Optical film and information technology apparatus comprising the same
a technology of information technology and optical film, applied in the field of optical film, can solve problems such as light leakage, and achieve the effects of excellent optical property and optical transparency, low haze, and not easily broken
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example 1
[0083]The resin composition in which poly(N-cyclohexylmaleimide-co-methylmethacrylate), the styrene-maleic anhydride resin and the phenoxy-based resin were uniformly mixed with each other at a weight ratio of 100:2.5:5 was provided to a 24φ extruder in which nitrogen was substituted from the raw material hopper to the extruder, and melted at 250° C. to manufacture the raw material pellet.
[0084]As the phenoxy-based resin, PKFE (Mw=60,000, Mn=16,000, and Tg=95° C.) manufactured by InChemRez®, Co., Ltd. was used, and Dylarck 332 that included 85 wt % of styrene and 15 wt % of maleic anhydride was used as the styrene-maleic anhydride copolymer resin. In the poly(N-cyclohexylmaleimide-co-methylmethacrylate) resin, the content of N-cyclohexylmaleimide was 6.5 wt % which was analyzed by using the NMR.
[0085]The obtained raw material pellets were dried in the vacuum, melted at 260° C. by using the extruder, and passed through the coat hanger type of T-die, the chrome-coated casting roll and ...
example 2
[0086]The resin composition in which poly(N-cyclohexylmaleimide-co-methylmethacrylate), the styrene-maleic anhydride resin and the phenoxy-based resin were uniformly mixed with each other at a weight ratio of 100:2.5:5 was provided to a 24φ extruder in which nitrogen was substituted from the raw material hopper to the extruder, and melted at 250° C. to manufacture the raw material pellet.
[0087]The obtained raw material pellets were dried in the vacuum, melted at 260° C. by using the extruder, and passed through the coat hanger type of T-die, the chrome-coated casting roll and the dry roll to manufacture the film that had the thickness of 150 μm. This film was stretched by using the pilot stretching device at 125 to 140° C. in the MD direction using a difference between speeds of rolls at the ratio of 170% described in the following Table 2, and stretched in the TD direction at 125 to 140° C. by using the tenter at the ratio of 250% described in the following Table 2 to manufacture t...
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