Process for producing rubbery polymer particle and process for producing resin composition containing the same
A resin composition and polymer technology are applied in the field of the preparation method of rubber-like polymer particles and the preparation method of the resin composition containing the particles, which can solve the problems of difficult separation, adverse effects on quality, unsatisfactory industry and the like, and achieve The effect of reducing equipment cost and efficient manufacturing
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manufacture example 1
[0109] (Production example 1) Production of rubbery polymer particle (A) latex
[0110] Add 200 parts by weight of water, 0.03 parts by weight of tripotassium phosphate, 0.25 parts by weight of potassium dihydrogen phosphate, 0.002 parts by weight of ethylenediaminetetraacetic acid, 0.001 parts by weight of ferrous sulfate and dodecylbenzenesulfonate into a 100L pressure-resistant polymerization kettle. 1.5 parts by weight of sodium bicarbonate, sufficient nitrogen replacement was carried out while stirring, and after deoxygenation, 75 parts by weight of butadiene and 25 parts by weight of styrene were added to the system, and the temperature was raised to 45°C. add to 0.015 parts by weight of an alkyl hydroperoxide, and then 0.04 parts by weight of sodium formaldehyde sulfite were added to start polymerization. From the beginning of polymerization to the 4th hour, add the pair 0.01 part by weight of alkyl hydroperoxide, 0.0015 part by weight of ethylenediaminetetraacetic ...
Embodiment 1
[0113] Add 126 g of methyl ethyl ketone (solubility in water at 20°C: 10% by weight) to a 1 L tank with a stirrer (a stirrer with 4 flat scraper blades with an inner diameter of 100 mm and a stirring blade diameter of 75 mm arranged in three stages in the axial direction), and stir at 500 rpm , 126 g of the aqueous latex of the rubber-like polymer particles (A) obtained in Production Example 1 was added. After uniform mixing, 200 g of water was added at a supply rate of 80 g / min while stirring at 500 rpm. After the supply is terminated, the stirring is promptly stopped, and as a result, a slurry liquid composed of a floating aggregate (F) and an aqueous phase containing a part of the organic solvent is obtained.
[0114] Next, the aggregate (F) containing a part of the water phase remained, and 348 g of the water phase was discharged from the outlet in the lower part of the tank. The aggregate (F) containing a part of the water phase was 104 g, and the proportion of the organ...
Embodiment 2
[0117] 136 g of methyl ethyl ketone was added to 94 g of the aggregate (F) obtained in Example 1, and mixed for 30 minutes under a stirring condition of 500 rpm to obtain a dispersion (G) in which rubbery polymer particles (A) were uniformly dispersed. The dispersion (G) was transferred to a 1L tank with a jacket and a stirrer (a stirrer with an inner diameter of 100 mm and a blade-type 90 mm anchor blade), and an epoxy resin (manufactured by Japan Epoch Resin Co., Ltd., Epico-to 828) was added. 92g, mixed evenly. Then, set the jacket temperature (hot water) at 60° C., and use a vacuum pump (oil rotary vacuum pump, manufactured by Sato Vacuum Co., Ltd., TSW-150) to continuously distill volatile components under reduced pressure until reaching a specified concentration ( 5000ppm), to obtain a transparent epoxy resin composition containing rubbery polymer particles (A). The time for volatilization was 5 hours and 20 minutes. As a result of observing the dispersion state of the...
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