JPH09324134A - Treated carbon black pigment and toner as electrostatic image developer containing the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To simply and efficiently obtain the subject pigment having an improved dispersibility into a solid or a liquid base material without using any complex processes by bringing a polymer during a growing radical is not deactivated into contact with carbon black. SOLUTION: This pigment is obtained by radically polymerizing (A) a radically polymerizable monomer to obtain (B) a polymer in the radical polymerization state and bringing the component B into contact with (C) carbon black during a growing radical is not deactivated. Preferably, the component B has 500-10×10<4> weight-average molecular weight and the component A has an activated surface and contains at least one kind of monomer selected from the group comprising vinyl acetate, styrene and its derivative.

Description

Detailed Description of the Invention

[0001]

FIELD OF THE INVENTION This invention relates to carbon black treated with high molecular weight polymers. For more information,
The present invention relates to a treated carbon black pigment obtained by subjecting a polymer in a process in which growth radicals are not deactivated and carbon black to a contact treatment, and an electrostatic image developing toner containing the pigment.

[0002]

2. Description of the Related Art Conventionally, carbon black has been widely used for various purposes because it has excellent coloring properties and conductivity. However, since carbon black has a powdery or granular shape, it is rarely used alone, and it is usually dispersed in a solid such as rubber or resin or a liquid such as a solvent to exert its characteristics. There are many. However, since carbon black has a high cohesive force between particles and has a weaker affinity with other resins and solvents, it is extremely difficult to uniformly mix or disperse it. Therefore, in order to solve this problem, the surface of the carbon black is coated with various kinds of surfactants or resins to enhance the affinity with a solid or liquid base, thereby uniformly mixing or dispersing the carbon black. Many technologies are being studied.

As a method for improving the dispersibility of carbon black, a method of treating carbon black with a coupling agent (JP-A-63-175869, JP-A-63-15).
8566, British Patent Nos. 1583564, 158341
1) and the like have been studied, but these have a problem that the dispersion of the carbon black after the treatment in the polymerizable monomer is still incomplete and the cost is high. A method of using a monomer component in the presence of carbon black (Japanese Patent Laid-Open No. 64-6965, West German Patent No. 3102823) has also been proposed, but this method has poor grafting efficiency.
The dispersion of carbon black in the polymerizable monomer after grafting was insufficient. Further, a method of treating carbon black by reacting it with an organic compound by a polymer reaction utilizing the surface functional group of carbon black (Japanese Patent Laid-Open No. 1-58242)
-284564, JP-A-5-241378) and the like have also been investigated, but these also did not sufficiently disperse the carbon black after treatment in the polymerizable monomer.

[0004]

SUMMARY OF THE INVENTION The first object of the present invention is as follows.
Is to provide a treated carbon black pigment having improved dispersibility in a solid or liquid base and a treated carbon black pigment easily and efficiently without taking complicated steps. The second object of the present invention is to provide a toner for developing an electrostatic image using the treated carbon black pigment.

[0005]

[Means for Solving the Problems] The present inventors carried out radical bulk or solution polymerization in the presence of an initiator to obtain a polymer having a weight average molecular weight of 500 to 100,000. The treated carbon black obtained by contact treatment with carbon black while the growth radicals of the polymer are not deactivated, has a very good dispersion state in a solid or liquid base. The dispersibility in the body is also very good, and the carbon black is uniformly dispersed by polymerizing a solution in which the treated carbon black is dispersed with a polymerizable monomer, for example, suspension polymerization or emulsion polymerization. It was found that a toner in a state of being obtained was obtained, and the present invention could be reached.

The carbon black used in the present invention may be used as it is, but it is more preferable to use it after activation treatment. The activation treatment refers to removal of water adhering to the surface of carbon black by heating and drying at 100 ° C. or higher, extraction of functional groups and hydrogen of carbon black by irradiation with ozone, UV light, or addition of radicals. Specific examples of the method include drying with a vacuum oven, irradiation with an ozone generator, UV irradiation, a combination thereof, and corona discharge. Further, there are various kinds of carbon black such as channel black, furnace black, acetylene black, and porous black, and any kind of carbon black may be used in the present invention.

The polymer in the radical polymerization process is
The weight average molecular weight thereof is preferably in the range of 500 to 100,000. When carbon black is treated with a polymer having a weight average molecular weight of less than 500, the dispersibility of the carbon black in the polymerizable monomer becomes low, and on the other hand,
When carbon black is treated with a polymer having a weight average molecular weight of more than 100,000, the secondary aggregate of carbon black tends to be dispersed in the polymerizable monomer without being sufficiently reduced. Further, due to further dispersion, the viscosity of the polymerizable monomer increases, so that the suspension or emulsion droplets become large,
The particle size of the particles obtained by polymerization tends to be large. The molecular weight of the polymer refers to the weight average molecular weight determined by gel permeation chromatography using a polystyrene standard. The treated carbon black pigment is formed, for example, by performing radical bulk polymerization or solution polymerization by heating a radical polymerizable monomer in the presence of a radical polymerization initiator for a certain period of time, and then subjecting the carbon black to the radical polymerization reaction product. It can be performed by putting it in and stirring. It is speculated that at least part of the treated carbon black pigment of the present invention is composed of grafted carbon black.

