JP2008274249A - Resin particles, method for producing the same, and silicone oil dispersion thereof - Google Patents

Abstract

Disclosed are fine particles having excellent dispersion stability in silicone oil useful for image display elements, electrorheological fluids, optical elements, cosmetics, inks, paints, lubricants, and the like, and a method for producing the same.
In a non-polar solvent, a silicone macromonomer and a vinyl monomer are dispersed while being irradiated with ultrasonic waves in the presence of a dispersant that is a copolymer of a silicone macromonomer and a vinyl monomer. The above-mentioned problems are solved by a method for producing resin particles characterized by polymerization.
[Selection] Figure 1

Description

  The present invention relates to resin particles, a production method thereof, and a silicone oil dispersion thereof. More specifically, the present invention relates to a method for producing resin particles obtained in the presence of a specific dispersant. The resin particles of the present invention have excellent dispersion stability in silicone oil, and are useful as raw materials for image display elements, electrorheological fluids, optical elements, cosmetics, inks, paints, lubricants, and the like.

In recent years, resin particles having a particle size of submicron or less have been used in various fields such as electronics, optics, cosmetics, paints, and machinery.
In general, methods for producing resin particles having a particle size of submicron or smaller include emulsion polymerization methods in water, soap-free polymerization methods, dispersion polymerization methods in organic solvents, and the like (for example, non-patent documents). 1).

However, resin particles produced by these polymerization methods have poor compatibility with the medium when dispersed in a medium (for example, silicone oil) and used as electrophoretic particles for image display elements or particles for viscous fluid. Therefore, there is a problem that the particles aggregate in the medium, the particles are not uniformly dispersed, and good fluidity of the particles cannot be obtained.
Therefore, various attempts have been reported to improve the dispersion stability of resin particles in a medium by producing resin particles using a silicone macromonomer as a dispersant.

  For example, there is a method for preventing aggregation of particles by adding a dispersant obtained by copolymerizing a silicone macromonomer to silicone oil used as a medium for an electrorheological fluid, and dispersing the particles in silicone oil containing a dispersant (for example, Patent Document 1).

  Also known is a method for producing resin particles having excellent dispersion stability in a medium, which comprises copolymerizing 2-vinylnaphthalene and a silicone macromonomer in a nonpolar solvent (for example, Patent Document 2). And Non-Patent Document 2).

Japanese Unexamined Patent Publication No. 6-172772 JP 2006-96985 A Polymer, Vol. 44, p.291, May, 1995, The Society of Polymer Science, Japan Nanotechnology Program (Nanofabrication / Measurement Technology) Functional Capsule Utilization Full Color Rewritable Paper Project, 2003-2005 Results Report, 506-524, 2006, Chemical Technology Strategy Promotion Organization

  The method described in Patent Document 1 is useful when the particle size is relatively large, in other words, when the particles settle and are relatively easily dispersed by the flow of the medium. However, since the dispersant is not immobilized on the particle surface, it is necessary to use a large amount of the dispersant when resin particles having a particle size of submicron or less are used. Therefore, the malfunction that the viscosity of the dispersion of a resin particle and a medium rises arises.

The method described in Patent Document 2 or Non-Patent Document 2 is based on the premise that a vinyl monomer called 2-vinylnaphthalene is used.
The inventors changed 2-vinylnaphthalene to a general vinyl monomer such as methyl methacrylate and styrene, and as a result of the additional test, particles aggregated during the polymerization and stably dispersed in the medium. It has been found that micron resin particles could not be obtained.

  Thus, as a result of earnest efforts, the inventors have used general dispersants such as methyl methacrylate and styrene when a specific dispersant is used and resin particles are produced under ultrasonic irradiation. Surprisingly, it has been found that resin particles having a particle size of submicron or less excellent in dispersion stability in a medium can be obtained even when using.

Thus, according to the present invention, in the presence of a dispersant that is a copolymer of a silicone macromonomer and a vinyl monomer, the silicone macromonomer and the vinyl monomer are ultrasonicated in a nonpolar solvent. Disclosed is a method for producing resin particles, particularly positively charged resin particles, characterized by being dispersed and polymerized while being irradiated.
Further, according to the present invention, there are provided resin particles obtained by the above production method, particularly positively charged resin particles and silicone oil dispersions thereof.

