Resin dispersion, coating materials, laminates, and process for production of the same
a technology of resin dispersion and coating material, which is applied in the direction of synthetic resin layered products, inks, tyre parts, etc., can solve the problems of insufficient effect, special apparatus, and difficulty in coating bonding or applying, and achieve excellent dispersibility in water, suppress bleeding out of surfactant, and disperse stably
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example 1
[0376]Into a glass flask equipped with a reflux condenser, a thermometer and a stirrer, 650 g of toluene and 350 g of the propylene / butene copolymer (TAFMER XM7070, manufactured by Mitsui Chemicals, Inc.; Copolymer 1) were put, and the interior was substituted with nitrogen gas, and the temperature was raised to 110° C. After raising the temperature, 35 g of maleic anhydride was added, and 10.7 g of t-butylperoxyisopropyl monocarbonate (Perbutyl I, manufactured by NOF Corporation) was added, whereupon stirring was continued at the same temperature for 10 hours to carry out the reaction. After completion of the reaction, the system was cooled to near room temperature, and acetone was added, whereupon the precipitated polymer was collected by filtration. Further, precipitation with acetone and filtration were repeated, and the finally obtained polymer was washed with acetone. The polymer obtained after the washing was dried under reduced pressure to obtain a white powdery maleic anhyd...
example 2
Melt-Modification Step
[0384]200 kg of a propylene / butene copolymer (TAFMER XM7070, manufactured by Mitsui Chemicals, Inc.: Copolymer 1) and 5 kg of maleic anhydride were dry-blended by a supermixer, followed by kneading by means of a twin screw extruder (TEX54αII, manufactured by The Japan Steel Works, Ltd.) under such conditions that the cylinder temperature at the kneading section was 200° C., the screw rotational speed was 125 rpm and the discharge rate was 80 kg / hr, while feeding Perbutyl I by a liquid-feeding pump so that it would be 1 part by weight per 100 parts by weight of the propylene / butene copolymer, to obtain a pelletized product.
[0385]The content (graft ratio) of maleic anhydride groups in the maleic anhydride-modified propylene / butene copolymer thus obtained was 0.8 wt % (0.08 mmol / g as maleic anhydride groups, and 0.16 mmol / g as carboxylic acid groups). Further, the weight average molecular weight was 156,000, and the number average molecular weight was 84,000 (both...
example 3
[0391]A hazy slightly yellow aqueous dispersion was obtained in the same manner as in Example 2 except that the amount of JEFFAMINE M-1000 used, was changed from 15 g to 22.5 g (22.5 mmol).
[0392]The evaluation results of the obtained aqueous resin dispersion are shown in Table 3.
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