JP2009134061A - Toner manufacturing method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a toner manufacturing method for achieving (1) an oilless dry toner manufacturing method for obtaining satisfactory fluidity of toner (releasing property) and fixation performance at low temperatures, (2) a toner manufacturing method for obtaining high-grade quality of image having excellent minute dot reproducibility and (3) a toner manufacturing method for achieving (1) and (2) simultaneously. <P>SOLUTION: This manufacturing method for the toner produced by granulating base particles of the toner from an aqueous liquid medium prepared by emulsifying/dispersing an oil phase containing at least wax and a binding resin material comprises a wax dispersion liquid manufacturing process for forming a wax dispersion liquid prepared by dispersing wax into an organic solvent, an oil phase forming process for forming the oil phase containing a binding resin component and the wax by using the wax dispersion liquid, and an emulsifying and dispersing process for emulsifying and/or dispersing the oil phase into the aqueous medium to satisfy the following formulas: Dwax2 =(0.9 to 1.1)× Dwax1 (wherein, Dwax1 denotes average particle diameter of wax in the wax dispersion liquid, and Dwax2 denotes average particle diameter of wax dispersion domain in toner particle) and D95wax1≤1.8 × Dwax1 (wherein, D95wax1 denotes particle diameter being 95/100 when counting from below the distribution of particle diameters of wax in the wax dispersion liquid). <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a method for producing a toner used in a developer for developing an electrostatic charge image in electrophotography, electrostatic recording, electrostatic printing, and the like. More specifically, the present invention relates to a method for producing a toner for electrophotography used in a copying machine, a laser printer, a plain paper fax machine, and the like using a direct or indirect electrophotographic developing system.

  In recent years, the strong demand for higher image quality from the market has spurred the development of an electrophotographic apparatus suitable for it and a toner developer used therefor. As a toner corresponding to high image quality, it is essential that the toner has a uniform particle size. When the toner particle size is uniform and the particle size distribution becomes sharp, the behavior of individual toner particles during development is aligned, and the reproducibility of minute dots is remarkably improved.

  For the above purpose, a toner (hereinafter referred to as a chemical toner) obtained by a suspension polymerization method or an emulsion polymerization aggregation method obtained by granulating in an aqueous phase has been developed.

  In the suspension polymerization method, a monomer, a polymerization initiator, a colorant, a release agent, and the like are added to an aqueous phase containing a dispersion stabilizer while stirring to form oil droplets, and then the temperature is raised and a polymerization reaction In this method, toner particles are obtained. According to the suspension polymerization method, although it is possible to reduce the toner particle size, it is necessary to use a dispersion stabilizer that lowers the chargeability when it remains, and if no dispersion stabilizer is used, There is a problem that it is difficult for the release agent to easily enter the oil droplets at the time of formation, and to be appropriately present on the surface of the toner particles.

  Further, a release agent fine particle coated with or impregnated with a vinyl polymer by adding a polymerizable vinyl monomer and a water-soluble polymerization initiator to the release agent emulsion for polymerization is added at the time of emulsification of the toner composition. A method of uniformly and firmly adhering to the toner surface has been proposed (Patent Document 1). However, in this method, it is essential to polymerize the release agent emulsion and the polymerizable vinyl monomer, and since the glass transition temperature (Tg) of the resin constituting the release agent fine particles is high, There exists a problem that it is inferior to releasability, low temperature fixability, etc.

  Patent Document 2 discloses a wax having a low melting point that cannot be used in a pulverized toner by producing a toner by suspension polymerization of a polymerizable monomer system containing a substance having a polar group and a release agent in water. It is described that can be contained. Contrary to the polar component, the nonpolar component such as wax does not exist in the vicinity of the surface of the toner particles, and has a pseudo capsule structure covered with the polar component on the surface. However, the wax distribution inside the toner particles has not been analyzed and is unknown.

Patent Document 3 describes a toner in which wax is encapsulated in toner particles and localized on the particle surface. However, the detailed dispersion state of the wax near the toner surface is unknown.
Japanese Patent Application Laid-Open No. H10-228561 defines the ratio of the wax exposed on the toner surface measured by FTIR-ATR. However, toner blocking and hot offset properties, filming and paper wrapping are in a completely trade-off relationship, and it is difficult to further improve the fixability by simply improving the toner and simply controlling the average particle size of the wax. Is in the situation.

  Therefore, while maintaining the advantages of a chemical toner that has a small particle size and narrow particle size distribution and excellent fluidity, it has excellent releasability at low temperatures, less filming, low temperature fixability and heat resistant storage stability. However, there is a strong demand for a method that can stably and efficiently obtain a toner capable of obtaining a high-quality image at the same time, but this method has not yet been provided.

JP 2004-226669 A Japanese Patent No. 2666316 Japanese Patent Application Laid-Open No. 2002-6541 JP 2004-246345 A

The subject of this invention is as follows.
(1) Provided is a method for producing an oil-less dry toner that achieves both toner fluidity (releasing properties) and low-temperature fixability.
(2) To provide a toner manufacturing method capable of obtaining a high-quality image having excellent fine dot reproducibility.
(3) A toner manufacturing method capable of achieving the same problems (1) to (2) is provided.

The present inventors have completed the present invention to solve the above-described problems.
That is, according to the present invention, the following toner production method is provided.
(1) In a method for producing a toner obtained by granulating toner base particles from an aqueous liquid medium obtained by emulsifying / dispersing an oil phase containing at least a wax and a binder resin material,
A wax dispersion manufacturing process for forming a wax dispersion in which the wax is dispersed in an organic solvent, an oil phase forming process for forming an oil phase containing a binder resin component and a wax using the wax dispersion, and the oil phase An emulsifying and dispersing step of dispersing and / or emulsifying in an aqueous medium,
The wax average particle diameter Dwax1 in the wax dispersion and the average particle diameter Dwax2 of the wax dispersion domain in the toner particles are:
Dwax2 = 0.9 to 1.1 × Dwax1,
The particle size D95wax1 of 95/100 from the bottom of the wax particle size distribution in the wax dispersion is D95wax1 ≦ 1.8 × Dwax1
A method for producing a toner, wherein
(2) The method for producing a toner as described in (1) above, wherein the oil phase contains at least a wax, a binder resin component, and an organic solvent.
(3) The oil phase is formed by mixing at least an organic solvent and the wax to 50 ° C. or higher, and then mixing a wax dispersion obtained by lowering the temperature and other toner composition components. The method for producing a toner according to (1) or (2).
(4) The toner according to item (3), wherein the other toner composition component is mixed with the wax dispersion in the form of an organic solvent liquid containing the component to form the oil phase. Manufacturing method.
(5) The method for producing a toner according to any one of (1) to (4), wherein the wax dispersion contains a part of a binder resin component.
(6) In an oil phase obtained by dissolving at least the binder resin component and a binder resin precursor composed of a modified polyester resin in an organic solvent and dispersing the wax, the binder resin precursor and After the compound that elongates or crosslinks is dissolved, the oil phase is dispersed in the form of droplets in an aqueous medium containing a fine particle dispersant to obtain an emulsified dispersion, and the binder resin precursor in the emulsified dispersion. The method for producing a toner according to any one of (1) to (5) above, further comprising a step of removing the organic solvent by crosslinking reaction and / or elongation reaction.
(7) Items (1) to (1) above, wherein the oil phase is obtained by dissolving or dispersing a layered inorganic mineral obtained by modifying at least part of ions between layers of the layered inorganic mineral with organic ions. The method for producing a toner according to any one of Items (6).
(8) The method for producing a toner according to any one of (1) to (7), wherein the binder resin is a polyester resin.
(9) The method for producing a toner according to any one of (1) to (8), wherein the content of the polyester resin in the binder resin is 50 to 100% by weight.
(10) The toner according to any one of (1) to (9) above, wherein the polyester resin has a THF-soluble component having a weight average molecular weight of 1,000 to 30,000. Production method.
(11) The acid value of the acidic group-containing polyester resin is 1.0 to 50.0 (KOHmg / g), any one of (1) to (10) above Toner manufacturing method.
(12) The toner production method as described in any one of (1) to (11) above, wherein the acidic group-containing polyester resin has a glass transition point of 35 to 65 ° C.
(13) The polymer according to any one of (1) to (12), wherein the polymer having a site capable of reacting with the compound having an active hydrogen group has a weight average molecular weight of 3,000 to 20,000. Toner production method.
(14) The toner production method as described in any one of (1) to (13) above, wherein the toner has an acid value of 0.5 to 40.0 (KOHmg / g). .
(15) The toner production method as described in any one of (1) to (14) above, wherein the toner has a glass transition point of 40 to 70 ° C.
(16) The toner according to any one of (1) to (15) above, wherein the volume average particle diameter Dv / number average particle diameter Dn of the toner is 1.30 or less. Method.
(1) The method for producing a toner according to any one of (1) to (16), wherein the number of particles of 2 μm or less of the toner is 20% by number or less.

  As is clear from the following detailed and specific description, the dry toner production method of the present invention can obtain a sharp particle size distribution in water-based granulation, and has excellent low-temperature fixability and high image quality. This provides an extremely excellent effect of providing a toner that provides an image with a high resolution.