The polymerizable monomer used in the radical polymerization during the treatment of carbon black in the present invention preferably contains vinyl acetate, or styrene or a derivative thereof. This is because styrene derivatives and vinyl acetate have a negative e value, which is a value indicating a relative charge on the double bond, and are more easily grafted to carbon black than those that do not. Radical-polymerizable monomers that can be used in the present invention include vinyl acetate, styrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, p-ethylstyrene, p-methoxystyrene and p-methylstyrene.
Styrene compounds such as bromostyrene, p-chlorostyrene, sodium p-styrenesulfonate, methyl acrylate, ethyl acrylate, n-propyl acrylate, n-butyl acrylate, 2-ethylhexyl acrylate, glycidyl acrylate, etc. Acrylic acid ester compounds, methacrylic acid ester compounds such as methyl methacrylate, ethyl methacrylate, n-propyl methacrylate, n-butyl methacrylate, and 2-ethylhexyl methacrylate, acrylonitrile, acrylamide, N-isopropylacrylamide, N-pi Examples thereof include N-substituted acrylamide compounds such as peryl acrylamide, divinylbenzene, methylenebisacrylamide, and crosslinkable monomers such as 1,3-butanediol dimethacrylate.

The polymerization initiator used in the radical or solution polymerization of the present invention is 2,2'-azobis-isobutyronitrile, 2,2'-azobis- (2,4-dimethylvaleronitrile), 1,1. ′ -Azobis- (cyclohexane-1-carbonitrile), 2,2′-azobis-4-
Diazo compounds such as methoxy-2,4-dimethylvaleronitrile and peroxides such as benzoyl peroxide and lauroyl peroxide are used. An appropriate amount of these polymerization initiators is used to obtain a desired molecular weight, but 0.1 to 10% by weight of the polymerizable monomer is generally added.

The polymerization initiators used in the radical polymerization and suspension polymerization of the present invention are 2,2'-azobis-isobutyronitrile, 2,2'-azobis- (2,4-dimethylvaleronitrile), 1 , 1'-Azobis- (cyclohexane-1-carbonitrile), 2,2'-azobis-4
A diazo compound such as -methoxy-2,4-dimethylvaleronitrile or a peroxide such as benzoyl peroxide or lauroyl peroxide is used. An appropriate amount of these polymerization initiators is used to obtain a desired molecular weight, but 0.1 to 10% by weight of the polymerizable monomer is generally added. The polymerization initiator used in the emulsion polymerization of the present invention includes 2,2'-azobis- (2-aminopropane) dihydrochloride and 2,2'-azobis-
Diazo compounds such as (4-cyanovaleric acid) and peroxides such as potassium persulfate and sodium persulfate are used. The amount of the polymerization initiator used is an appropriate amount to obtain a desired molecular weight, but it is generally 0.1 to 0.1% of the polymerizable monomer.
10% by weight is added.

In the present invention, a suspension stabilizer can be used when preparing the suspension droplets. Examples of the stabilizer used include polyvinyl alcohol, methyl cellulose, ethyl cellulose, hydroxyethyl cellulose, carboxymethyl cellulose, sodium polyacrylate, water-soluble polymers such as sodium polymethacrylate, sodium dodecylbenzenesulfonate, sodium octadecyl sulfate, and sodium oleate. , Anionic surfactants such as sodium laurate, potassium stearate, cationic surfactants such as laurylamine acetate, stearylamine acetate, lauryltrimethylammonium chloride, zwitterionic surfactants such as lauryldimethylamine oxide, poly Oxyethylene alkyl ether, polyoxyethylene alkylphenyl ether, polyoxyethylene alkylamine, etc. Surfactants such as nonionic surfactants, tricalcium phosphate, aluminum hydroxide, barium sulfate,
Examples thereof include inorganic salts such as calcium sulfate and barium carbonate. The amount of these stabilizers used is preferably 0.01 to 20 parts by weight with respect to 100 parts by weight of the polymerizable monomer.

Further, in the present invention, an emulsifier can be used in the preparation of emulsified droplets. Examples of the emulsifier used include, for example, anionic surfactants such as sodium dodecylbenzenesulfonate, sodium octadecyl sulfate, sodium oleate, sodium laurate, and potassium stearate; laurylamine acetate, stearylamine acetate, and lauryltrimethylammonium chloride. Cationic surfactants, zwitterionic surfactants such as lauryl dimethylamine oxide, surfactants such as nonionic surfactants such as polyoxyethylene alkyl ether, polyoxyethylene alkyl phenyl ether, polyoxyethylene alkylamine, etc. Is mentioned. The amount of these emulsifiers used is
It is preferable to use 0.01 to 10 parts by weight with respect to 100 parts by weight of the polymerizable monomer. Also, bulk polymerization of these,
Suspension polymerization and emulsion polymerization are performed in a system without oxygen.

