Acrylic processing aid and vinyl chloride-based resin composition comprising same
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Example 1
[0087]To an 8 L polymerization reactor equipped with an agitator were added 50 parts by weight of deionized water and 0.1 parts by weight of sodium lauryl sulfate, and the inside of the polymerization reactor was replaced enough with a nitrogen gas, followed by elevating the inner temperature of the polymerization reactor to 75° C. Then, 80 parts by weight of methyl methacrylate and 5 parts by weight of n-butyl acrylate were mixed with 85 parts by weight of deionized water and 0.25 part by weight of sodium lauryl sulfate to obtain a mixture, and then the mixture obtained was added successively in the reactor together with 0.03 part by weight of potassium persulfate for 3 hours. A further reaction was conducted at 75° C., i.e., the inner temperature of the reactor for 0.5 hour to produce a first copolymer latex.
[0088]Next, to the reactor which contains the first copolymer latex, a mixture in which 10 parts by weight of n-butyl acrylate and 5 parts by weight of polyethylene glyc
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Example 2
[0090]Acrylic processing aid powder was obtained by the same method as that of Example 1 except that 12 parts by weight of n-butyl acrylate and 3 parts by weight of polyethylene glycol methacrylate were used in the step of forming an acrylic shell.
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Example 3
[0091]Acrylic processing aid powder was obtained by the same method as that of Example 1 except that 9 parts by weight of n-butyl acrylate and 6 parts by weight of polyethylene glycol methacrylate were used in the step of forming an acrylic shell.
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