  According to the present invention, it is possible to obtain resin particles having a particle size of submicron or less, particularly positively charged resin particles, excellent in dispersion stability in a medium. Further, the same effect can be obtained with resin particles further containing a pigment.

  Since the resin particles of the present invention, especially positively charged resin particles, are excellent in dispersion stability in a medium, they are used as raw materials for image display elements, electrorheological fluids, optical elements, cosmetics, inks, paints, lubricants, and the like. It can be used suitably.

Hereinafter, the present invention will be described in detail.
The method of the present invention is characterized in that a silicone macromonomer and a vinyl monomer are dispersed and polymerized in a nonpolar solvent in the presence of a specific dispersant while irradiating with ultrasonic waves.
The specific dispersant is a copolymer composed of a silicone macromonomer and a vinyl monomer.

  The inventors of the present invention, as shown in FIG. 1, in the dispersion polymerization in which a silicone macromonomer and a vinyl monomer are copolymerized in a nonpolar solvent, the silicone macromonomer and the vinyl monomer are copolymerized. Dispersant 2 which is a polymer is present on the surface of resin particles 1 precipitated in a nonpolar solvent by dispersion polymerization, functions as a dispersant for achieving dispersion stability, and dispersant 2 which is a copolymer. However, it is assumed that the resin particles 1 and the silicone chain portion 4 of the resin particles 1 are physically fixed by affinity or the like. In FIG. 1, 3 indicates the site of the silicone chain derived from the silicone macromonomer constituting the dispersant, and 5 indicates the site of the copolymer chain derived from the silicone macromonomer and vinyl monomer constituting the dispersant. To do.

  This estimation is based on the use of an organic solvent such as isopropyl alcohol in which a copolymer of a silicone macromonomer and a vinyl monomer is soluble, and it contains a crosslinking component such as ethylene glycol dimethacrylate and is insoluble in the organic solvent. This is based on the fact that the inventors have confirmed that the dispersion stability of the resin particles in the silicone oil is lower after washing the resin particles than before washing.

The silicone macromonomer that is a copolymer component of the dispersant used in the dispersion polymerization of the present invention has a polymerizable unsaturated group at one end and a silicone unit (an organosiloxane unit such as a dimethylpolysiloxane unit). Various compounds can be used in a timely manner.
Examples of such silicone macromonomers include the following formula:

(R ₁ is a hydrogen atom or a methyl group, R ₂ is an alkylene group of C2-4, R ₃ is an alkyl group or a phenyl group C1 -4, n is an integer)
The thing which has a structure shown by these is mentioned.
In the above formula, examples of the C ₂ -C ₄ alkylene group represented by R ₂ include ethylene, trimethylene, tetramethylene groups and positional isomers thereof.
Examples of the C ₁ -C ₄ alkyl group represented by R ₃ include methyl, ethyl, propyl, butyl groups and positional isomers thereof.
N represents an integer between 3 and 500, preferably between 10 and 250.

  The molecular weight of the silicone macromonomer is preferably in the range of a number average molecular weight of 500 to 40000, more preferably 1000 to 20000. A mixture of two or more of the above silicone macromers may be used.

  More specific examples of the silicone macromonomer include α-butyl-ω- (3-methacryloxypropyl) polydimethylsiloxane.

  The dispersant according to the present invention is obtained by, for example, adding a silicone macromonomer and a vinyl monomer to a nonpolar solvent and heating the mixture with stirring according to a conventional method. It can be obtained by copolymerization in a nonpolar solvent. A polymerization initiator may be used for the copolymerization.

The specific polymerization initiator is not particularly limited as long as it is a radical polymerization initiator.
As radical polymerization initiators, for example, azobisisobutyronitrile, 2,2′-azobis (2-methylbutyronitrile), 2,2′-azobis (2,4-dimethylvaleronitrile), 4,4′- Azo initiators such as azobis (4-cyanovaleric acid) and 2,2′-azobis (2-methylpropionamidine); and benzoyl peroxide, halochlorobenzoyl peroxide, lauroyl peroxide and t-butyl peroxide Examples thereof include peroxide-based initiators such as benzoate.
The polymerization initiator is preferably preliminarily dissolved in the monomer composition (mixture of silicone macromonomer and vinyl monomer) in an amount of about 0.1 to 5% by weight.