Further, the toner for developing an electrostatic image of the present invention may contain an auxiliary component usually used in electrophotographic toner, for example, a charge control agent. Known charge control agents are used, and examples thereof include nigrosine, azo metal complexes, derivatives of dialkylsalicylic acid, and quaternary ammonium salt compounds. The amount of these used is suitably from 0.1 to 20 parts by weight based on 100 parts by weight of the polymerizable monomer. Further, waxes such as low molecular weight polyethylene, polypropylene, and carnauba wax can be contained for improving the releasability of the electrophotographic toner from the fixing roller during heat fixing. The use amount of these is preferably 1 to 30 parts by weight based on 100 parts by weight of the polymerizable monomer. The carbon black polymer obtained by the present invention is not only a polymerized toner for developing an electrostatic charge image, but also a pulverized toner for developing an electrostatic charge image, a wet toner for developing an electrostatic charge image, an ink ribbon coating agent for thermal transfer, and a thermal transfer. It can also be used as an ink, a back coat agent for a magnetic recording medium, and the like.

[0014]

EXAMPLES The present invention will be specifically described below based on examples.

Example 1 100 parts by weight of styrene and 1 part by weight of 2,2'-azobis- (2,4-dimethylvaleronitrile) were placed in a flask equipped with a stirrer, an inert gas introducing tube, a reflux condenser and a thermometer. Was added and nitrogen gas was blown into the system with stirring to replace oxygen in the system, and the mixture was placed in a water bath at 70 ° C. and polymerized to obtain polystyrene having a weight average molecular weight of 23,000. Carbon black (MA100 manufactured by Mitsubishi Kagaku Co., Ltd.) that was previously treated by irradiating ozone at room temperature with a UV ozone irradiator
20 parts by weight was added and stirring was continued to obtain a treated carbon black pigment. Large secondary aggregates of carbon black were no longer visible.

Example 2 In the same manner as in Example 1, after obtaining polystyrene having a weight average molecular weight of 16000, carbon black (Colum) was preheated and dried in a vacuum oven at 110 ° C.
bian Carbon Co. Made Neospectr
A treated carbon black pigment was obtained in the same manner as in Example 1 except that aII) was added. Large secondary aggregates of carbon black were no longer visible.

Example 3 In the same manner as in Example 1, after obtaining polystyrene having a weight average molecular weight of 60000, the polymer was preheated and dried in a vacuum oven at 110 ° C. to obtain a carbon black (FW200 manufactured by Degussa AG). And add
Similarly, a treated carbon black pigment was obtained. Large secondary aggregates of carbon black were no longer visible.

Example 4 In the same manner as in Example 1, after obtaining polystyrene having a weight average molecular weight of 5000, untreated carbon black (Cab
MON manufactured by OT (Monarch 880) was added thereto and contacted with the polystyrene in the same manner to obtain a treated carbon black pigment. A small amount of large secondary aggregates of carbon black was observed as compared with Examples 1, 2, and 3.

Example 5 In the same manner as in Example 1, after obtaining polystyrene having a weight average molecular weight of 300, untreated carbon black (MA100 manufactured by Mitsubishi Chemical Corporation) was added, and a treated carbon black pigment was obtained in the same manner. . A small amount of large secondary aggregates of carbon black was observed as compared with Examples 1, 2, and 3.

Example 6 30 parts by weight of vinyl acetate, 70 parts by weight of methyl methacrylate, 2,2'-azobis- (2,4) were placed in a flask equipped with a stirrer, an inert gas introducing tube, a reflux condenser and a thermometer. -Dimethylvaleronitrile) 1 part by weight was added, nitrogen gas was blown into the system while stirring at 100 rpm to replace oxygen in the system, and the mixture was placed in a water bath at 70 ° C for polymerization to give a weight average molecular weight of 40.
000 vinyl acetate-methyl methacrylate copolymer was obtained. 20 parts by weight of carbon black (MA100 manufactured by Mitsubishi Kagaku Co., Ltd.) which had been treated by irradiating ozone at room temperature with a UV ozone irradiator was added thereto, and stirring was continued to obtain a treated carbon black pigment. Large secondary aggregates of carbon black were no longer visible.

Example 7 10 parts by weight of methyl acrylate, 90 parts by weight of styrene, 1 part of 2,2'-azobis-isobutyronitrile were placed in a flask equipped with a stirrer, an inert gas introducing tube, a reflux condenser and a thermometer. After adding parts by weight and blowing nitrogen gas while stirring at 100 rpm to replace oxygen in the system, the mixture was placed in a water bath at 60 ° C. and polymerized to obtain a methyl acrylate-styrene copolymer having a weight average molecular weight of 65,000. Carbon black (MA10 manufactured by Mitsubishi Kagaku Co., Ltd.) was previously treated by irradiating ozone at room temperature with a UV ozone irradiator.
0) 20 parts by weight was added, and stirring was continued for further 1 hour to obtain a treated carbon black pigment. Large secondary aggregates of carbon black were no longer visible.

