Defoaming agent and lubricating oil composition
A technology of defoaming agent and polymer, which is applied in lubricating compositions, additives, petroleum industry, etc., can solve problems such as increased foaming, oil film rupture, and accelerated deterioration of lubricating oil, so as to inhibit the decline of defoaming performance and maintain defoaming performance The effect of foam performance
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manufacture example 1~10
[0172] (Measurement of average particle size of defoamer)
[0173] In the following production examples, regarding the average particle diameter of the antifoaming agent obtained by dispersion polymerization, a dynamic light scattering method measuring device Photal ELSZ-0 (manufactured by Otsuka Electronics Co., Ltd.) was used to dilute the dispersion polymerization liquid with mineral oil. The finished sample (25°C) was measured, and based on the measured results, it was calculated by cumulative analysis.
manufacture example 1
[0175] The defoamer A was produced by dispersion polymerization according to the following procedure.
[0176] Mineral oil (40° C. Kinematic viscosity when: 8.9mm 2 / s) 30 parts by mass, 1.5 parts by mass of polyalkylmethacrylate (weight-average molecular weight Mw=450,000) as a polymer dispersant, and KF2012 (methacrylate modified polydiacrylate) as a defoamer monomer Methylsiloxane; produced by Shin-Etsu Chemical Co., Ltd.; functional group equivalent 4,600g / mol) 3 parts by mass, made into a homogeneous solution under stirring, and then using a diaphragm pump to implement vacuum degassing and nitrogen purging of the reaction system 5 times. Under nitrogen flow, PEROCTA O (1,1,3,3-tetramethylbutyl peroxy-2-ethylhexanoate: 1,1,3,3-tetramethylbutyl peroxy- 2-Ethylhexanoate, peroxide-based radical polymerization initiator; manufactured by NOF Co., Ltd.) 0.15 parts by mass, and then, under a nitrogen atmosphere, stirred at a polymerization temperature of 70°C for 8 hours to car...
manufacture example 2~10
[0178] Except having changed the defoamer monomer, polymer dispersant, radical initiator and their usage amounts as shown in Table 1, the defoamers B to J were produced by dispersion polymerization in the same manner as in Production Example 1.
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