  The vinyl monomer that can be used in the present invention is not particularly limited, and various commonly used vinyl monomers can be used. For example, styrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, p-ethylstyrene, 2,4-dimethylstyrene, pn-butylstyrene, p-tert-butylstyrene, pn-hexyl Styrene, pn-octyl styrene, pn-nonyl styrene, pn-decyl styrene, pn-dodecyl styrene, n-methoxy styrene, p-phenyl styrene, p-chloro styrene, 3,4-di Styrenes such as chlorostyrene and derivatives thereof; vinyl halides such as vinyl chloride, vinylidene chloride, vinyl bromide and vinyl fluoride; vinyl esters such as vinyl acetate, vinyl propionate, vinyl benzoate and vinyl butyrate; acrylic Methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, Propyl acrylate, n-octyl acrylate, dodecyl acrylate, 2-ethylhexyl acrylate, stearyl acrylate, 2-chloroethyl acrylate, phenyl acrylate, methyl α-chloroacrylate, methyl methacrylate, methyl methacrylate, methacryl Propyl acid, n-butyl methacrylate, isobutyl methacrylate, n-octyl methacrylate, dodecyl methacrylate, 2-ethylhexyl methacrylate, stearyl methacrylate, phenyl methacrylate, dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate, acrylic Α-methylene aliphatic monocarboxylic acid esters such as diethylaminoethyl acetate and diethylaminoethyl methacrylate; acrylonitrile, methacrylonitrile, acrylamide, methacrylate Acrylic acid or methacrylic acid derivatives such as amide, 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl methacrylate; acrylic acid, methacrylic acid, maleic acid, fumaric acid, etc. Fatty acids having a double bond in the molecule can be used.

  In addition, vinyl ethers such as vinyl methyl ether, vinyl ethyl ether, vinyl isobutyl ether; vinyl ketones such as vinyl methyl ketone, vinyl hexyl ketone, methyl isopropenyl ketone; N-vinyl pyrrole, N-vinyl carbazole, N-vinyl indole, N-vinyl compounds such as N-vinylpyrrolidone, vinyl naphthalene salts, and the like can be used alone or in combination of two or more in a range not impeding the effects of the present invention.

Further, a compound having two or more polymerizable double bonds may be added as a vinyl monomer. Such a compound also serves as a crosslinking agent.
Examples of the crosslinking agent include aromatic divinyl compounds such as divinylbenzene, divinylnaphthalene and derivatives thereof, and diethylenic carboxylic acid esters such as ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, triethylene glycol triacrylate, and trimethylolpropane triacrylate. , N, N-divinylaniline, divinyl ether, divinyl sulfite and other divinyl compounds and compounds containing three or more vinyl groups, and the like can be used alone or in combination of two or more.

The vinyl monomer for producing the dispersant is preferably used in an amount of 2 to 50 parts by weight with respect to 100 parts by weight of the silicone macromonomer for producing the dispersant.
When the amount is less than 2 parts by weight, the affinity with the resin particles is deteriorated, so that it is difficult to physically fix the resin particles. As a result, the dispersion stability of the resin particles is deteriorated, which is not preferable.
Moreover, when more than 50 weight part, since affinity with a nonpolar solvent worsens and the dispersion stability of a resin particle worsens, it is unpreferable. A more preferable usage amount is 5 to 25 parts by weight.
Further, by using a vinyl monomer having no electron-donating group as a vinyl monomer used for producing the dispersant, for example, methyl methacrylate, the polarity of the resin particles in the silicone oil can be clearly made positive. .

  Non-polar solvents that can be used for producing the dispersant according to the present invention include paraffinic hydrocarbons such as pentane, hexane, heptane, octane, nonane, decane, and dodecane, isoparaffinic hydrocarbons such as isohexane, isooctane, and isododecane, and liquid paraffin. And silicone oils such as alkyl naphthenic hydrocarbons such as dimethyl silicone oil, phenyl methyl silicone oil, dialkyl silicone oil, alkyl phenyl silicone oil, cyclic polydialkyl siloxane or cyclic polyalkyl phenyl siloxane.