Example 8 After obtaining a butyl acrylate-styrene copolymer having a weight average molecular weight of 10,000 in the same manner as in Example 7, 110 ° C.
Carbon black (MA600 manufactured by Mitsubishi Kagaku Co., Ltd.) previously heated and dried in a vacuum oven of No. 1 was added to obtain a treated carbon black pigment in the same manner. Large secondary aggregates of carbon black were no longer visible.

Example 9 In the same manner as in Example 7, after obtaining a 2-ethylhexyl acrylate-styrene copolymer having a weight average molecular weight of 300,000, untreated carbon black (TBBlack6B manufactured by SINLOIHI) was added, and the same procedure was performed. A treated carbon black pigment was obtained. A small amount of large secondary agglomerates of carbon black as compared with Examples 7 and 8 was observed.

Example 10 100 parts by weight of methyl acrylate was added to a flask equipped with a stirrer, an inert gas introduction tube, a reflux condenser and a thermometer.
2'-azobis- (2,4-dimethylvaleronitrile)
1 part by weight was added, nitrogen gas was blown into the system while stirring at 100 rpm to replace oxygen in the system, and the mixture was placed in a water bath at 60 ° C. for polymerization to obtain methyl polyacrylate having a weight average molecular weight of 50,000. Add 20 parts by weight of carbon black (MA100 manufactured by Mitsubishi Chemical), which was previously treated by irradiating ozone at room temperature with a UV ozone irradiator,
The stirring was further continued to obtain a treated carbon black pigment. In comparison with Examples 7 and 8, the carbon black of 2
Sub-aggregates were observed, though to some extent.

Example 11 30 parts by weight of styrene, 70 parts by weight of butyl acrylate, 2,2'-azobis- (2,4-) were placed in a flask equipped with a stirrer, an inert gas introducing tube, a reflux condenser and a thermometer. 1 part by weight of dimethyl valeronitrile), nitrogen gas was blown into the system while stirring at 100 rpm to replace oxygen in the system, and the mixture was placed in a water bath at 60 ° C. for 0.5 hour to polymerize, and as a polymer in the radical polymerization process, Average molecular weight 6500
After butyl acrylate-styrene copolymer of 0 was added, 20 parts by weight of carbon black (MA100 manufactured by Mitsubishi Kagaku Co., Ltd.), which had been previously treated by irradiation with ozone at room temperature by a UV ozone irradiation device, was added thereto, and further for 1 hour. The stirring was continued to obtain a treated carbon black pigment. Large secondary aggregates of carbon black were no longer visible.

Example 12 In the same manner as in Example 11, a methyl acrylate-styrene copolymer having a weight average molecular weight of 10,000 was prepared as a polymer in the radical polymerization process, and then the methyl acrylate-
Carbon black (made by Mitsubishi Kagaku Co., Ltd.) pre-heated and dried on a styrene copolymer in a vacuum oven at 110 ° C.
MA600) was added and brought into contact to obtain a treated carbon black pigment. Large secondary aggregates of carbon black were no longer visible.

Example 13 In the same manner as in Example 11, a methyl methacrylate-styrene copolymer having a weight average molecular weight of 30,000 was used as a polymer in the radical polymerization process, and the methyl methacrylate-styrene copolymer was not treated. Carbon black (S
TB Black 6B) manufactured by INLOIHI was added and brought into contact with each other to obtain a treated carbon black pigment. Example 5
Compared to 6, the large secondary aggregate of carbon black
It was observed to some extent.

Example 14 In the same manner as in Example 1, after obtaining polystyrene having a weight average molecular weight of 200,000 as a polymer in the radical polymerization process, carbon black (MA10 manufactured by Mitsubishi Kagaku Co., Ltd. manufactured by Mitsubishi Kagaku Co., Ltd.) was preliminarily dried by heating in a vacuum oven at 110 ° C.
0) was added and brought into contact with each other to obtain a treated carbon black pigment. Large secondary aggregates of carbon black were no longer visible.

Example 15 1 g of treated carbon black prepared in Examples 1 to 14
Was dispersed in 10 ml of toluene and allowed to stand, and the sedimentation state of carbon black was observed with the lapse of time, and the dispersibility of carbon black was evaluated. The results are shown in Tables 1 to 3.
It was shown to.

Example 16-1 The treated carbon black pigment was dispersed in a polymerizable monomer and suspension-polymerized to prepare particles, and the results of observing the cross section are shown in Tables 1 to 3. Monomer phase (O) Styrene: 25 parts by weight n-butyl acrylate: 5 parts by weight Treated carbon black pigment prepared in Examples 1, 2, 3, 6, 7, 8, 11, 12: 10 parts by weight Initiator: 1 part by weight 2,2'-azobis- (2,4-dimethylvaleronitrile) aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Polyvinyl alcohol (Poval 217EE manufactured by Kuraray Co., Ltd.): 3 parts by weight Nigrosine: 0. 1 part by weight Styrene, n-butyl acrylate and Examples 1, 2, 3,
The treated carbon black pigments prepared in Nos. 6, 7, 8, 11, and 12 were dispersed by a ball mill, an initiator was added to this to obtain a monomer phase, and the monomer phase was then stirred beforehand to prepare the monomer phase. Put the aqueous dispersion medium phase in the stirring tank,
It was suspended by a homogenizer (made by Tokushu Kika Kogyo).
After replacing this suspension with nitrogen, polymerization was carried out at 60 ° C. The suspension droplet was observed with an optical microscope. After completion of the polymerization, purification is performed using a centrifuge, and then filtration is performed.
The desired particles were obtained by drying under reduced pressure. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. In this measurement result, as shown in Tables 1 to 3, it was observed that all particles contained carbon black, and the size was about 9 microns.

