Chlorinated propylene random copolymer and compositions containing the same
一种无规共聚物、氯化丙烯的技术,应用在接枝聚合物粘合剂、粘合剂类型、应用等方向,能够解决低烤漆温度等问题,达到耐水性优异、液体状态良好、耐汽醇性优异的效果
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Embodiment 1-1~1-3
[0124] [Examples 1-1 to 1-3] (solvent system)
[0125] 500 g of a propylene-based random copolymer (Tm = 80° C., melt viscosity at 170° C.: about 3000 mPa·s) prepared using a metallocene catalyst as a polymerization catalyst was charged into a reaction kettle with an enamel lining. Add 5L chloroform, at 2kg / cm 2 Chlorination is carried out by feeding gaseous chlorine from the bottom of the reactor while irradiating ultraviolet rays under high pressure. In order to adjust the chlorine content, samples were taken on the way, and the solvent chloroform was distilled off with an evaporator. Then replace it with toluene / cyclohexane=70 / 30 (weight ratio), and add 2.0% by weight of epoxy resin (Epikote) 828 (manufactured by Yuhua Shieluepokishi Co., Ltd.) with respect to the resin as a stabilizer, so that the resin concentration is 20% by weight to obtain the chlorinated propylene-based random copolymer resin solutions of Examples 1-1 to 1-3 in which the chlorine content was changed...
Embodiment 2-1-2-3
[0126] [Example 2-1-2-3] (solvent system)
[0127] 700 g of a propylene-based random copolymer prepared using a metallocene catalyst as a polymerization catalyst (melt viscosity at Tm = 80° C., 170° C. is about 3000 mPa·s), 20 g of maleic anhydride, and 15 g of dicumyl peroxide were thoroughly mixed in advance. , feed the twin-screw extruder of L / D=34, φ=40mm, and the residence time is 10 minutes. The barrel temperature is set at 180°C (the first barrel - the seventh barrel) for reaction, and the exhaust is carried out in the seventh barrel to remove unreacted maleic anhydride to obtain maleic anhydride modified propylene random copolymerization things. 500 g of this resin was charged into a reaction vessel with an enamel lining, and chlorination was carried out in the same manner as in Example 1 to prepare a resin composition to obtain chlorine in Examples 2-1 to 2-3 whose chlorine content was changed as shown in Table 1. Propylene-based random copolymer resin solution.
Embodiment 3
[0129] 700g of propylene-based random copolymer (melt viscosity at Tm=92°C, 170°C is about 4100mPa·s) prepared with metallocene catalyst as polymerization catalyst and 15g of dicumyl peroxide were fully mixed in advance, and supplied to L / D =34, φ=40mm twin-screw extruder, the residence time is 15 minutes. The barrel temperature was set at 180° C. (the first barrel to the seventh barrel), and the molecular weight and molecular weight distribution were adjusted through thermal degradation to obtain a propylene-based random copolymer. 500 g of this resin was placed in an enamel-lined reactor, and chlorination was carried out in the same manner as in Example 1. After chlorination, a resin composition was prepared using ethyl acetate as a solvent instead of toluene, and the chlorinated propylene-based random copolymer resin solutions of Examples 3-1 to 3-3 whose chlorine content varied as shown in Table 1 were obtained.
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