The present invention has the following features.
(Wax dispersion)
In the present invention, it is necessary that a particle size D95wax1 of 95/100 from the bottom of the wax particle size distribution in the wax dispersion is D95wax1 ≦ 1.8 × wax average particle size Dwax1. When D95wax1 is larger than 1.8 × Dwax1, that is, when the wax particle size distribution in the wax dispersion is wide and there are many coarse wax particles, a sharp toner having a uniform particle size distribution in aqueous granulation I can't get the particles. Further, it is impossible to obtain a toner excellent in releasability and lubricity. Therefore, a good image cannot be obtained. Therefore, it is important to obtain a relatively sharp wax dispersion such as D95wax1 ≦ 1.8 × Dwax1.
In addition, in order to obtain a wax dispersion having a sharp particle size distribution in an organic solvent, the organic solvent and the wax are heated to 50 ° C. or higher, and then the temperature is lowered to create a uniform and small particle size. It is preferable in that a simple wax is obtained.

  The particle diameter of the wax in the present invention is preferably from μm to μm. If the particle size is less than this, it may be difficult to achieve the desired releasability and lubricity. If the particle size exceeds this range, sharp toner particles having a uniform particle size distribution are obtained. May not be able to get.

  In preparing the wax dispersion in the present invention, it is desirable to stir the dispersion when the temperature of the organic solvent and the wax is raised to 50 ° C. or higher, and the stirring condition at the time of the temperature drop is also particularly preferable. Therefore, it is preferable to keep stirring sufficiently strong (more than the rotational speed RPM of the stirring impeller).

  The amount of wax (weight) depends on the type of organic solvent used to prepare the wax dispersion and the amount of other toner material component liquids used when mixing with the wax dispersion to form the oil phase. The amount is preferably about twice to twice the amount. If it is less than this, it is difficult to easily reduce the particle size of the wax and achieve a narrow particle size distribution range, and the use of a large amount of organic solvent exceeding this upper limit results in a decrease in the amount of recovered wax and the solvent recovery cost, etc. It is not economical from the point of view.

  In the preparation of the wax dispersion according to the present invention, it is usually not necessary to add a surfactant or the like. (Of course, use of no surfactant is not an indispensable matter in the present invention). Also, when preparing the binder resin component liquid, it is usually not necessary to add a dispersant such as a surfactant. Therefore, normally, the oil phase containing the wax dispersion and the binder resin component is substantially free of surfactant derived therefrom. A surfactant may be contained in the aqueous medium in which the oil phase is emulsified and dispersed, but this surfactant is removed along with the aqueous medium to be removed by washing and filtering after toner base particle granulation. Therefore, the obtained dry toner contains substantially no surfactant that adversely affects the charging characteristics.

  In the present invention, the organic solvent for preparing the wax dispersion is preferably an organic solvent that does not dissolve the wax when the temperature is lowered to room temperature and can disperse the wax in a uniform particle size in the above range. The liquid containing the other toner material and forming the oil phase preferably has the toner material dissolved or dispersed in a solvent. The solvent preferably contains an organic solvent. This organic solvent is preferably miscible with the organic solvent for preparing the wax dispersion, and both can be the same solvent. These organic solvents are preferably removed when the toner base particles are formed or after the toner base particles are formed.

  Both of these organic solvents, that is, the organic solvent for preparing the wax dispersion and the organic solvent for the oil phase can be appropriately selected according to the purpose, but since the removal is easy, the boiling point is 150 ° C. It is preferable that it is less than. Specifically, such as toluene, xylene, benzene, carbon tetrachloride, methylene chloride, 1,2-dichloroethane, 1,1,2-trichloroethane, trichloroethylene, chloroform, monochlorobenzene, dichloroethylidene, methyl acetate, ethyl acetate In addition to water-immiscible solvents, water-miscible solvents such as methyl ethyl ketone and methyl isobutyl ketone are exemplified. Of these, toluene, xylene, benzene, methylene chloride, 1,2-dichloroethane, chloroform, carbon tetrachloride and the like are preferable, and ethyl acetate is particularly preferable. These may be used alone or in combination of two or more.

  The amount of these organic solvents used can be appropriately selected according to the purpose, but is preferably 40 to 300 parts by weight, more preferably 60 to 140 parts by weight, based on 100 parts by weight of the toner material. More preferred is ~ 120 parts by weight.

  The toner material in the present invention contains other desired components such as a modified layered inorganic mineral in addition to a binder resin, a release agent (wax), and a colorant. Those other than the layered inorganic mineral obtained by modifying at least a part of the metal cations of the modified layered inorganic mineral with an organic cation can be appropriately selected according to the purpose. Any of a polymer, a compound having an active hydrogen group, and a polymer having reactivity to the active hydrogen group may be contained.

(Layered inorganic mineral)
The modified layered inorganic mineral is preferably one having a smectite basic crystal structure modified with an organic cation. Moreover, a metal anion can be introduce | transduced by substituting a part of bivalent metal of a layered inorganic mineral for a trivalent metal. However, since a hydrophilic property is high when a metal anion is introduced, a layered inorganic compound in which at least a part of the metal anion is modified with an organic anion is desirable.
Examples of the organic ion modifier of the layered inorganic mineral obtained by modifying at least part of the ions of the layered inorganic mineral with organic ions include quaternary alkyl ammonium salts, phosphonium salts and imidazolium salts. A quaternary alkyl ammonium salt is desirable. Examples of the quaternary alkylammonium include trimethylstearylammonium, dimethylstearylbenzylammonium, dimethyloctadecylammonium, oleylbis (2-hydroxyethyl) methylammonium and the like.

  Examples of the organic ion modifier include branched, unbranched or cyclic alkyl (C1-C44), alkenyl (C1-C22), alkoxy (C8-C32), hydroxyalkyl (C2-C22), ethylene oxide, propylene oxide, and the like. Examples include sulfates, sulfonates, carboxylates, or phosphates. A carboxylic acid having an ethylene oxide skeleton is desirable.

By modifying at least part of the layered inorganic mineral with organic ions, it has moderate hydrophobicity, the oil phase containing the toner composition and / or toner composition precursor has non-Nutnian viscosity, and the toner is deformed (The spherical oil phase dispersed in the aqueous medium can be made non-spherical rather than crosslinked and solidified while maintaining its shape). At this time, the content of the layered inorganic mineral obtained by modifying a part of the toner material with organic ions is preferably 0.05 to 2% by weight.
The layered inorganic mineral partially modified with organic ions can be appropriately selected, and examples thereof include montmorillonite, bentonite, hectorite, attapulgite, sepiolite, and mixtures thereof. Among these, organically modified montmorillonite or bentonite is preferable because the viscosity can be easily adjusted without affecting the toner characteristics and the addition amount can be reduced.

Commercially available layered inorganic minerals partially modified with an organic cation include Bentone 3, Bentone 38, Bentone 38V (above, manufactured by Leox), Thixogel VP (manufactured by United catalyst), Kraton 34, Kraton 40, Kraton XL Quartium 18 bentonite such as (made by Southern Clay), and stearalkonium bentonite such as Bentone 27 (made by Leox), Thixogel LG (made by United catalyst), Clayton AF, Clayton APA (made by Southern Clay) Quaternium 18 / benzalkonium bentonite such as Clayton HT and Clayton PS (manufactured by Southern Clay). Particularly preferred are Clayton AF and Clayton APA. Moreover, as a layered inorganic mineral partially modified with an organic anion, a material obtained by modifying DHT-4A (manufactured by Kyowa Chemical Industry Co., Ltd.) with an organic anion represented by the following general formula (1) is particularly preferable. The following general formula (1) includes, for example, Hytenol 330T (Daiichi Kogyo Seiyaku Co., Ltd.).
Formula (1) R ₁ (OR ₂ ) _n OSO ₃ M
[Wherein, R ₁ represents an alkyl group having 13 carbon atoms, and R ₂ represents an alkylene group having 2 to 6 carbon atoms. n represents an integer of 2 to 10, and M represents a monovalent metal element]
By using a modified layered inorganic mineral, it has moderate hydrophobicity, and therefore tends to be present at the interface of the droplets, so that the surface is unevenly distributed and can exhibit charging properties.

  In the toner of the present invention, the ratio (Dv / Dn) of the volume average particle diameter (Dv) to the number average particle diameter (Dn) is 1.00 to 1.30, which is high resolution and high image quality. It is possible to obtain the toner. Furthermore, in the case of a two-component developer, even if a long-term balance of the toner is performed, fluctuations in the particle size of the toner in the developer are reduced, and good and stable developability even with long-term stirring in the developing device. Is possible. If Dv / Dn exceeds 1.30, the variation in particle size of individual toner particles is large, and the behavior of the toner varies during development and the like, and the reproducibility of minute dots is impaired. Therefore, a high-quality image cannot be obtained. More preferably, Dv / Dn is in the range of 1.00 to 1.20, and a better image can be obtained.

  In the toner of the present invention, the volume average particle diameter Dv is preferably 3.0 to 7.0 μm. In general, it is said that the smaller the particle size of the toner, the more advantageous it is to obtain a high-resolution and high-quality image, but it is disadvantageous for transferability and cleaning properties. is there. When the volume average particle diameter is smaller than the above range, in the case of a two-component developer, the toner is fused to the surface of the carrier during a long period of stirring in the developing device, and the charging ability of the carrier is reduced. When it is used, toner filming on the developing roller and toner fusion to a member such as a blade for thinning the toner are likely to occur. In addition, these phenomena are greatly related to the content of fine powder. In particular, when the particle size of 2 μm or less exceeds 20%, it becomes an obstacle to the adhesion to the carrier and the high level of charging stability. Conversely, when the toner particle size is larger than the above range, it becomes difficult to obtain a high-resolution and high-quality image, and the toner particle size when the balance of the toner in the developer is performed. In many cases, fluctuations of It was also clarified that the same applies when the volume average particle diameter / number average particle diameter is larger than 1.30.