  Of these, silicone oils such as dimethyl silicone oil, phenylmethyl silicone oil, dialkyl silicone oil, alkylphenyl silicone oil, cyclic polydialkylsiloxane, or cyclic polyalkylphenylsiloxane are preferred in consideration of environmental influences such as the working environment.

  In order to efficiently disperse by ultrasonic waves in the production of the dispersant, the silicone oil used is more preferably an oil having a kinematic viscosity measured by JIS K 2283 of 100 centistokes or less.

  The amount of the nonpolar solvent used for the preparation of the copolymer as a dispersant is preferably 20 to 400 parts by weight, more preferably 50 to 200 parts by weight with respect to 100 parts by weight of the monomer composition.

  The reaction temperature and time in the above copolymerization are not particularly limited. Can be used. Preferably, the reaction can be carried out at a reaction temperature of 40 to 120 ° C. and a reaction time of 0.5 to 50 hours. More preferably, the reaction temperature is 40 to 80 ° C., and the reaction time is 2 to 25 hours.

  The polymerization atmosphere may be an air atmosphere or an inert gas atmosphere. Among these, it is preferable to carry out in an inert gas atmosphere in order to prevent polymerization rate delay and polymerization inhibition due to oxygen in the atmosphere. Examples of such an inert gas include nitrogen gas and argon gas. In particular, a nitrogen gas atmosphere is preferable from the economical aspect.

  Here, the obtained dispersant may or may not be separated from the nonpolar solvent used after the production of the dispersant. When not separated, a dispersant dispersed or dissolved in a nonpolar solvent can be used as it is for the production of resin particles.

As the silicone macromonomer used for the production of the resin particles according to the present invention, a silicone macromonomer exemplified in the production of the dispersant can be selected and used.
Moreover, as a vinyl-type monomer used for manufacture of the resin particle by this invention, it can select and use from the vinyl-type monomer illustrated in manufacture of the said dispersing agent.

In the production of the resin particles according to the present invention, the vinyl monomer is preferably used in an amount of 50 to 500 parts by weight with respect to 100 parts by weight of the silicone macromonomer.
When the amount of the vinyl monomer used is less than 50 parts by weight, the resulting copolymer of the silicone macromonomer and the vinyl monomer is in a fibrous form, making it difficult to obtain the desired resin particles. Moreover, since it will become easy to occur aggregation of resin particles at the time of resin particle manufacture when it exceeds 500 weight part, it is not preferable.
A more preferable use amount is 100 to 400 parts by weight.

  In the production of the resin particles of the present invention, the polymerization initiator used in the dispersion polymerization can be selected from the polymerization initiators exemplified in the production of the dispersant, and the same use amount can be used. At that time, the polymerization initiator is usually used after being dissolved in a vinyl monomer.

  Moreover, as a nonpolar solvent used for the dispersion polymerization under the ultrasonic irradiation for manufacturing a resin particle, it can select and use from the nonpolar solvent illustrated in manufacture of the said dispersing agent. As a usage-amount of this nonpolar solvent, 400-1900 weight part is preferable with respect to 100 weight part of monomer compositions, for example, More preferably, it is 400-900 weight part.

The production of the resin particles according to the present invention involves the production of a silicone macromonomer and a vinyl monomer in a nonpolar solvent in the presence of a dispersant that is a copolymer of a silicone macromonomer and a vinyl monomer. It is carried out by dispersion polymerization under sonic irradiation.
The ratio of the dispersant to the vinyl monomer is preferably 20 to 400 parts by weight with respect to 100 parts by weight of the vinyl monomer. If the amount is less than 20 parts by weight, the resin particles tend to aggregate during the production of the resin particles, which is not preferable. On the other hand, when the amount is more than 400 parts by weight, the obtained resin particles tend to be fibrous, and the desired resin particles are difficult to obtain. More preferably, it is 40-200 weight part.
The ratio of the silicone macromonomer and the vinyl monomer is preferably 20 to 200 parts by weight with respect to 100 parts by weight of the vinyl monomer. If the proportion of the silicone macromonomer is less than 20 parts by weight, it is difficult to fix the dispersant on the particle surface, and the dispersion stability of the particles decreases with time, which is not preferable. On the other hand, when the amount is more than 200 parts by weight, the obtained resin particles tend to be fibrous, and it is difficult to obtain desired resin particles. More preferably, it is 25 to 100 parts by weight.

