Dispersion stabilizer for suspension polymerization and method for producing vinyl resin
a technology of suspension polymerization and stabilizer, which is applied in the direction of transportation and packaging, mixing, chemistry apparatus and processes, etc., can solve the problems of not fully satisfying the above required performance, and achieve the effects of improving bulk density, excellent polymerization stability, and small particle siz
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example 1
[0051]In a 5 liter autoclave, 100 parts of a deionized aqueous solution in which PVA (A1) was dissolved in an amount of 880 ppm relative to vinyl chloride were charged, and deionized water was additionally charged to have 1200 parts of deionized water in total. Then, 0.65 parts of a 70% solution of cumyl peroxyneodecanoate in toluene and 1.05 parts of a 70% solution of t-butyl peroxyneododecanoate in toluene were charged in the autoclave. An operation in which nitrogen was introduced into the autoclave to produce a pressure of 0.2 MPa and then the nitrogen was purged was repeated 5 times in total. Inside the autoclave was thus sufficiently purged with nitrogen to remove oxygen, followed by charging of 940 parts of vinyl chloride. The contents in the autoclave were raised in temperature to 57° C. to initiate polymerization of the vinyl chloride monomer with stirring. The pressure in the autoclave was 0.80 MPa at the beginning of the polymerization. Approximately 3.5 hours after the i...
example 2
[0064]Suspension polymerization of vinyl chloride was carried out in the same manner as that in Example 1 other than using a deionized aqueous solution in which PVA (A1) (240 ppm based on vinyl chloride) and PVA (B1) (640 ppm based on vinyl chloride) were dissolved, instead of the deionized aqueous solution of PVA (A1), to produce vinyl chloride resin particles. Evaluation results of the vinyl chloride resin particles are shown in Table 2.
examples 3-14
[0065]Suspension polymerization of vinyl chloride was carried out in the same manner as that in Example 2 other than changing the type and amount of the PVA (A) and the PVA (B) to be used as shown in Table 1 to produce vinyl chloride resin particles. Evaluation results of the vinyl chloride resin particles are shown in Table 2.
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