  The relationship between toner shape and transferability will be described. When using a full-color copier that transfers images with multi-color development, the amount of toner on the photoconductor increases compared to the case of one-color black toner used in black-and-white copiers. It is difficult to improve transfer efficiency. In addition, when ordinary irregular toner is used, a shearing force or friction between the photosensitive member and the cleaning member, between the intermediate transfer member and the cleaning member, and / or between the photosensitive member and the intermediate transfer member. Due to the force, toner fusing or filming occurs on the surface of the photoreceptor or the intermediate transfer member, and transfer efficiency tends to deteriorate. When generating a full-color image, it is difficult to transfer the four-color toner images uniformly. Furthermore, when an intermediate transfer member is used, problems are likely to occur in terms of color unevenness and color balance, and high-quality full-color images are stabilized. Output is not easy.

  From the viewpoint of a balance between blade cleaning and transfer efficiency, particles having a toner circularity of 0.950 or less are 20 to 80% of the total toner particles, thereby achieving both cleaning and transferability. Cleaning and transferability are greatly related to the material of the blade and how to apply the blade, and transfer also varies depending on the process conditions, so that the design according to the process can be performed within the above range. However, if the toner circularity is 0.950 or less than 20% of all toner particles, cleaning with a blade becomes difficult. On the other hand, when the particles having a circularity of 0.950 or less exceed 80% of the total toner particles, the above-described transferability is deteriorated. This phenomenon is caused by excessively deformed toner shape, so that toner movement during transfer (photosensitive member surface to transfer paper, photosensitive member surface to intermediate transfer belt, first intermediate transfer belt to second intermediate transfer belt) , Etc.) are not smooth, and the toner particles vary in behavior, so that uniform and high transfer efficiency cannot be obtained. In addition, unstable charging and brittleness of particles begin to appear. Furthermore, it becomes a fine phenomenon in the developer, which causes a decrease in the durability of the developer. For this reason, it is preferable that the toner has a circularity of 0.950 or less of 20 to 80% of the total toner particles.

(2 μm or less grain size, circularity)
The particle ratio of 2 μm or less, the circularity, and the average circularity of the toner of the present invention can be measured by a flow type particle image analyzer FPIA-2100 (manufactured by Toa Medical Electronics Co., Ltd.).
As a specific measuring method, 0.1 to 0.5 ml of a surfactant, preferably alkylbenzene sulfonate is added as a dispersant to 100 to 150 ml of water from which impure solids have been removed in advance, and further measurement is performed. Add about 0.1-0.5g of sample. The suspension in which the sample is dispersed is obtained by performing dispersion treatment with an ultrasonic disperser for about 1 to 3 minutes, and measuring the shape and distribution of the toner with the above apparatus at a dispersion concentration of 3000 to 10,000 / μl. .

(Toner particle size)
The average particle size and particle size distribution of the toner are determined by the Carcoulter counter method. Examples of the measuring device for the particle size distribution of the toner particles include Coulter Counter TA-II and Coulter Multisizer II (both manufactured by Coulter). In the present invention, measurement was performed using a Coulter Counter TA-II type connected to an interface (Nichiken Giken) that outputs number distribution and volume distribution and a PC9801 personal computer (manufactured by NEC).

The measurement method is described below.
First, 0.1 to 5 ml of a surfactant (preferably alkylbenzene sulfonate) is added as a dispersant to 100 to 150 ml of an aqueous electrolytic solution. Here, the electrolytic solution is a solution prepared by preparing a 1% NaCl aqueous solution using primary sodium chloride. For example, ISOTON-II (manufactured by Coulter) can be used. Here, 2 to 20 mg of a measurement sample is further added. The electrolytic solution in which the sample is suspended is subjected to a dispersion treatment with an ultrasonic disperser for about 1 to 3 minutes. Volume distribution and number distribution are calculated.
As channels, 2.00 to less than 2.52 μm; 2.52 to less than 3.17 μm; 3.17 to less than 4.00 μm; 4.00 to less than 5.04 μm; 5.04 to less than 6.35 μm; 6 Less than 35 to 8.00 μm; less than 8.00 to less than 10.08 μm; less than 10.08 to less than 12.70 μm; less than 12.70 to less than 16.00 μm; less than 16.00 to less than 20.20 μm; Uses 13 channels less than 40 μm; 25.40 to less than 32.00 μm; 32.00 to less than 40.30 μm, and targets particles having a particle size of 2.00 μm to less than 40.30 μm. The volume-based volume average particle diameter (Dv) obtained from the volume distribution according to the present invention and the number average particle diameter (Dn) obtained from the number distribution and the ratio Dv / Dn were obtained.

  According to a further study of the present invention, the acidic group-containing polyester resin is used to effectively exhibit low-temperature fixability while maintaining heat-resistant storage stability and to impart offset resistance after modification with a prepolymer. It is preferable that the weight-average molecular weight of the THF-soluble component is 1,000 to 30,000. This is because when the amount is less than 1,000, the oligomer component increases, the heat-resistant storage stability is deteriorated, and when it exceeds 30,000, the modification with the prepolymer is insufficient due to steric hindrance and the offset resistance is deteriorated.

The molecular weight according to the present invention is measured by GPC (gel permeation chromatography) as follows. Stabilize the column in a heat chamber at 40 ° C., flow THF at a flow rate of 1 ml / min through the column at this temperature, and prepare a THF sample solution of resin prepared at a sample concentration of 0.05 to 0.6% by weight. Is measured by injecting 50 to 200 μl. In measuring the molecular weight of the sample, the molecular weight distribution of the sample was calculated from the relationship between the logarithmic value of the prepared calibration curve and the count using several types of monodisperse polystyrene standard samples. As a standard polystyrene sample for preparing a calibration curve, for example, Pressure Chemical Co. Alternatively, the molecular weights of Toyo Soda Kogyo Co., Ltd. are 6 × 10 ² , 2.1 × 10 ³ , 4 × 10 ³ , 1.75 × 10 ⁴ , 5.1 × 10 ⁴ , 1.1 × 10 ⁵ , 3.9. It is appropriate to use x10 ⁵ , 8.6 × 10 ⁵ , 2 × 10 ⁶ , 4.48 × 10 ⁶ , and use at least about 10 standard polystyrene samples. An RI (refractive index) detector is used as the detector.

  In addition, by adjusting the acid value of the acidic group-containing polyester resin to 1.0 to 50.0 (KOHmg / g), particle size control by adding a base compound, low-temperature fixability, high-temperature offset resistance, heat-resistant storage stability, It is possible to improve toner characteristics such as charging stability. That is, when the acid value exceeds 50.0 (KOHmg / g), the extension or crosslinking reaction of the modified polyester becomes insufficient, and the high-temperature offset resistance is affected, and when it is less than 1.0 (KOHmg / g) This is because a dispersion stabilizing effect due to the base compound during production cannot be obtained, and the elongation or cross-linking reaction of the modified polyester tends to proceed, resulting in a problem in production stability.

The method for measuring the acid value of the polyester resin of the present invention is based on a method based on JIS K0070. However, when the sample does not dissolve, a solvent such as dioxane or THF is used as the solvent.
The acid value is specifically determined by the following procedure.
Measuring device: Potentiometric automatic titrator DL-53 Titrator (Metler Toledo)
Electrode used: DG113-SC (Metler Toledo)
Analysis software: LabX Light Version 1.00.000
Calibration of the apparatus: Use a mixed solvent of 120 ml of toluene and 30 ml of ethanol.
Measurement temperature: 23 ° C
The measurement conditions are as follows.
Stir
Speed [%] 25
Time [s] 15
EQP titration
Titrant / Sensor
Titrant CH3ONa
Concentration [mol / L] 0.1
Sensor DG115
Unit of measurement mV
Predispensing to volume
Volume [mL] 1.0
Wait time [s] 0
Titrant addition Dynamic
dE (set) [mV] 8.0
dV (min) [mL] 0.03
dV (max) [mL] 0.5
Measure mode Equilibrium controlled
dE [mV] 0.5
dt [s] 1.0
t (min) [s] 2.0
t (max) [s] 20.0
Recognition
Threshold 100.0
Steepest jump only No
Range No
Tendency None
Termination
at maximum volume [mL] 10.0
at potential No
at slope No
after number EQPs Yes
n = 1
comb. termination conditions No
Evaluation
Procedure Standard
Potential 1 No
Potential 2 No
Stop for reevaluation No

(Measurement method of acid value)
Measurement is performed under the following conditions in accordance with the measurement method described in JIS K0070-1992.
Sample preparation: 0.5 g of polyester (0.3 g for ethyl acetate-soluble component) is added to 120 ml of toluene and dissolved by stirring at room temperature (23 ° C.) for about 10 hours. Further, 30 ml of ethanol is added to prepare a sample solution.
The measurement can be calculated by the apparatus described above, but specifically, the calculation is performed as follows.
Titrate with a pre-standardized N / 10 caustic potash to alcohol solution, and obtain the acid value from the consumption of the alcohol potash solution by the following calculation.
Acid value = KOH (ml) x N x 56.1 / sample weight (where N is a factor of N / 10 KOH)

  In the present invention, the heat-resistant storage performance of the main component of the polyester resin after modification, that is, the binder resin depends on the glass transition point of the polyester resin before modification, so the glass transition point of the polyester resin is designed at 35 to 65 ° C. It is preferable to do. That is, if it is less than 35 ° C., the heat-resistant storage stability is insufficient, and if it exceeds 65 ° C., it adversely affects low-temperature fixing.