  The dispersion polymerization reaction under ultrasonic irradiation is preferably performed in an inert atmosphere for the same reason as in the above-described method for producing a dispersant. A more preferable inert atmosphere is a nitrogen gas atmosphere.

  The reaction temperature and time in the above dispersion polymerization are not particularly limited, and can be adjusted as appropriate depending on the type and amount of polymerization initiator used and the amount of vinyl monomer used in the reaction. It is. Preferably, the reaction can be carried out at a reaction temperature of 40 to 120 ° C. and a reaction time of 0.5 to 50 hours. More preferably, the reaction temperature is 40 to 80 ° C., and the reaction time is 2 to 12 hours.

  Ultrasonic irradiation is a method of irradiating ultrasonic waves by immersing a container containing a mixed solution to be used for reaction in a generally used ultrasonic cleaning device with a medium such as warm water, or generating internal irradiation type ultrasonic waves. Using an apparatus or the like, it can be performed by a method of irradiating ultrasonic waves by inserting an ultrasonic vibrator into a container containing a mixed solution to be subjected to reaction.

  The ultrasonic transmission frequency is preferably 16 kHz or more, and more preferably in the range of 20 to 500 kHz. The output is preferably 10 to 1000 W per 1 L of the medium irradiated with ultrasonic waves.

  In addition, a mechanical stirring device such as a magnetic stirrer can be used in combination for dispersion polymerization under ultrasonic irradiation.

  Alternatively, the polymerization temperature (reaction temperature) may be adjusted by circulating a medium whose temperature is controlled by an external temperature controller in the ultrasonic cleaning apparatus.

The particle diameter of the resin particles can be controlled by the amount of the dispersant used and the selection of the vinyl monomer used.
For example, the particle diameter of the resin particles can be reduced by increasing the proportion of the dispersant used relative to the vinyl monomer used. Moreover, the particle diameter of the resin particles can also be reduced by selecting and using a vinyl monomer having high affinity for the nonpolar solvent.

  The average particle diameter of the resin particles is preferably 0.02 to 1.0 μm, and more preferably 0.05 to 0.8 μm. This is because when the average particle size is smaller than 0.02 μm, the viscosity of the nonpolar solvent increases during polymerization, and as a result, it becomes difficult to produce resin particles having stable average particles, and when the average particle size is larger than 1.0 μm, This is not preferable because the dispersion stability in oil is lowered.

  The resin particles may further contain a pigment. As the pigment, organic pigments or inorganic pigments well known to those skilled in the art can be suitably used.

  For example, black pigments include carbon black (CI Pigment Black 7) such as furnace black, lamp black, acetylene black, channel black, or copper oxide, iron oxide (CI Pigment Black 11). And metal pigments such as titanium oxide, and organic pigments such as aniline black (CI Pigment Black 1).

  Further, as pigments, CI Pigment Yellow 1, 3, 12, 13, 14, 17, 24, 34, 35, 37, 42 (yellow iron oxide), 53, 55, 74, 81, 83, 95 97, 98, 100, 101, 104, 108, 109, 110, 117, 120, 138, 153, CI Pigment Red 1, 2, 3, 5, 17, 22, 23, 31, 38, 48 : 2, 48: 2, 48: 3, 48: 4, 49: 1, 52: 2, 53: 1, 57: 1, 60: 1, 63: 1, 63: 2, 64: 1, 81, 83 , 88, 101 (Bengara), 104, 105, 106, 108, 112, 114, 122 (Quinacridone magenta), 123, 146, 149, 166, 168, 170, 172, 177, 178, 179, 185, 190, 193, 209, 219, CI Pig Blue 1, 2, 15, 15: 1, 15: 2, 15: 3, 15: 4, 15: 6, 16, 17: 1, 56, 60, 63, CI Pigment Green 1, 4, 7 , 8, 10, 17, 18, 36, etc. can also be used.

