; in the process of preparing the polyolefin resin raw material into a polyolefin porous diaphragm substrate, control the polyethylene resin raw material to the finished diaphragm substrate The increase of the crystallinity of the material is le...
Embodiment 1
[0087] 1. Preparation of battery separator
[0088] The resin raw material adopts a single polyethylene resin with a mass average molecular weight Mw of 600,000 and a crystallinity of 54%. The resin and paraffin oil are melted and mixed in a twin-screw extruder at a temperature of 200°C at a mass ratio of 25:75. 0.3% of antioxidant is added, and the homogeneously kneaded melt is extruded and cast through a slit die. The extrusion speed of the die head melt is 5m / min, the cooling speed of the cast sheet is 80°C / min, and the gel sheet is asynchronously (non-synchronously) biaxially stretched once at 116°C, and the stretching ratio in the MD and TD directions Both are 4.5 times, and the stretching speed is 30% / s. The stretched film was then extracted with dichloromethane to remove paraffin oil components. The film after extraction is subjected to secondary stretching at 125° C., and the secondary stretching is only stretched in the TD direction, and the stretching ratio is 1.1 ...
Embodiment 2
[0095] The resin raw material adopts a single polyethylene resin with a mass average molecular weight Mw of 600,000 and a crystallinity of 54%. The resin and paraffin oil are melted and mixed in a twin-screw extruder at a temperature of 200°C at a mass ratio of 25:75. 0.3% of antioxidant is added, and the homogeneously kneaded melt is extruded and cast through a slit die. The extrusion speed of the die head melt is 5.5m / min, the cooling speed of the cast sheet is 80°C / min, and the gel sheet is asynchronously stretched once at 118°C, and the stretching ratios in both MD and TD directions are 4 times, the stretching speed is 33% / s. The stretched film was then extracted with dichloromethane to remove paraffin oil components. The film after extraction is subjected to secondary stretching at 126° C., and the secondary stretching is only stretched in the TD direction, and the stretching ratio is 1.1 times. Finally, it is made into a polyolefin porous diaphragm base material after ...
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