The glass transition point of the present invention is measured with a Rigaku THRMOFLEX TG8110 manufactured by Rigaku Corporation at a temperature increase rate of 10 ° C./min.
A method for measuring Tg will be outlined. As an apparatus for measuring Tg, a TG-DSC system TAS-100 manufactured by Rigaku Corporation was used.
First, about 10 mg of a sample is placed in an aluminum sample container, which is placed on a holder unit and set in an electric furnace. First, after heating from room temperature to 150 ° C. at a temperature rising rate of 10 ° C./min, the sample was allowed to stand at 150 ° C. for 10 minutes, the sample was cooled to room temperature and left for 10 minutes, and the temperature rising rate was again increased to 150 ° C. under a nitrogen atmosphere. DSC measurement was performed by heating at min. Tg was calculated from the tangent of the endothermic curve near the Tg and the base line using the analysis system in the TAS-100 system.

  According to a further study of the present invention, the prepolymer for modifying the polyester resin is an important binder resin component for realizing low-temperature fixability and high-temperature offset resistance, and its weight average molecular weight is 3,000 to 20, 000 is preferred. That is, when the weight average molecular weight is less than 3,000, it becomes difficult to control the reaction rate, and problems in production stability begin to occur. On the other hand, when the weight average molecular weight exceeds 20,000, sufficient modified polyester cannot be obtained and the offset resistance starts to be affected.

  Further examination of the present invention revealed that the toner acid value is a more important index than the binder resin acid value for low-temperature fixability and high-temperature offset resistance. The toner acid value of the present invention is derived from the terminal carboxyl group of the unmodified polyester. The unmodified polyester preferably has an acid value of 0.5 to 40.0 (KOHmg / g) in order to control low-temperature fixability (fixing lower limit temperature, hot offset occurrence temperature, etc.) as a toner. In other words, when the toner acid value exceeds 40.0 (KOHmg / g), the modified polyester is insufficiently stretched or cross-linked, affecting high-temperature offset resistance, and less than 0.5 (KOHmg / g). In this case, the dispersion stabilizing effect due to the base compound at the time of production cannot be obtained, and the extension or crosslinking reaction of the modified polyester tends to proceed, resulting in a problem in production stability. The toner acid value is measured by a method based on JIS K0070.

  The glass transition point of the toner of the present invention is preferably 40 to 70 ° C. in order to obtain low temperature fixability, heat resistant storage stability and high durability. That is, when the glass transition point is less than 40 ° C., blocking in the developing machine and filming to the photoreceptor are liable to occur, and when it exceeds 70 ° C., the low-temperature fixability tends to deteriorate.

  The toner of the present invention is a solution or dispersion formed by dissolving or dispersing a toner component consisting of a binder component consisting of a modified polyester resin capable of reacting at least with active hydrogen and a colorant in an organic solvent. It is obtained by reacting with a cross-linking agent and / or an extender in a hydrogen medium, and removing the solvent from the resulting dispersion.

Examples of the reactive modified polyester resin (RMPE) capable of reacting with active hydrogen used in the present invention include a polyester prepolymer (A) having an isocyanate group. Examples of the prepolymer (A) include a polycondensate of a polyol (PO) and a polycarboxylic acid (PC) and a polyester having active hydrogen further reacted with a polyisocyanate (PIC). Examples of the group containing active hydrogen in the polyester include a hydroxyl group (alcoholic hydroxyl group and phenolic hydroxyl group), an amino group, a carboxyl group, a mercapto group, and the like. Among these, an alcoholic hydroxyl group is preferable.
An amine is used as a crosslinking agent for the reactive modified polyester resin, and a diisocyanate compound (diphenylmethane diisocyanate or the like) is used as an extender. The amines described in detail later act as a crosslinking agent and an extender for the modified polyester capable of reacting with active hydrogen.

  Modified polyester such as urea-modified polyester obtained by reacting the polyester prepolymer (A) having an isocyanate group with an amine (B) can easily adjust the molecular weight of the polymer component, and is a dry toner, particularly oilless low-temperature fixing. It is convenient to ensure the characteristics (wide releasability and fixability without a release oil application mechanism to the fixing heating medium). Particularly, a polyester prepolymer whose end is modified with urea can suppress adhesion to a heating medium for fixing while maintaining high fluidity and transparency in the fixing temperature range of the unmodified polyester resin itself.

  A preferred polyester prepolymer used in the present invention is a polyester having an active hydrogen group such as an acid group or a hydroxyl group at the terminal, and a functional group such as an isocyanate group that reacts with the active hydrogen. A modified polyester (MPE) such as urea-modified polyester can be derived from this prepolymer, but in the case of the present invention, a preferred modified polyester used as a toner binder is a polyester prepolymer (A) having an isocyanate group. It is a urea-modified polyester obtained by reacting amines (B) as a crosslinking agent and / or an extender. The polyester prepolymer (A) having an isocyanate group is obtained by further reacting a polyester having an active hydrogen group, which is a polycondensate of a polyol (PO) and a polycarboxylic acid (PC), with a polyisocyanate (PIC). Can do. Examples of the active hydrogen group possessed by the polyester include hydroxyl groups (alcoholic hydroxyl groups and phenolic hydroxyl groups), amino groups, carboxyl groups, mercapto groups, and the like. Among these, alcoholic hydroxyl groups are preferred.

  Examples of the polyol (PO) include a diol (DIO) and a trivalent or higher polyol (TO), and (DIO) alone or a mixture of (DIO) and a small amount of (TO) is preferable. Diol (DIO) includes alkylene glycol (ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,4-butanediol, 1,6-hexanediol, etc.); alkylene ether glycol (diethylene glycol, triethylene glycol, Ethylene glycol, dipropylene glycol, polyethylene glycol, polypropylene glycol, polytetramethylene ether glycol, etc.); alicyclic diols (1,4-cyclohexanedimethanol, hydrogenated bisphenol A, etc.); bisphenols (bisphenol A, bisphenol F, Bisphenol S, etc.); alkylene oxide (ethylene oxide, propylene oxide, butylene oxide, etc.) adduct of the above alicyclic diol; Alkylene oxide phenol compound (ethylene oxide, propylene oxide, butylene oxide, etc.), etc. adducts. Among them, preferred are alkylene glycols having 2 to 12 carbon atoms and alkylene oxide adducts of bisphenols, and particularly preferred are alkylene oxide adducts of bisphenols and alkylene glycols having 2 to 12 carbon atoms. It is a combined use. Examples of the trivalent or higher polyol (TO) include 3 to 8 or higher polyhydric aliphatic alcohols (glycerin, trimethylolethane, trimethylolpropane, pentaerythritol, sorbitol, etc.); trivalent or higher phenols (Tris) Phenol PA, phenol novolak, cresol novolak, etc.); alkylene oxide adducts of the above trivalent or more polyphenols.

  Examples of the polycarboxylic acid (PC) include dicarboxylic acid (DIC) and trivalent or higher polycarboxylic acid (TC), and DIC alone or a mixture of DIC and a small amount of (TC) is preferable. Dicarboxylic acids (DIC) include alkylene dicarboxylic acids (succinic acid, adipic acid, sebacic acid, etc.); alkenylene dicarboxylic acids (maleic acid, fumaric acid, etc.); aromatic dicarboxylic acids (phthalic acid, isophthalic acid, terephthalic acid, naphthalene) Dicarboxylic acid and the like). Of these, preferred are alkenylene dicarboxylic acids having 4 to 20 carbon atoms and aromatic dicarboxylic acids having 8 to 20 carbon atoms. Examples of the trivalent or higher polycarboxylic acid (TC) include aromatic polycarboxylic acids having 9 to 20 carbon atoms (such as trimellitic acid and pyromellitic acid). In addition, as polycarboxylic acid (PC), you may make it react with a polyol (PO) using the above-mentioned acid anhydride or lower alkyl ester (Methyl ester, ethyl ester, isopropyl ester, etc.). The ratio of the polyol (PO) and the polycarboxylic acid (PC) is usually 2/1 to 1/1, preferably 1 as the equivalent ratio [OH] / [COOH] of the hydroxyl group [OH] and the carboxyl group [COOH]. 5/1 to 1/1, more preferably 1.3 / 1 to 1.02 / 1.

  As polyisocyanate (PIC), aliphatic polyisocyanate (tetramethylene diisocyanate, hexamethylene diisocyanate, 2,6-diisocyanatomethylcaproate, etc.); alicyclic polyisocyanate (isophorone diisocyanate, cyclohexylmethane diisocyanate, etc.); aromatic Diisocyanates (tolylene diisocyanate, diphenylmethane diisocyanate, etc.); araliphatic diisocyanates (α, α, α ′, α′-tetramethylxylylene diisocyanate, etc.); isocyanurates; And a combination of two or more of these.

  The ratio of the polyisocyanate (PIC) is usually 5/1 to 1/1, preferably 4 /, as an equivalent ratio [NCO] / [OH] of the isocyanate group [NCO] and the hydroxyl group [OH] of the polyester having a hydroxyl group. 1 to 1.2 / 1, more preferably 2.5 / 1 to 1.5 / 1. When [NCO] / [OH] exceeds 5, low-temperature fixability deteriorates. When the molar ratio of [NCO] is less than 1, when a modified polyester is used, the urea content in the ester becomes low and the hot offset resistance deteriorates. The content of the polyisocyanate (3) component in the prepolymer (A) having an isocyanate group at the terminal is usually 0.5 to 40% by weight, preferably 1 to 30% by weight, more preferably 2 to 20% by weight. It is. If it is less than 0.5% by weight, the hot offset resistance deteriorates, and it is disadvantageous in terms of both heat-resistant storage stability and low-temperature fixability. On the other hand, if it exceeds 40% by weight, the low-temperature fixability deteriorates.