The pigment can be mixed in the dispersant or the resin particles by dispersing in a non-polar solvent by a conventional method and then polymerizing.
The apparatus for dispersing the pigment is not particularly limited, and examples thereof include a media type dispersing apparatus such as a ball mill, an attritor, and a sand mill, a shear type dispersing apparatus such as a homomixer, a homogenizer, and a biomixer, and an ultrasonic dispersing apparatus. It is done.

  The obtained resin particles may be taken out from the nonpolar solvent, and can be used without being taken out depending on applications. The extracted resin particles can be washed with a nonpolar solvent as necessary. Further, the washed resin particles may be dispersed in a nonpolar solvent and distributed.

  The resin particles of the present invention are excellent in dispersion stability in a nonpolar solvent (for example, silicone oil). The resin particles of the present invention can be suitably used as a raw material for image display elements, electrorheological fluids, optical elements, cosmetics, inks, paints, lubricants and the like by utilizing this property.

Hereinafter, the present invention will be described in more detail based on examples, but the present invention is not limited to these examples. In addition, the measuring method of the various values in an Example and a comparative example is described below.
(Number average molecular weight)
The number average molecular weight was measured using gel permeation chromatography (GPC). In addition, a number average molecular weight means a polystyrene (PS) conversion number average molecular weight. The measuring method is as follows.
Measuring device: GPC HLC-8020 manufactured by Tosoh Corporation
Guard column: TOSOH TSKguardcolumn HHR (S) x 1 (7.5 mm ID x 7.5 cm)
Column: TOSOH TSK-GEL GMHHR-H (S) × 3 (7.8 mm ID × 30 cm)
Measurement conditions: column temperature (40 ° C.), mobile phase (primary THF / 45 ° C.),
S. PUMP / R. PUMP flow rate (0.8 / 0.5 mL / min),
RI temperature (35 ° C), INLET temperature (35 ° C),
Measurement time (55 min), detector (UV254 nm, RI)
Measurement method: 50 mg of a sample was dissolved overnight in 10 mL primary THF (mobile phase), and filtered through a 0.45 μm or 0.20 μm filter.
Standard polystyrene for calibration curve: manufactured by Showa Denko KK, trade name “shodex” weight average molecular weight: 1030000, manufactured by Tosoh Corporation, weight average molecular weight: 5480000, 3840000, 355000, 102000, 37900, 9100, 2630, 495

(Average particle size)
The average particle diameter here means a Z average particle diameter measured using a method called a dynamic light scattering method. That is, the silicone oil dispersion of resin particles was irradiated with laser light, and the intensity of scattered light scattered from the resin particles was measured with a time change in units of microseconds. This is a Z average particle size obtained by a cumulant analysis method for calculating an average particle size by applying a scattering intensity distribution caused by the detected resin particles to a normal distribution. This type of average particle diameter can be easily measured with a commercially available measuring apparatus. In this example, “Zeta Sizer Nano ZS” commercially available from Malvern was used for the measurement.
The above-mentioned commercially available measuring apparatus is equipped with data analysis software, and the Z average particle diameter was calculated by automatically analyzing the measurement data.

(Kinematic viscosity)
The kinematic viscosity was measured according to JIS K 2283 (crude viscosity and petroleum product kinematic viscosity test method).

(Measurement of electrification of particles)
In a 20 ml glass bottle, weigh the silicone oil dispersion described in the examples, and then add silicone oil (kinematic viscosity: 1 centistokes, KF-96L-1CS, manufactured by Shin-Etsu Chemical Co., Ltd.) so that the solid content of the resin particles is 1 wt%. ) To give 10 g, which was used as a measurement sample.
Next, parallel plates with two glass plates coated with indium tin oxide (ITO) on one side, with the coated surface facing inward and a spacer with a copper tape attached between the glass plates, with a spacing of 1 mm between the glass plates (Jig) was prepared.

  The jig was immersed in the measurement sample, a voltage of +100 V was applied to the left side of the jig, and the sample was allowed to stand for 10 seconds. After 10 seconds, the jig is pulled up from the measurement sample. If particles adhere to the left glass plate, the chargeability of the particles is negative. If particles adhere to the right glass plate, the particles are charged. Was rated as positive.