Example 16-2 Similar to Example 15, Examples 4, 5, 9, 10, 1
Suspension polymerization was carried out using the treated carbon black pigments prepared in Nos. 3 and 14 to prepare particles. The dispersibility of the treated carbon black pigment is not as good as that of Example 16-1, but is sufficiently practical and the size is 9
It was about micron. Similarly, the results are shown in Tables 1 to 3.

[Table 1] * ¹ : Weight average molecular weight of treated carbon black pigment (CB) * ² : Settled state when dispersed in toluene (Example 15) * ³ : Dispersibility of carbon black (CB) in polymer particles (Example) 16-1 and Example 16-2) * ⁴ : Average number of carbon black (CB) secondary aggregates per 1 μm ^{2 of} polymer particle cross section * ⁵ : Maximum size of carbon black (CB) secondary aggregates

[0032]

[Table 2]

[0033]

[Table 3]

Example 17 Monomer phase (O) Styrene: 30 parts by weight Treated carbon black pigment prepared in Example 1: 10 parts by weight Initiator: 1 part by weight 2,2'-azobis- (2,4-dimethylvalero) Nitrile) Water-based dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Polyvinyl alcohol (Kuraray's Poval 217EE): 3 parts by weight Nigrosine: 0.1 parts by weight styrene and the treated carbon black pigment prepared in Example 1 are ball milled. After dispersing with, after adding an initiator to this to obtain a monomer phase, the aqueous dispersion medium phase prepared by stirring with the monomer phase in advance is put into a stirring tank, and a homogenizer (made by Tokushu Kika Kogyo) Was suspended at 9500 rpm for 10 minutes. After replacing the suspension with nitrogen, polymerization was carried out at 70 ° C. for 7 hours. When the suspension droplets were observed with an optical microscope, the treated carbon black pigment was found in all suspension droplets. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 4, in this measurement result, it was observed that all particles contained the treated carbon black pigment, and the size was about 9 microns. Here, the maximum diameter of the secondary agglomerates of the treated carbon black pigment in the particles was 0.3 μm or less, and the number of secondary agglomerates of carbon black per 1 μm ^{2 of} its cross section was 3 or more. . A cross-sectional sample of the obtained particles was prepared by the ultrathin section method and observed by a transmission microscope. The results are shown in FIG. It is observed that the treated carbon black pigment is very well dispersed.

Example 18 In the same manner as in Example 17, suspension polymerization was carried out using the treated carbon black pigment prepared in Example 2 to prepare particles. As shown in Table 4, in this measurement result, it was observed that all particles contained the treated carbon black pigment, and the size was about 9 microns.

Example 19 Monomer Phase (O) Styrene: 15 parts by weight n-butyl acrylate: 15 parts by weight Treated carbon black pigment prepared in Example 3: 10 parts by weight Initiator: 1 part by weight 2,2'- Azobis- (2,4-dimethylvaleronitrile) Water-based dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Polyvinyl alcohol (Poval 217EE manufactured by Kuraray Co., Ltd.): 3 parts by weight Nigrosine: 0.1 parts by weight Styrene and acrylic acid n -A butyl and the treated carbon black pigment prepared in Example 3 were dispersed by a ball mill, an initiator was added to this to obtain a monomer phase, and the aqueous dispersion medium prepared by stirring with the monomer phase in advance. Put the phases in a stirring tank and homogenize (made by Tokushu Kika Kogyo)
Was suspended at 9500 rpm for 10 minutes. After replacing the suspension with nitrogen, polymerization was carried out at 70 ° C. for 7 hours. The suspension droplet was observed with an optical microscope. After completion of the polymerization, purification is performed using a centrifuge, and then filtration is performed.
The desired particles were obtained by drying under reduced pressure. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. The results of this measurement are as shown in Table 4,
It was observed that all particles contained the treated carbon black pigment, and the size was about 9 microns.

Example 20 In the same manner as in Example 18, the treated carbon black pigment prepared in Example 4 was used to carry out suspension polymerization to prepare particles. As shown in Table 4, the results of this measurement showed that all the particles contained the treated carbon black pigment,
The size was about 10 microns.