  The number of isocyanate groups contained per molecule in the prepolymer (A) having an isocyanate group is usually 1 or more, preferably 1.5 to 3 on average, more preferably 1.8 to 2.5 on average. It is. If it is less than 1 per molecule, the molecular weight of the urea-modified polyester will be low, and the hot offset resistance will deteriorate.

As amines (B), diamine (B1), trivalent or higher polyamine (B2), aminoalcohol (B3), aminomercaptan (B4), amino acid (B5), and amino acids B1-B5 blocked (B6). Examples of the diamine (B1) include aromatic diamines (phenylenediamine, diethyltoluenediamine, 4,4′diaminodiphenylmethane, etc.); alicyclic diamines (4,4′-diamino-3,3′dimethyldicyclohexylmethane, diaminecyclohexane, Isophorone diamine etc.); and aliphatic diamines (ethylene diamine, tetramethylene diamine, hexamethylene diamine etc.) and the like. Examples of the trivalent or higher polyamine (B2) include diethylenetriamine and triethylenetetramine. Examples of amino alcohol (B3) include ethanolamine and hydroxyethylaniline. Examples of amino mercaptan (B4) include aminoethyl mercaptan and aminopropyl mercaptan. Examples of the amino acid (B5) include aminopropionic acid and aminocaproic acid.
As (B6) which blocked the amino group of (B1) to (B5), ketimine compounds obtained from the amines and ketones (acetone, methyl ethyl ketone, methyl isobutyl ketone, etc.) of (B1) to (B5), And oxazolidine compounds. Among these amines (B), preferred are (B1) and a mixture of (B1) and a small amount of (B2).

  Furthermore, if necessary, the molecular weight of the polyester can be adjusted using an elongation terminator. Examples of the elongation terminator include monoamines (diethylamine, dibutylamine, butylamine, laurylamine, etc.), and those obtained by blocking them (ketimine compounds).

  The ratio of amines (B) is the equivalent ratio [NCO] / [NHx] of isocyanate groups [NCO] in the prepolymer (A) having isocyanate groups and amino groups [NHx] in amines (B). The ratio is usually 1/2 to 2/1, preferably 1.5 / 1 to 1 / 1.5, more preferably 1.2 / 1 to 1 / 1.2. When [NCO] / [NHx] is more than 2 or less than 1/2, the molecular weight of the polyester is lowered and the hot offset resistance is deteriorated.

  In the present invention, the polyester resin (polyester) that is preferably used as a toner binder includes urea-modified polyester (UMPE), and the polyester may contain a urethane bond as well as a urea bond. The molar ratio of the urea bond content to the urethane bond content is usually 100/0 to 10/90, preferably 80/20 to 20/80, and more preferably 60/40 to 30/70. When the molar ratio of the urea bond is less than 10%, the hot offset resistance is deteriorated.

  Modified polyester such as urea-modified polyester (UMPE) is produced by a one-shot method or the like. The weight average molecular weight of the modified polyester such as urea-modified polyester (UMPE) is usually 10,000 or more, preferably 20,000 to 10,000,000, more preferably 30,000 to 1,000,000. If it is less than 10,000, the hot offset resistance deteriorates. The number average molecular weight of a modified polyester such as a urea-modified polyester is not particularly limited when a non-modified polyester (PE) described later is used, and may be a number average molecular weight that can be easily obtained to obtain the weight average molecular weight. In the case of a modified polyester such as UMPE alone, the number average molecular weight is usually 2000-15000, preferably 2000-10000, and more preferably 2000-8000. When it exceeds 20000, the low-temperature fixability and the glossiness when used in a full-color apparatus are deteriorated.

In the present invention, a modified polyester such as polyester modified with a urea bond (UMPE) is not only used alone, but also with this, unmodified polyester (PE) can be contained as a toner binder component. The combined use of PE improves low-temperature fixability and gloss when used in a full-color device, and is preferable to single use.
Examples of PE include polycondensates of polyol PO and polycarboxylic acid PC similar to the polyester component of UMPE, and preferred ones are also the same as in UMPE. The weight average molecular weight (Mw) of PE is 10,000 to 300,000, preferably 14,000 to 200,000. Its Mn (number average molecular weight) is 1000 to 10000, preferably 1500 to 6000. For UMPE, not only unmodified polyesters but also those modified with chemical bonds other than urea bonds, such as those modified with urethane bonds, can be used in combination. UMPE and PE are preferably at least partially compatible with each other in terms of low-temperature fixability and hot offset resistance. Accordingly, the polyester component of UMPE and PE preferably have similar compositions. The weight ratio of UMPE to PE when PE is contained is usually 5/95 to 80/20, preferably 5/95 to 30/70, more preferably 5/95 to 25/75, particularly preferably 7/93. ~ 20/80. When the weight ratio of UMPE is less than 5%, the hot offset resistance is deteriorated, and it is disadvantageous in terms of both heat-resistant storage stability and low-temperature fixability.

  The hydroxyl value (mgKOH / g) of PE is preferably 5 or more, and the acid value (mgKOH / g) of PE is usually 1 to 30, preferably 5 to 20. By giving an acid value, it tends to be negatively charged, and further, the affinity between the paper and the toner is good when fixing to paper, and the low-temperature fixability is improved. However, when the acid value exceeds 30, there is a tendency to deteriorate with respect to the stability of charging, particularly the environmental fluctuation. In the polymerization reaction, if the acid value is touched, it will cause blurring in the granulation process, making it difficult to control the emulsification.

(Measurement method of hydroxyl value)
Weigh accurately 0.5 g of sample into a 100 ml volumetric flask and add 5 ml of acetylating reagent correctly. Then, it is immersed in a bath at 100 ° C. ± 5 ° C. and heated. After 1-2 hours, the flask is removed from the bath, allowed to cool, water is added and shaken to decompose acetic anhydride. Furthermore, in order to complete the decomposition, the flask is again heated in a bath for 10 minutes or more and allowed to cool, and then the wall of the flask is thoroughly washed with an organic solvent. This solution is subjected to potentiometric titration with an N / 2 potassium hydroxide ethyl alcohol solution using the electrode to determine the OH value (according to JISK0070-1966).

  In the present invention, the glass transition point (Tg) of the toner binder is usually 40 to 70 ° C., preferably 40 to 60 ° C. If it is less than 40 ° C., the heat resistance of the toner deteriorates, and if it exceeds 70 ° C., the low-temperature fixability becomes insufficient. Due to the coexistence of a modified polyester such as a urea-modified polyester resin, the dry toner of the present invention tends to have good heat-resistant storage stability even when the glass transition point is low, as compared with a known polyester-based toner.

(wax)
In the present invention, the wax (release agent) is preferably contained in the toner in an amount of 1 to 10%. If it is less than 1%, the required releasability cannot be obtained, and the fixing property is deteriorated. If it exceeds 10%, there is a problem such as filming. As the wax used in the toner of the present invention, a low melting point wax having a melting point of 50 to 120 ° C. works more effectively as a release agent in the dispersion with the binder resin between the fixing roller and the toner interface, As a result, the fixing roller is effective against high-temperature offset resistance without applying a release agent such as oil.
The melting point of the wax in the present invention was the maximum endothermic peak measured by a differential scanning calorimeter (DSC).
The following materials can be used as the wax component that functions as a release agent that can be used in the present invention. That is, as specific examples, waxes and waxes include plant waxes such as carnauba wax, cotton wax, wood wax, rice wax, animal waxes such as beeswax and lanolin, mineral waxes such as ozokerite and cercin, And petroleum waxes such as paraffin, microcrystalline, and petrolatum. In addition to these natural waxes, synthetic hydrocarbon waxes such as Fischer-Tropsch wax and polyethylene wax, and synthetic waxes such as esters, ketones and ethers can be used. Furthermore, fatty acid amides such as 12-hydroxystearic acid amide, stearic acid amide, phthalic anhydride imide, and chlorinated hydrocarbon, and poly n-stearyl methacrylate and poly n-lauryl methacrylate which are low molecular weight crystalline polymer resins A crystalline polymer having a long alkyl group in the side chain, such as a polyacrylate homopolymer or copolymer (for example, a copolymer of n-stearyl acrylate-ethyl methacrylate, etc.) can also be used.
In particular, paraffin wax, polyethylene wax, polypropylene wax, sazol wax and the like are preferable, and among these, paraffin wax having a low melting point is preferable in terms of improving low-temperature fixability.

