Film, inner liner for tire, and tire using the inner liner
An auxiliary layer and resin composition technology, applied in the direction of pneumatic tires, special tires, tire parts, etc., can solve the problems of insufficient bending resistance and softness, easy fracture of the inner liner, and inability to display gas barrier properties, etc., to achieve Effect of good gas barrier property, excellent gas barrier property and bending resistance, internal pressure retention improvement
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[0094] The present invention will be described in further detail by the following examples. The present invention is not limited by these examples, and can be appropriately changed within the scope not departing from the spirit of the present invention.
Synthetic example 1
[0096] 2 parts by mass of an ethylene-vinyl alcohol copolymer having an ethylene content: 44 mol% and a degree of saponification: 99.9% (MFR at 190° C. under a load of 2160 g: 5.5 g / 10 minutes) was charged into a pressurized reaction tank and 8 parts by mass of N-methyl-2-pyrrolidone, and the mixture was heated and stirred at 120° C. for 2 hours to completely dissolve the ethylene-vinyl alcohol copolymer. Next, 0.4 parts by mass of propylene oxide was added to the mixture as the epoxy compound (E), and the resulting reaction mixture was heated at 160° C. for 4 hours. After the heating was completed, the mixture was poured into 100 parts by mass of distilled water to settle. The resulting precipitate was sufficiently washed with a large amount of distilled water to wash off N-methyl-2-pyrrolidone and unreacted propylene oxide, whereby a modified ethylene-vinyl alcohol copolymer was obtained. The modified ethylene-vinyl alcohol copolymer thus obtained is pulverized by a pulveri...
Synthetic example 2
[0098] By using the "TEM-35BS" extruder (37mmΦ, L / D=52.5, manufactured by Toshiba Machine Co., Ltd.), the screw structure, vent hole, and pressure (dydroforming) inlet are as follows Figure 5settings shown in . The extruder was operated at a screw rotation number of 400 rpm with barrel C1 water cooled and barrels C2-C3 and barrels C4-C15 heated at 200°C and 240°C, respectively. Resin was supplied at a rate of 15 kg / hour from the resin base port of C1. After the supplied EVOH was melted, water and oxygen were removed from the vent hole 1, and glycidol was supplied from the hydroreforming inlet of C9 at a rate of 2.5 kg / hour (supply pressure: 6 MPa), thereby obtaining glycidol-modified EVOH .
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