Example 21 Monomer phase (O) Methyl methacrylate: 30 parts by weight Treated carbon black pigment prepared in Example 11: 10 parts by weight Initiator: 1 part by weight 2,2'-azobis- (2,4- Dimethylvaleronitrile) Aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Polyvinyl alcohol (Poval 217EE manufactured by Kuraray Co., Ltd.): 3 parts by weight Nigrosine: 0.1 parts by weight Methyl methacrylate and the treated carbon prepared in Example 11 After dispersing the black pigment with a ball mill, adding an initiator to this to obtain a monomer phase, and then putting the aqueous dispersion medium phase prepared by stirring with the monomer phase in a stirring tank, and then using a homogenizer (special machine 95 made by Kato Kogyo
The suspension was performed at 00 rpm for 10 minutes. After replacing the suspension with nitrogen, polymerization was carried out at 70 ° C. for 7 hours. The suspension droplet was observed with an optical microscope. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 4, in this measurement result, it was observed that all particles contained the treated carbon black pigment, and the size was about 9 microns.

Example 22 Monomer phase (O) Methyl methacrylate: 30 parts by weight Treated carbon black pigment prepared in Example 12: 10 parts by weight Initiator 2,2'-azobis-isobutyronitrile: 1 part by weight Aqueous system Dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Polyvinyl alcohol (Poval 217EE manufactured by Kuraray Co., Ltd.): 3 parts by weight Nigrosine: 0.1 parts by weight Methyl methacrylate and the treated carbon black pigment prepared in Example 12 were ball milled. After dispersing, add an initiator to this to obtain a monomer phase, and then put the aqueous dispersion medium phase prepared by stirring with the monomer phase in a stirring tank and use a homogenizer (manufactured by Tokushu Kika Kogyo). 95
The suspension was performed at 00 rpm for 10 minutes. After replacing the suspension with nitrogen, polymerization was carried out at 70 ° C. for 7 hours. The suspension droplet was observed with an optical microscope. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 4, in this measurement result, it was observed that all the particles contained the treated carbon black pigment, and the size was about 8 μm.

Example 23 In the same manner as in Example 22, suspension polymerization was carried out using the treated carbon black pigment prepared in Example 13 to prepare particles. As shown in Table 4, in this measurement result, it was observed that all particles contained the treated carbon black pigment, and the size was about 8 μm.

Example 24 Monomer Phase (O) Styrene: 30 parts by weight Treated carbon black pigment prepared in Example 1: 10 parts by weight Initiator: 1 part by weight 2,2'-azobis- (2,4-dimethylvalero) Nitrile) Water-based dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Calcium phosphate: 3 parts by weight Sodium dodecylbenzene sulfonate: 0.1 parts by weight Styrene and the treated carbon black pigment prepared in Example 1 were dispersed by a ball mill. After that, an initiator was added to this to obtain a monomer phase, and the aqueous dispersion medium phase prepared by stirring with the monomer phase in advance was put into a stirring tank, and a homogenizer (manufactured by Tokushu Kika Kogyo Co., Ltd.) was operated at 9500 rpm for 10 minutes. Suspended for a minute. After replacing the suspension with nitrogen, polymerization was carried out at 70 ° C. for 7 hours. When the suspension droplets were observed with an optical microscope, the treated carbon black pigment was found in all suspension droplets. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 4, in this measurement result, it was observed that all particles contained the treated carbon black pigment, and the size was about 9 microns.

Example 25 Monomer phase (O) Styrene: 30 parts by weight Treated carbon black pigment prepared in Example 1: 10 parts by weight Initiator: 1 part by weight 2,2'-azobis- (2,4-dimethylvalero) Nitrile) Water-based dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Hydroxypropyl cellulose: 3 parts by weight (Shin-Etsu Chemical Metroze 65SH50) Styrene and the treated carbon black pigment prepared in Example 1 were dispersed by a ball mill, and then this After adding an initiator to obtain a monomer phase, the aqueous dispersion medium phase prepared by stirring with the monomer phase in advance is put into a stirring tank and suspended at 9500 rpm for 10 minutes by a homogenizer (manufactured by Tokushu Kika Kogyo). Let After the suspension was purged with nitrogen, polymerization was carried out at 60 ° C. for 7 hours. When the suspension droplets were observed with an optical microscope, the treated carbon black pigment was found in all suspension droplets. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 4, in this measurement result, it was observed that all particles contained the treated carbon black pigment, and the size was about 9 microns.

Example 26 Monomer phase (O) Styrene: 15 parts by weight n-butyl acrylate: 15 parts by weight Treated carbon black pigment prepared in Example 2: 10 parts by weight Initiator: 1 part by weight 2,2'- Azobis- (2,4-dimethylvaleronitrile) Aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Hydroxypropyl cellulose: 3 parts by weight (Shin-Etsu Chemical Metroz 65SH50) Styrene and n-butyl acrylate and in Example 2 After dispersing the prepared treated carbon black pigment by a ball mill, adding an initiator to this to obtain a monomer phase, and then putting the aqueous dispersion medium phase prepared by stirring with the monomer phase in a stirring tank, Homogenizer (made by Tokushu Kika Kogyo)
Was suspended at 9500 rpm for 10 minutes. After the suspension was purged with nitrogen, polymerization was carried out at 60 ° C. for 7 hours. Also, when observing the suspension droplets with an optical microscope,
The treated carbon black pigment was in every suspension drop. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 4, in this measurement result, it was observed that all particles contained the treated carbon black pigment, and the size was about 9 microns.