(Coloring agent)
As the colorant used in the present invention, known dyes and pigments can be used. For example, carbon black, nigrosine dye, iron black, naphthol yellow S, Hansa yellow (10G, 5G, G), cadmium yellow, yellow oxidation Iron, ocher, yellow lead, titanium yellow, polyazo yellow, oil yellow, Hansa yellow (GR, A, RN, R), pigment yellow L, benzidine yellow (G, GR), permanent yellow (NCG), Vulcan fast yellow (5G, R), Tartrazine Lake, Quinoline Yellow Lake, Anthrazan Yellow BGL, Isoindolinone Yellow, Bengala, Red Dan, Lead Zhu, Cadmium Red, Cadmium Mercury Red, Antimon Zhu, Permanent Red 4R, Para Red, Faisa Red, Parachlor Rutonitroaniline Red, Resol Fast Scarlet G, Brilliant Fast Scarlet, Brilliant Carnmin BS, Permanent Red (F2R, F4R, FRL, FRLL, F4RH), Fast Scarlet VD, Belkan Fast Rubin B, Brilliant Scarlet G, Resol Rubin GX, Pas -Manent Red F5R, Brilliant Carmine 6B, Pigment Scarlet 3B, Bordeaux 5B, Toluidine Maroon, Permanent Bordeaux F2K, Helio Bordeaux BL, Bordeaux 10B, Bon Maroon Light, Bon Maroon Medium, Eosin Lake, Rhodamine Lake B, Rhodamine Lake Y, Alizarin Lake, thioindigo red B, thioindigo maroon, oil red, quinacridone red, pyrazo Red, polyazo red, chrome vermillion, benzidine orange, perinone orange, oil orange, cobalt blue, cerulean blue, alkali blue rake, peacock blue rake, Victoria blue rake, metal-free phthalocyanine blue, phthalocyanine blue, fast sky blue, indance Ren Blue (RS, BC), Indigo, Ultramarine Blue, Bituminous Blue, Anthraquinone Blue, Fast Violet B, Methyl Violet Lake, Cobalt Purple, Manganese Purple, Dioxane Violet, Anthraquinone Violet, Chrome Green, Zinc Green, Chrome Oxide, Pyridian, Emerald Green , Pigment Green B, Naphthol Green B, Green Gold, Acid Green Lake, Malachite Green A rk, phthalocyanine green, anthraquinone green, titanium oxide, zinc white, lithopone and mixtures thereof can be used. The content of the colorant is usually 1 to 15% by weight, preferably 3 to 10% by weight, based on the toner.

The colorant used in the present invention can also be used as a master batch combined with a resin.
As the binder resin to be kneaded together with the production of the masterbatch or the masterbatch, in addition to the above-mentioned modified and unmodified polyester resins, styrene such as polystyrene, poly p-chlorostyrene, polyvinyltoluene, and substituted polymers thereof; Styrene-p-chlorostyrene copolymer, styrene-propylene copolymer, styrene-vinyltoluene copolymer, styrene-vinylnaphthalene copolymer, styrene-methyl acrylate copolymer, styrene-ethyl acrylate copolymer Styrene-butyl acrylate copolymer, styrene-octyl acrylate copolymer, styrene-methyl methacrylate copolymer, styrene-ethyl methacrylate copolymer, styrene-butyl methacrylate copolymer, styrene-α- Chloromethyl methacrylate copolymer, Tylene-acrylonitrile copolymer, styrene-vinyl methyl ketone copolymer, styrene-butadiene copolymer, styrene-isoprene copolymer, styrene-acrylonitrile-indene copolymer, styrene-maleic acid copolymer, styrene-malein Styrene copolymers such as acid ester copolymers; polymethyl methacrylate, polybutyl methacrylate, polyvinyl chloride, polyvinyl acetate, polyethylene, polypropylene, polyester, epoxy resin, epoxy polyol resin, polyurethane, polyamide, polyvinyl butyral, poly Acrylic resin, rosin, modified rosin, terpene resin, aliphatic or alicyclic hydrocarbon resin, aromatic petroleum resin, chlorinated paraffin, paraffin wax, etc. The

  The master batch can be obtained by mixing and kneading a resin for a master batch and a colorant under a high shear force to obtain a master batch. In this case, an organic solvent can be used in order to enhance the interaction between the colorant and the resin. Also, a so-called flushing method called watering paste containing water of a colorant is mixed and kneaded together with a resin and an organic solvent, and the colorant is transferred to the resin side to remove moisture and organic solvent components. Since it can be used as it is, it does not need to be dried and is preferably used. For mixing and kneading, a high shear dispersion device such as a three-roll mill is preferably used.

  A method for producing an electrophotographic toner in which particles comprising a colorant and a resin and particles comprising at least charge control agent particles are mixed together in a container using a rotating body in order to adhere and fix the charge control agent on the toner particle surface However, in this method, the object of the present invention is to include a step of mixing at a peripheral speed of the rotating body of 40 to 150 m / sec in a container without a fixing member protruding from the inner wall of the container. Toner particles are obtained. Next, the used toner will be described.

  The toner of the present invention may contain a charge control agent as necessary. Known charge control agents can be used, such as nigrosine dyes, triphenylmethane dyes, chromium-containing metal complex dyes, molybdate chelate pigments, rhodamine dyes, alkoxy amines, quaternary ammonium salts (fluorine-modified 4 Secondary ammonium salts or compounds, tungsten simple substances or compounds, fluorine activators, salicylic acid metal salts, and metal salts of salicylic acid derivatives. Specifically, Nitronine-based dye Bontron 03, quaternary ammonium salt Bontron P-51, metal-containing azo dye Bontron S-34, oxynaphthoic acid metal complex E-82, salicylic acid metal complex E- 84, E-89 of a phenol-based condensate (manufactured by Orient Chemical Industry Co., Ltd.), TP-302 of a quaternary ammonium salt molybdenum complex, TP-415 (manufactured by Hodogaya Chemical Industry Co., Ltd.), quaternary ammonium Copy charge PSY VP2038 of salt, copy blue PR of triphenylmethane derivative, copy charge of quaternary ammonium salt NEG VP2036, copy charge NX VP434 (manufactured by Hoechst), LRA-901, LR-147 which is a boron complex (Nippon Carlit), copper phthalocyanine, perylene, quinaclide And azo pigments, and other high molecular compounds having a functional group such as a sulfonic acid group, a carboxyl group, and a quaternary ammonium salt.

  In the present invention, the amount of charge control agent used is determined by the toner production method including the type of binder resin, the presence or absence of additives used as necessary, and the dispersion method, and is uniquely limited. However, it is preferably used in the range of 0.1 to 10 parts by weight with respect to 100 parts by weight of the binder resin. The range of 0.2 to 5 parts by weight is preferable. When the amount exceeds 10 parts by weight, the chargeability of the toner is too high, the effect of the main charge control agent is reduced, the electrostatic attractive force with the developing roller is increased, the flowability of the developer is reduced, and the image density is reduced. Incurs a decline. These charge control agents and mold release agents can be melt-kneaded together with the master batch and the resin, and of course, they may be added when dissolved and dispersed in an organic solvent.

An external additive is used to assist the fluidity, developability, and chargeability of the colored particles obtained in the present invention. As this external additive, inorganic fine particles can be preferably used. The primary particle diameter of the inorganic fine particles is preferably 5 mμ to 2 μm, and particularly preferably 5 mμ to 500 mμ. Moreover, it is preferable that the specific surface area by BET method is 20-500 m < ² > / g. The proportion of the inorganic fine particles used is preferably 0.01 to 5% by weight of the toner, and particularly preferably 0.01 to 2.0% by weight. Specific examples of the inorganic fine particles include, for example, silica, alumina, titanium oxide, barium titanate, magnesium titanate, calcium titanate, strontium titanate, zinc oxide, tin oxide, quartz sand, clay, mica, wollastonite, diatomaceous earth. Examples include soil, chromium oxide, cerium oxide, pengala, antimony trioxide, magnesium oxide, zirconium oxide, barium sulfate, barium carbonate, calcium carbonate, silicon carbide, and silicon nitride. Among these, as the fluidity imparting agent, it is preferable to use hydrophobic silica fine particles and hydrophobic titanium oxide fine particles in combination. In particular, when stirring and mixing is performed using an average particle size of both fine particles of 50 mμ or less, the electrostatic force and van der Waals force with the toner are remarkably improved, so that a desired charge level is obtained. It is clear that even with stirring and mixing inside the developing machine, a fluidity-imparting agent is not detached from the toner, a good image quality that does not generate fireflies and the like can be obtained, and the residual toner can be further reduced. became.

  Titanium oxide fine particles are excellent in environmental stability and image density stability, but have a tendency to deteriorate the charge rise characteristics. Therefore, if the amount of titanium oxide fine particles added is larger than the amount of silica fine particles added, the effect of side effects is large. It is possible to become. However, when the addition amount of the hydrophobic silica fine particles and the hydrophobic titanium oxide fine particles is in the range of 0.3 to 1.5 wt%, the charge rising characteristics are not greatly impaired, and the desired charge rising characteristics can be obtained, that is, repeated copying. It has been found that stable image quality can be obtained and toner blowing can be suppressed even if the process is performed.

  The resin for toner binder can be produced by the following method. Polyol (PO) and polycarboxylic acid (PC) are heated to 150-280 ° C. in the presence of a known esterification catalyst such as tetrabutoxytitanate, dibutyltin oxide, etc., and the generated water is distilled off as necessary. Thus, a polyester having a hydroxyl group is obtained. Next, this is reacted with polyisocyanate (PIC) at 40 to 140 ° C. to obtain a polyester prepolymer (A) having an isocyanate group. Further, this A is reacted with amines (B) at 0 to 140 ° C. to obtain a polyester (UMPE) modified with a urea bond. The number average molecular weight of this modified polyester is 1000 to 10000, preferably 1500 to 6000. When reacting PIC and when reacting A and B, a solvent can be used if necessary. Usable solvents include aromatic solvents (toluene, xylene, etc.); ketones (acetone, methyl ethyl ketone, methyl isobutyl ketone, etc.); esters (ethyl acetate, etc.); amides (dimethylformamide, dimethylacetamide, etc.) and ethers And those inert to isocyanates (PIC), such as tetrahydrofuran (such as tetrahydrofuran). When polyester (PE) that is not modified with a urea bond is used in combination, PE is produced in the same manner as the polyester having a hydroxyl group, and this is dissolved in the solution after completion of the UMPE reaction and mixed.

