Manufacturing method of resin
A manufacturing method and resin technology, applied in the field of resin manufacturing, can solve problems such as large amount of residual monomers and insufficient batch productivity, and achieve the effect of suppressing pollution of manufacturing equipment and less volatilization
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[0081] Hereinafter, an Example and a comparative example are shown, and this invention is demonstrated concretely.
[0082] The measurement of the amount of residual monomers in the following examples and comparative examples was performed under the above-mentioned conditions by GPC in the same manner as the measurement of the weight average molecular weight.
[0083] In addition, the reproducibility of a weight average molecular weight was judged by the following criteria.
[0084] Reproducibility criteria
[0085] ○: The same polymerization reaction is repeated twice, and the rate of change of the weight average molecular weight of the second time ((weight average molecular weight of the second time - weight average molecular weight of the first time) / weight average molecular weight of the first time × 100) is in Within ±10%
[0086] ×: The same polymerization reaction is repeated twice, and the change rate of the weight average molecular weight of the second time deviat...
Embodiment 2
[0092] The thermal radical polymerization initiator was changed to 1,1,3,3-tetramethylbutyl peroxy-2-ethylhexanoate (manufactured by NOF Corporation, PEROCTA (registered trademark) O: 10 hours half-life temperature 65°C ), except that the reaction temperature was set at 109° C., the reaction was carried out in the same manner, and a carboxyl group-containing resin solution with a weight average molecular weight of 18,500 and a solid content acid value of 180 KOHmg / g was obtained. As a result of measuring the total amount of residual monomers, it was 0.7% by mass. Moreover, the same reaction was performed again, and as a result, the weight average molecular weight was 19300 and the reproducibility of molecular weight was favorable.
Embodiment 3
[0094] The thermal radical polymerization initiator was changed to tert-butyl peroxybenzoate (manufactured by Nippon Kayaku Co., Ltd., KAYABUTYL B (registered trademark): 10-hour half-life temperature 105°C), and the reaction temperature was set to 127°C. The reaction was carried out to obtain a carboxyl group-containing resin solution with a weight average molecular weight of 14800 and a solid content acid value of 180KOHmg / g. As a result of measuring the total amount of residual monomers, it was 0.6% by mass. Moreover, the same reaction was performed again, and as a result, the weight average molecular weight was 15100 and the reproducibility of molecular weight was favorable.
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