Example 27 In the same manner as in Example 17, suspension polymerization was carried out using the treated carbon black pigment prepared in Example 5 to prepare particles. The dispersibility of the treated carbon black pigment is shown in Example 1.
Although it was not as good as 7 to 26, it was sufficiently practical and the size was about 9 microns.

Example 28 In the same manner as in Example 17, suspension polymerization was carried out using the treated carbon black pigment prepared in Example 14 to prepare particles. The dispersibility of the treated carbon black pigment was not as good as that of Examples 17 to 26, but it was sufficiently practical. However, the size of the particles was as large as 16 microns.

The results of Examples 17 to 28 are shown in Table 1 below.

[Table 4] CB represents carbon black * 1: The dispersibility is not as good as in Examples 17 to 26, but it is sufficiently practical.

Comparative Example 1 MA1 manufactured by Mitsubishi Chemical Co., Ltd. was used as untreated carbon black.
00 (trade name), Columbian Carbon
Co. Made NeospectraII (trade name), Deg
ussa A. G. FIG. FW200 (trade name) and C
1 g of Monarch 880 (trade name) manufactured by abot was dispersed in 10 ml of toluene and allowed to stand, and the results of observing the sedimentation state of carbon black with the lapse of time are shown in Table 5.

Comparative Example 2 Untreated carbon black was dispersed in a polymerizable monomer,
Suspension polymerization was performed to prepare particles, and the results of observing the cross section are shown in Table 5. Monomer phase (O) Styrene: 25 parts by weight n-butyl acrylate: 5 parts by weight Untreated carbon black: 10 parts by weight Initiator: 1 part by weight 2,2′-azobis- (2,4-dimethylvaleronitrile) Aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Polyvinyl alcohol (Poval 217EE manufactured by Kuraray Co., Ltd.): 3 parts by weight Nigrosine: 0.1 parts by weight After styrene and untreated carbon black are dispersed by a ball mill, this is After an initiator was added to obtain a monomer phase, an aqueous dispersion medium phase prepared by stirring the monomer phase in advance was placed in a stirring tank and suspended by a homogenizer (made by Tokushu Kika Kogyo). After replacing this suspension with nitrogen, polymerization was carried out at 60 ° C. When the suspension droplets were observed with an optical microscope, some suspension droplets did not contain carbon black. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 5, the results of this measurement showed that some particles did not contain carbon black.

[0049]

[Table 5] * ¹ : Weight-average molecular weight of treated carbon black pigment (CB) * ² : Sedimentation state when dispersed in toluene (Comparative example 1) * ³ : Dispersibility of carbon black (CB) in polymer particles (Comparative example) 2) * ⁴ : Average number of secondary aggregates of carbon black (CB) per 1 μm ^{2 of} polymer particle cross section * ⁵ : Maximum size of secondary aggregate of carbon black (CB)

Comparative Example 3 Monomer phase (O) Styrene: 30 parts by weight Untreated carbon black (MA100 manufactured by Mitsubishi Kasei): 10 parts by weight Initiator: 1 part by weight 2,2'-azobis- (2,4-dimethyl) Valeronitrile) Aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Polyvinyl alcohol (Povale 217EE manufactured by Kuraray Co., Ltd.): 3 parts by weight Nigrosine: 0.1 parts by weight Styrene and untreated carbon black were dispersed by a ball mill. After that, an initiator was added to this to obtain a monomer phase, and the aqueous dispersion medium phase prepared by stirring with the monomer phase in advance was put into a stirring tank, and a homogenizer (manufactured by Tokushu Kika Kogyo Co., Ltd.) was operated at 9500 rpm for 10 minutes. Suspended for a minute. This suspension was replaced with nitrogen and then at 70 ° C. for 7 hours.
The polymerization was carried out. When the suspension droplets were observed with an optical microscope, some suspension droplets did not contain carbon black. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 6 in this measurement result, it was observed that some particles did not contain carbon black. The size was about 9 microns.

Comparative Example 4 Monomer phase (O) Styrene: 30 parts by weight Untreated carbon black (MA100 manufactured by Mitsubishi Chemical Corporation): 10 parts by weight Initiator: 1 part by weight 2,2'-azobis- (2,4-dimethyl) Valeronitrile) Aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Calcium phosphate: 3 parts by weight Sodium dodecylbenzene sulfonate: 0.1 parts by weight After styrene and untreated carbon black are dispersed by a ball mill, After adding an initiator to obtain a monomer phase, an aqueous dispersion medium phase prepared by stirring with the monomer phase in advance is put into a stirring tank and suspended at 9500 rpm for 10 minutes by a homogenizer (manufactured by Tokushu Kika Kogyo). It was This suspension was replaced with nitrogen and then at 70 ° C. for 7 hours.
The polymerization was carried out. When the suspension droplets were observed with an optical microscope, some suspension droplets did not contain carbon black. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 6 in this measurement result, it was observed that some particles did not contain carbon black. The size was about 9 microns.