The dry toner of the present invention can be produced by the following method, but is not limited thereto.
(Toner production method in aqueous medium)
As the aqueous medium used in the present invention, water alone may be used, but a solvent miscible with water may be used in combination. Examples of the miscible solvent include alcohol (methanol, isopropanol, ethylene glycol, etc.), dimethylformamide, tetrahydrofuran, cellosolves (methyl cellosolve, etc.), lower ketones (acetone, methyl ethyl ketone, etc.), and the like.
In the present invention, a urea-modified polyester (UMPE) or the like can be obtained by reacting a reactive modified polyester such as a polyester prepolymer (A) having an isocyanate group with an amine (B) in an aqueous medium. As a method for stably forming a dispersion comprising a modified polyester such as urea-modified polyester or a reactive modified polyester such as prepolymer (A) in an aqueous medium, a modified polyester such as urea-modified polyester or a pre-polymer can be used in an aqueous medium. Examples thereof include a method in which a composition of a toner raw material composed of reactive modified polyester such as polymer (A) is added and dispersed by shearing force. Reactive modified polyester such as prepolymer (A) and other toner composition (hereinafter referred to as toner raw material), colorant, colorant masterbatch, release agent, charge control agent, unmodified polyester resin, etc. Although mixing may be performed when forming the dispersion in the medium, it is more preferable to mix the toner raw materials in advance and then add and disperse the mixture in the aqueous medium. In the present invention, other toner materials such as a colorant, a release agent, and a charge control agent do not necessarily have to be mixed when forming particles in an aqueous medium, but after the particles are formed. , May be added. For example, after forming particles containing no colorant, the colorant can be added by a known dyeing method.

  The dispersion method is not particularly limited, and known equipment such as a low-speed shear method, a high-speed shear method, a friction method, a high-pressure jet method, and an ultrasonic wave can be applied. In order to make the particle size of the dispersion 2 to 20 μm, a high-speed shearing type is preferable. When a high-speed shearing disperser is used, the rotational speed is not particularly limited, but is usually 1000 to 30000 rpm, preferably 5000 to 20000 rpm. The dispersion time is not particularly limited, but in the case of a batch method, it is usually 0.1 to 5 minutes. The temperature during dispersion is usually 0 to 150 ° C. (under pressure), preferably 40 to 98 ° C. Higher temperatures are preferred in that the dispersion of the urea-modified polyester or prepolymer (A) has a low viscosity and is easy to disperse.

  The amount of the aqueous medium used is usually 50 to 2000 parts by weight, preferably 100 to 1000 parts by weight, based on 100 parts of the toner composition containing a polyester such as urea-modified polyester and prepolymer (A). If the amount is less than 50 parts by weight, the dispersion state of the toner composition is poor, and toner particles having a predetermined particle diameter cannot be obtained. If it exceeds 20000 parts by weight, it is not economical. Moreover, a dispersing agent can also be used as needed. It is preferable to use a dispersant because the particle size distribution becomes sharp and the dispersion is stable.

Various dispersants for emulsifying and dispersing are used in an aqueous medium obtained by emulsifying and dispersing an oily phase in which a toner composition component is dispersed. Such a dispersant includes a surfactant, an inorganic fine particle dispersant, a polymer fine particle dispersant and the like.
As surfactants, anionic surfactants such as alkylbenzene sulfonates, α-olefin sulfonates, phosphate esters, alkylamine salts, amino alcohol fatty acid derivatives, polyamine fatty acid derivatives, amine salt types such as imidazoline, Quaternary ammonium salt type cationic surfactants such as alkyltrimethylammonium salt, dialkyldimethylammonium salt, alkyldimethylbenzylammonium salt, pyridinium salt, alkylisoquinolinium salt, benzethonium chloride, fatty acid amide derivative, polyhydric alcohol Nonionic surfactants such as derivatives, for example, amphoteric surfactants such as alanine, dodecyldi (aminoethyl) glycine, di (octylaminoethyl) glycine and N-alkyl-N, N-dimethylammonium betaine. It is.

  Further, by using a surfactant having a fluoroalkyl group, the effect can be obtained in a very small amount. Preferred anionic surfactants having a fluoroalkyl group include fluoroalkyl carboxylic acids having 2 to 10 carbon atoms and metal salts thereof, disodium perfluorooctanesulfonyl glutamate, 3- [omega-fluoroalkyl (C6-C11 ) Oxy] -1-alkyl (C3-C4) sodium sulfonate, 3- [omega-fluoroalkanoyl (C6-C8) -N-ethylamino] -1-propanesulfonic acid sodium, fluoroalkyl (C11-C20) carvone Acids and metal salts, perfluoroalkylcarboxylic acids (C7 to C13) and metal salts thereof, perfluoroalkyl (C4 to C12) sulfonic acids and metal salts thereof, perfluorooctanesulfonic acid diethanolamide, N-propyl-N- ( 2-hydroxyethyl) -Fluorooctanesulfonamide, perfluoroalkyl (C6-C10) sulfonamidopropyltrimethylammonium salt, perfluoroalkyl (C6-C10) -N-ethylsulfonylglycine salt, monoperfluoroalkyl (C6-C16) ethyl phosphate, etc. Is mentioned.

  Product names include Surflon S-111, S-112, S-113 (Asahi Glass Co., Ltd.), Florard FC-93, FC-95, FC-98, FC-129 (Sumitomo 3M Co., Ltd.), Unidyne DS-101. DS-102 (Daikin Kogyo Co., Ltd.), MegaFuck F-110, F-120, F-113, F-191, F-812, F-833 (Dainippon Ink Co., Ltd.), Xtop EF-102 , 103, 104, 105, 112, 123A, 123B, 306A, 501, 201, 204 (manufactured by Tochem Products), and Fgentent F-100, F150 (manufactured by Neos).

Examples of cationic surfactants include aliphatic primary, secondary or secondary amine acids having a fluoroalkyl group, aliphatic quaternary ammonium salts such as perfluoroalkyl (C6-C10) sulfonamidopropyltrimethylammonium salt, benza Luconium salt, benzethonium chloride, pyridinium salt, imidazolinium salt, trade names include Surflon S-121 (manufactured by Asahi Glass), Florard FC-135 (manufactured by Sumitomo 3M), Unidyne DS-202 (manufactured by Daikin Industries) Megafac F-150, F-824 (manufactured by Dainippon Ink, Inc.), Xtop EF-132 (manufactured by Tochem Products), and Footgent F-300 (manufactured by Neos).
In addition, tricalcium phosphate, calcium carbonate, titanium oxide, colloidal silica, hydroxyapatite and the like can be used as an inorganic compound dispersant that is hardly soluble in water.

  Further, the same effect as that of the inorganic dispersant was confirmed for the fine particle polymer. For example, MMA polymer fine particles 1 μm and 3 μm, styrene fine particles 0.5 μm and 2 μm, styrene-acrylonitrile fine particle polymer 1 μm, (PB-200H (Kao) SGP (Soken), Technopolymer SB (Sekisui Plastics), SGP-3G (Soken) Micropearl (Sekisui Fine Chemical)).

  In addition, as a dispersant that can be used in combination with the above inorganic dispersant and fine particle polymer, the dispersed droplets may be stabilized by a polymer protective colloid. For example, acrylic acid, methacrylic acid, α-cyanoacrylic acid, α-cyanomethacrylic acid, itaconic acid, crotonic acid, fumaric acid, maleic acid or maleic anhydride and other (meth) acrylic monomers containing hydroxyl groups Bodies such as β-hydroxyethyl acrylate, β-hydroxyethyl methacrylate, β-hydroxypropyl acrylate, β-hydroxypropyl methacrylate, γ-hydroxypropyl acrylate, γ-hydroxypropyl methacrylate, 3-acrylate Chloro-2-hydroxypropyl, 3-chloro-2-hydroxypropyl methacrylate, diethylene glycol monoacrylate, diethylene glycol monomethacrylate, glycerol monoacrylate, glycerol monomethacrylate, N -Methylol acrylamide, N-methylol methacrylamide, etc., vinyl alcohol or ethers with vinyl alcohol, such as vinyl methyl ether, vinyl ethyl ether, vinyl propyl ether, etc., or esters of compounds containing vinyl alcohol and carboxyl groups, such as Pinyl acetate, pinyl propionate, vinyl butyrate, etc., acrylamide, methacrylamide, diacetone acrylamide or their methylol compounds, acid chlorides such as acrylic acid chloride, methacrylic acid chloride, pinyl pyridine, vinyl pyrrolidone, vinyl imidazole, ethylene imine, etc. Homopolymers or copolymers such as those having nitrogen atoms or heterocyclic rings thereof, polyoxyethylene, polyoxypropylene, polymers Oxyethylene alkylamine, polyoxypropylene alkylamine, polyoxyethylene alkylamide, polyoxypropylene alkylamide, polyoxyethylene nonyl phenyl ether, polyoxyethylene lauryl phenyl ether, polyoxyethylene stearyl phenyl ester, polyoxyethylene nonylphenyl Polyoxyethylenes such as esters, celluloses such as methyl cellulose, hydroxyethyl cellulose, and hydroxypropyl cellulose can be used.

  Furthermore, in order to reduce the viscosity of the dispersion medium containing the toner composition, a solvent in which a polyester such as urea-modified polyester or prepolymer (A) is soluble can be used. The use of a solvent is preferable in that the particle size distribution becomes sharp. The solvent is preferably volatile with a boiling point of less than 100 ° C. from the viewpoint of easy removal. Examples of the solvent include toluene, xylene, benzene, carbon tetrachloride, methylene chloride, 1,2-dichloroethane, 1,1,2-trichloroethane, trichloroethylene, chloroform, monochlorobenzene, dichloroethylidene, methyl acetate, ethyl acetate, Methyl ethyl ketone, methyl isobutyl ketone and the like can be used alone or in combination of two or more. In particular, aromatic solvents such as toluene and xylene and halogenated hydrocarbons such as methylene chloride, 1,2-dichloroethane, chloroform, and carbon tetrachloride are preferable. The usage-amount of the solvent with respect to 100 parts of prepolymers (A) is 0-300 parts normally, Preferably it is 0-100 parts, More preferably, it is 25-70 parts. When a solvent is used, the solvent (solvent) is removed from the resultant reaction product under normal pressure or reduced pressure after the extension and / or crosslinking reaction of the modified polyester (prepolymer) with an amine.