Example 1
(Production of dispersant)
Into a 300 ml separable flask, 97.2 g of silicone oil (kinematic viscosity: 1 centistokes, KF-96L-1CS, manufactured by Shin-Etsu Chemical Co., Ltd.) and 2,2′-azo-bis- (2,4-dimethylvalero) as an initiator in advance. Methyl methacrylate (7.2 g) in which 0.97 g of nitrile was dissolved and 90.0 g of silicone macromonomer (Silaplane FM-0721, manufactured by Chisso, number average molecular weight 5900) were added. The resulting mixture was subjected to solution polymerization for 20 hours while stirring at 50 ° C. under a nitrogen atmosphere. The obtained reaction product was a colorless and transparent liquid. Hereinafter, this reaction product was used as it was as a dispersant (solid content concentration 50%) in Examples and Comparative Examples.

Example 2
In a 300 ml separable flask, silicone oil (KF-96L-1CS, manufactured by Shin-Etsu Chemical Co., Ltd.) 176.0 g, lauroyl peroxide 0.72 g, methyl methacrylate 11.2 g, silicone macromonomer (Silaplane FM-0721, Chisso) 4.8 g and the dispersant obtained in Example 1 were added. The obtained mixture was subjected to dispersion polymerization for 8 hours under ultrasonic irradiation at 60 ° C. in a nitrogen atmosphere.

  For ultrasonic irradiation, a 300 ml separable flask is immersed in a cleaning tank (internal dimensions: L230 mm × W180 mm × H110 mm) of an ultrasonic cleaning machine (VS-150, manufactured by VELVO-CLEAR) with an output of 150 W, and water in the tank is 60 It carried out in the state kept at ℃ constant temperature.

After completion of the dispersion polymerization, the resin particles were precipitated and separated by centrifugation, and dispersed again in silicone oil (KF-96L-1CS, manufactured by Shin-Etsu Chemical Co., Ltd.). This operation was repeated 3 times, and the resin particles were washed to remove reaction residues such as a polymerization initiator. Thereafter, the resin particles were further dispersed in silicone oil to obtain a silicone oil dispersion of resin particles having a solid content of 8%. The average particle diameter of the obtained resin particles in the silicone oil solvent was 301 nm, and no precipitation of particles was observed even after one week had passed after the silicone oil dispersion.
When the chargeability of the obtained resin particles was measured, it was found that the particles were positively charged.

Examples 3-7 and Comparative Example 1
The same operation as in Example 2 was carried out except that the dispersant, vinyl monomer, etc. in Example 1 were changed as shown in Table 1.
The chargeability of each obtained resin particle is also shown in Table 1, but the resin particle obtained in Comparative Example 1 was agglomerated and solidified, so the chargeability of this particle could not be measured.

Example 8
In a 300 ml glass bead pot containing 500 g of zirconia beads (diameter 5 mm), 60.0 g of silicone oil (KF-96L-1CS, manufactured by Shin-Etsu Chemical) and 10.0 g of the dispersant obtained in Example 1 and magenta as a pigment 2.0 g of pigment (CROMOFUTAL Pink PT, manufactured by Ciba Specialty Chemicals) was added, and the pigment was dispersed by a bead mill at room temperature for 24 hours.
Next, 61.6 g of the above solution (52.0 g of silicone oil, 8.0 g of the dispersant obtained in Example 1, 1.6 g of magenta pigment) was transferred to a 300 ml separable flask. In this flask, 128.0 g of silicone oil (KF-96L-1CS, manufactured by Shin-Etsu Chemical), 8.0 g of methyl methacrylate in which 0.72 g of lauroyl peroxide was dissolved in advance as an initiator, silicone macromonomer (FM-0721, Chisso) Product, number average molecular weight 5900) 4.8 g and ethylene glycol dimethacrylate 1.6 g. Thereafter, the same operation as in Example 2 was performed to obtain a silicone oil dispersion of resin particles having a solid content of 8%. The average particle diameter of the obtained resin particles in the silicone oil solvent was 403 nm, and no precipitation of particles was observed even after one week had passed after the silicone oil dispersion.
When the chargeability of the obtained resin particles was measured, it was found that the particles were positively charged.