Comparative Example 5 Monomer phase (O) Styrene: 30 parts by weight Untreated carbon black: 10 parts by weight (Neospectra II manufactured by Columbian Carbon Co.) Initiator: 1 part by weight 2,2'-azobis- (2,4) -Dimethylvaleronitrile) Aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Hydroxypropyl cellulose: 3 parts by weight (Metronose 65SH50 manufactured by Shin-Etsu Chemical Co., Ltd.) Styrene and untreated carbon black are dispersed by a ball mill, and then this After adding an initiator to obtain a monomer phase, the aqueous dispersion medium phase prepared by stirring with the monomer phase in advance is put into a stirring tank and suspended at 9500 rpm for 10 minutes by a homogenizer (manufactured by Tokushu Kika Kogyo). Let The suspension was replaced with nitrogen for 7 hours at 60 ° C.
The polymerization was carried out. When the suspension droplets were observed with an optical microscope, some suspension droplets did not contain carbon black. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 6 in this measurement result, it was observed that some particles did not contain carbon black. The size was about 9 microns.

Comparative Example 6 Monomer Phase (O) Styrene: 15 parts by weight n-butyl acrylate: 15 parts by weight (Neospectra II manufactured by Columbian Carbon Co.) Untreated carbon black: 10 parts by weight Initiator: 1 part by weight 2, 2'-Azobis-isobutyronitrile aqueous dispersion medium phase (W) Ion-exchanged water: 150 parts by weight Hydroxypropyl cellulose: 3 parts by weight (Shin-Etsu Chemical Metroze 65SH50) Styrene, n-butyl acrylate and untreated carbon black After dispersing with a ball mill, an initiator is added to this to obtain a monomer phase, and the aqueous dispersion medium phase prepared by stirring with the monomer phase in advance is put in a stirring tank,
9500rp by homogenizer (made by Tokushu Kika Kogyo)
It was suspended for 10 minutes. After the suspension was purged with nitrogen, polymerization was carried out at 60 ° C. for 7 hours. The suspension droplet was observed with an optical microscope. After completion of the polymerization, purification was performed using a centrifuge, followed by filtration and drying under reduced pressure to obtain target particles. The obtained particles were observed with an optical microscope. The particle size was measured by a Coulter counter. As shown in Table 6 in this measurement result, it was observed that some particles did not contain carbon black. The size was about 9 microns.

The results of Comparative Examples 3 to 6 are shown in Table 6 below.

[Table 6] CB represents carbon black * 2: Some particles do not contain carbon black, and even particles containing carbon black have poor dispersibility.

Examples 29 to 40 The suspension-polymerized particles obtained in Examples 17 to 28 were treated with a commercially available charge control agent [Bontron E84 manufactured by Orient Co., Ltd.] by a spray dry method to develop an electrostatic image. When a toner for toner was obtained and an image was printed using the toner by an electrostatic copying machine [Riccopy FT6500 manufactured by Ricoh Co., Ltd.], it was possible to obtain a fine image with excellent fine line reproducibility and no bleeding or fog. It was

Comparative Examples 7 to 12 Images were formed using the suspension-polymerized particles obtained in Comparative Examples 1 to 6 in the same manner as in Examples 29 to 40. Only unclear images with low image density were obtained. I couldn't do it.

[0057]

【effect】

1. Claim 1 A treated carbon black pigment having improved dispersibility could be obtained. 2. Claims 2, 3 and 4 It is possible to obtain a treated carbon black pigment having further improved dispersibility. 3. Claims 5 and 6: The dispersibility of carbon black is very good, the size of the secondary aggregate of carbon black is 0.3 µm or less, and the secondary aggregate of carbon black per 1 µm ^{2 of the} toner cross section is smaller than that of the secondary aggregate. The number was 3 or more. Therefore, an image produced using the toner for developing an electrostatic charge image had a sufficient color density and was clear.

[Brief description of drawings]

FIG. 1 is a transmission electron micrograph of a cross-section sample produced by an ultrathin section method for particles produced in Example 17. Black dots indicate carbon black secondary aggregates.

Claims (6)

[Claims] 1. Obtained by subjecting a radical-polymerizable monomer to radical polymerization to obtain a polymer in a radical polymerization process, and subjecting the polymer and carbon black to a contact treatment before the growth radicals of the polymer are deactivated. Treated carbon black pigment. 2. The weight average molecular weight of the polymer to be contact-treated with carbon black is 500 to 100,000.
The treated carbon black pigment described. 3. The treated carbon black pigment according to claim 1, which is used after the surface activation treatment of carbon black. 4. The radical-polymerizable monomer contains at least one monomer selected from the group consisting of vinyl acetate, styrene and derivatives thereof, according to claim 1, 2 or 3. Treated carbon black pigment. 5. An electrostatic charge image developing toner obtained by dispersing the treated carbon black pigment according to claim 1, 2, 3 or 4 in a polymerizable monomer component and subjecting it to suspension polymerization or emulsion polymerization. 6. Toner particles having a cross-section of 1 μm ² have 3 or more secondary aggregates of the treated carbon black pigment dispersed therein, and the maximum diameter of the secondary aggregates of the treated carbon black pigment is 0.3 μm or less. The toner for developing an electrostatic charge image according to claim 5.