Porous polypropylene resin film, separator for use in a battery, and battery
A polypropylene-based, porous membrane technology, applied in the field of porous membranes, can solve the problem of not being able to be used as an electrolyte, and achieve the effect of preventing the deterioration of battery characteristics
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Embodiment 1
[0258] With respect to 100 parts by mass of polypropylene resin (manufactured by Prime Polymer, Prime Polypro F300SV, MFR: 3g / 10 min), 0.2 parts by weight of antioxidant (manufactured by Ciba Specialty Chemicals, IRGANOX B225) is added and used as β crystal nucleation 3,9-bis[4-(N-cyclohexylcarbamoyl)phenyl]-2,4,8,10-tetraoxospiro[5.5]undecane 0.2 parts by mass of the agent, using Toshiba Machine Co., Ltd. The manufactured co-rotating twin-screw extruder (diameter φ40mm, L / D=32) was melted and kneaded at 270°C and extruded from a drawing die. The extruded tow was cooled in water at 30°C and used The cutter was pelletized to obtain resin composition A1.
[0259] The resin composition A1 was extruded at 200°C and cooled and solidified by a casting roll at 126°C to produce a non-porous film.
[0260] The non-porous membrane was stretched in the longitudinal direction at 110°C by 4 times, and then stretched in the transverse direction at 145°C by 2.0 times in sequential biaxial stretc...
Embodiment 2
[0263] Different from the above resin composition A1, high density polyethylene (manufactured by PrimePolymer, Hi-ZEX3300F, density: 0.950g / cm 3 , MFR: 1.1g / 10 min) 80 parts by mass of microcrystalline wax (manufactured by Nippon Seiki Co., Ltd., Hi-Mic1090) 20 parts by mass and dibenzylidene sorbitol as a nucleating agent (New Japan Physicochemical Co., Ltd. Made by the company, Gelol D) 0.2 parts by weight, using the same type of co-rotating twin-screw extruder at 230°C for melt-kneading and extruding from a drawing die, the extruded tow is placed in 30°C water It was cooled, and pelletized with a cutter to obtain a resin composition B1.
[0264] Use different extruders to extrude the resin compositions A1 and B1 at 200°C, pass them through two three-layer feed blocks, and co-extrude them with a T-die for multi-layer molding. After stretching, the film thickness ratio reached A1 / B1 / A1=3.5 / 1 / 3.5 to laminate, and then use a 127°C casting roll to cool and solidify, thereby fabrica...
Embodiment 3
[0268] Use different extruders to extrude the resin compositions A1 and B1 at 200°C, pass them through two three-layer feed blocks, and co-extrude them with a T-die for multi-layer molding. After stretching, the film thickness ratio reached A1 / B1 / A1=3.5 / 1 / 3.5 to laminate, and then use a casting roll at 125°C to cool and solidify to produce a laminated non-porous film.
[0269] The laminated non-porous film was stretched in the longitudinal direction at 120°C by 4.0 times, and then stretched at 98°C in the transverse direction by 2.0 times in sequential two-way stretching, and then relaxed by 6% in the transverse direction at 115°C to obtain Laminated porous membrane (sample).
[0270] Various characteristics of the obtained laminated porous film (sample) were measured and evaluated, and the results are summarized in Table 1.
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