Example 9
A silicone oil dispersion of resin particles having a solid content of 8% was carried out in the same manner as in Example 8 except that 2.0 g of a cyan pigment (IRGALITE Blue GLO, manufactured by Ciba Specialty Chemicals) was used instead of the magenta pigment. Got. The average particle diameter of the obtained resin particles in the silicone oil solvent was 424 nm, and no precipitation of particles was observed even after one week had passed after the silicone oil dispersion.
When the chargeability of the obtained resin particles was measured, it was found that the particles were positively charged.

Comparative Example 2
As a result of performing the same operation as in Example 8 except that the silicone macromonomer was not added, the entire system was solidified by aggregation. Moreover, the pigment was not taken in in the particle | grains but the white layer was seen.
Also, the chargeability of the resin particles could not be measured because the resin particles aggregated.

Comparative Example 3
As a result of performing the same operation as in Example 2 except that ultrasonic stirring was not performed and mechanical stirring was performed instead, particles were coalesced during dispersion polymerization, and the viscosity of the reaction solution was increased. The operation was terminated because the entire system solidified.
Also, the chargeability of the resin particles could not be measured because the resin particles aggregated.

  The amount of each composition used for the production of the resin particles in Examples 2 to 9 and Comparative Examples 1 to 3, the particle diameter of each resin particle obtained, and after one week of the silicone oil dispersion of each resin particle The following table shows the results of examining the state of the resin particles and the chargeability of each resin particle.

From Table 1, it can be seen that the resin particles of the examples had good dispersibility in silicone oil and little aggregation of the particles. On the other hand, Comparative Example 1 that does not use a silicone macromonomer for resin particles, Comparative Example 2 that does not use a dispersant, and Comparative Example 3 that does not irradiate ultrasonic waves all have resin particles agglomerated, and therefore, dispersibility in silicone oil is high. It turns out that it was very bad.
Further, when the chargeability of the resin particles of Examples 2 to 9 was examined, it was found that all of these resin particles were positively charged resin particles.
Moreover, since all of the resin particles of Comparative Examples 1 to 3 were aggregated, the chargeability of these resin particles could not be measured.

Example 10
The resin particles crosslinked with ethylene glycol dimethacrylate obtained in Examples 7 to 9 were each washed with isopropyl alcohol. Next, the particles were air-dried and further isopropyl alcohol was removed by drying under reduced pressure, and then added to silicone oil and dispersed by ultrasonic irradiation to obtain a silicone oil dispersion having a solid content of 8%. In the obtained silicone oil dispersion, unlike the results of Examples 7 to 9, precipitation of particles was observed over time. From this result, the resin particles of the present invention have been inferred to have the structure shown in FIG.

  The resin particles according to the present invention are excellent in dispersion stability in silicone oil and are non-aggregating particles, so there is no fear of particle shape change over time, and even without containing a charge control agent such as a dispersant. Since it exhibits chargeability, it can be usefully used in image display elements, electrorheological fluids, optical elements, cosmetics, inks, paints, lubricants, and the like.

It is a schematic explanatory drawing of the resin particle of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Resin particle 2 Dispersant which is copolymer 3 Silicone chain part derived from silicone macromonomer constituting dispersant 4 Silicone chain part derived from silicone macromonomer constituting resin particle 5 Silicone macromonomer constituting dispersant Site of copolymer chain derived from vinyl monomer

Claims (8)

  In the presence of a dispersant, which is a copolymer of a silicone macromonomer and a vinyl monomer, in a nonpolar solvent, the silicone macromonomer and the vinyl monomer are dispersed and polymerized while being irradiated with ultrasonic waves. A method for producing a resin particle.   The method for producing tree seed particles according to claim 1, wherein the resin particles are positively charged resin particles.   The method for producing resin particles according to claim 1, wherein the nonpolar solvent is a silicone oil having a kinematic viscosity of 100 centistokes or less.   The method for producing resin particles according to claim 1, wherein the nonpolar solvent further contains a pigment.   Resin particles obtained by the method for producing resin particles according to any one of claims 1 to 4.   The resin particles according to claim 5, wherein the resin particles are positively charged resin particles.   7. The positively charged resin particle according to claim 5, wherein the resin particle has an average particle diameter in the range of 0.02 μm to 1.0 μm.   A silicone oil dispersion of positively charged resin particles according to any one of claims 5 to 7.

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