  The elongation and / or crosslinking reaction time is selected, for example, depending on the reactivity of the isocyanate group structure of the prepolymer (A) and the amines (B), but is usually 10 minutes to 40 hours, preferably 2 to 24 hours. It's time. The reaction temperature is generally 0 to 150 ° C, preferably 40 to 98 ° C. Moreover, a well-known catalyst can be used as needed. Specific examples include dibutyltin laurate and dioctyltin laurate. In addition, as an extender and / or a crosslinking agent, the above-described amines (B) are used.

  In the present invention, it is preferable to remove the solvent of the dispersion at 10 to 50 ° C. prior to the removal of the solvent from the dispersion (reaction liquid) after the elongation and / or crosslinking reaction. The toner is deformed by liquid agitation before the removal of the solvent. Further, Dv and Dn can be controlled by adjusting, for example, characteristics of resin fine particles, addition amount, and the like.

The toner of the present invention can be used as a two-component developer. In this case, it may be used by mixing with a magnetic carrier, and the content ratio of the carrier and the toner in the developer is preferably 1 to 10 parts by weight of the toner with respect to 100 parts by weight of the carrier. As the magnetic carrier, conventionally known ones such as iron powder, ferrite powder, magnetite powder, magnetic resin carrier having a particle diameter of about 20 to 200 μm can be used. Examples of the coating material include amino resins such as urea-formaldehyde resin, melamine resin, benzoguanamine resin, urea resin, polyamide resin, and epoxy resin. Polyvinyl and polyvinylidene resins such as acrylic resins, polymethyl methacrylate resins, polyacrylonitrile resins, polyvinyl acetate resins, polyvinyl alcohol resins, polyvinyl butyral resins, polystyrene resins and styrene acrylic copolymer resins, Halogenated olefin resin such as vinyl, polyester resin such as polyethylene terephthalate resin and polybutylene terephthalate resin, polycarbonate resin, polyethylene resin, polyvinyl fluoride resin, polyvinylidene fluoride resin, polytrifluoroethylene resin, polyhexafluoro Propylene resin, copolymer of vinylidene fluoride and acrylic monomer, copolymer of vinylidene fluoride and vinyl fluoride, tetrafluoroethylene and vinylidene fluoride And fluoro such as terpolymers of non-fluoride monomers including, and silicone resins. Moreover, you may make conductive powder etc. contain in coating resin as needed. As the conductive powder, metal powder, carbon black, titanium oxide, tin oxide, zinc oxide or the like can be used. These conductive powders preferably have an average particle diameter of 1 μm or less. When the average particle diameter is larger than 1 μm, it becomes difficult to control electric resistance.
The toner of the present invention can also be used as a one-component magnetic toner that does not use a carrier or a non-magnetic toner.

  An embodiment for carrying out the image forming method of the present invention will be described with reference to FIG. The tandem image forming apparatus shown in FIG. 1 is a tandem type color image forming apparatus. The tandem image forming apparatus includes a copying machine main body (150), a paper feed table (200), a scanner (300), and an automatic document feeder (ADF) (400).

  The copying apparatus main body (150) is provided with an endless belt-shaped intermediate transfer body (1050) at the center. The intermediate transfer member (1050) is stretched around support rollers (1014), (1015), and (1016), and can rotate clockwise in FIG. An intermediate transfer member cleaning device (1017) for removing residual toner on the intermediate transfer member (1050) is disposed in the vicinity of the support roller (1015). The intermediate transfer member (1050) stretched between the support roller (1014) and the support roller (1015) has four image forming units (1018) of yellow, cyan, magenta, and black along the conveyance direction. A tandem developing device (120) arranged opposite to each other is arranged. An exposure device (1021) is disposed in the vicinity of the tandem developing device (120). A secondary transfer device (1022) is disposed on the side of the intermediate transfer member (1050) opposite to the side on which the tandem developing device (120) is disposed. In the secondary transfer device (1022), a secondary transfer belt (1024), which is an endless belt, is stretched between a pair of rollers (1023), and a transfer sheet conveyed on the secondary transfer belt (1024) and The intermediate transfer member (1050) can contact each other. A fixing device (1025) is disposed in the vicinity of the secondary transfer device (1022). The fixing device (1025) includes a fixing belt (1026) that is an endless belt, and a pressure roller (1027) that is pressed against the fixing belt (1027).

  In the tandem image forming apparatus, in the vicinity of the secondary transfer device (1022) and the fixing device (1025), a sheet reversing device (1028) for reversing the transfer paper for image formation on both sides of the transfer paper. ) Is arranged.

  Next, full color image formation (color copying) using the tandem developing device (120) will be described. That is, first, a document is set on the document table (130) of the automatic document feeder (ADF) (400), or the automatic document feeder (400) is opened and the contact glass (1032) of the scanner (300) is opened. A document is set on the document and the automatic document feeder (400) is closed.

  When a start switch (not shown) is pressed, when a document is set on the automatic document feeder (400), the document is transported and moved onto the contact glass (1032). ) Immediately after the document is set on the scanner (300), the first traveling body (1033) and the second traveling body (1034) travel. At this time, light from the light source is irradiated by the first traveling body (1033) and reflected light from the document surface is reflected by the mirror in the second traveling body (1034), and is read through the imaging lens (1035). The color original (color image) is read at (1036) and read, and the image information is black, yellow, magenta and cyan.

  Each image information of black, yellow, magenta, and cyan is stored in each image forming unit (1018) (black image forming unit, yellow image forming unit, magenta image forming unit, and cyan in the tandem developing unit 120. Image forming means), and each toner image of black, yellow, magenta and cyan is formed in each image forming means. That is, each image forming means (1018) (black image forming means, yellow image forming means, magenta image forming means, and cyan image forming means) in the tandem developing means (120) is as shown in FIG. Electrostatic latent image carrier (1110) (black electrostatic latent image carrier (1010K), yellow electrostatic latent image carrier (1010Y), magenta electrostatic latent image carrier (1010M), and Electrostatic latent image carrier for cyan (1010C)), charging device (160) for uniformly charging the electrostatic latent image carrier (1110), and for each color image corresponding image based on each color image information And exposing the electrostatic latent image carrier (L in FIG. 2) to form an electrostatic latent image corresponding to each color image on the electrostatic latent image carrier, and the electrostatic latent image. Each color toner (black toner A developing device (61) that develops using yellow toner, magenta toner, and cyan toner to form a toner image with each color toner, and transfer charging for transferring the toner image onto the intermediate transfer body (1050) Device (1062), a cleaning device (63), and a static eliminator (64), and each monochrome image (black image, yellow image, magenta image, and cyan image) based on the image information of each color. ) Can be formed. The black image, the yellow image, the magenta image, and the cyan image formed in this way are respectively transferred onto the intermediate transfer member (1050) that is rotated by the support rollers (1014), (1015), and (1016). A black image formed on the electrostatic latent image carrier (1010K), a yellow image formed on the yellow electrostatic latent image carrier (1010Y), and a magenta electrostatic latent image carrier (1010M). The formed magenta image and the cyan image formed on the cyan electrostatic latent image carrier (1010C) are sequentially transferred (primary transfer). Then, the black image, the yellow image, the magenta image, and the cyan image are superimposed on the intermediate transfer member (1050) to form a composite color image (color transfer image).

  On the other hand, in the paper feed table (200), one of the paper feed rollers (142) is selectively rotated so that the sheet (recording paper) is fed from one of the paper feed cassettes (144) provided in the paper bank (143). ), Separated one by one by the separation roller (145), sent to the paper feed path (146), and conveyed by the conveyance roller (147) to the paper feed path (148) in the copier body (150). Guide and stop against the registration roller (1049). Alternatively, the sheet feed roller (142) is rotated to feed out the sheets (recording paper) on the manual feed tray (1054), separated one by one by the separation roller (1058), and put into the manual feed path (1053). It stops against the registration roller (1049). The registration roller (1049) is generally used while being grounded, but may be used in a state where a bias is applied to remove paper dust from the sheet. Then, the registration roller (1049) is rotated in synchronization with the synthesized color image (color transfer image) synthesized on the intermediate transfer member (1050), and the intermediate transfer member (1050), the secondary transfer device (1022), and the like. The sheet (recording paper) is sent between the sheets, and the composite color image (color transfer image) is transferred (secondary transfer) onto the sheet (recording paper) by the secondary transfer device (1022). A color image is transferred and formed on (recording paper). The residual toner on the intermediate transfer member (1050) after image transfer is cleaned by the intermediate transfer member cleaning device (1017).

  The sheet (recording paper) on which the color image has been transferred is conveyed by the secondary transfer device (1022) and sent to the fixing device (1025). In the fixing device (1025), heat and pressure are applied. The composite color image (color transfer image) is fixed on the sheet (recording paper). Thereafter, the sheet (recording paper) is switched by the switching claw (1055) and discharged by the discharge roller (1056) and stacked on the paper discharge tray (1057) or switched by the switching claw (1055). After being reversed by the apparatus (1028) and guided again to the transfer position, an image is recorded also on the back surface, then discharged by the discharge roller (1056), and stacked on the discharge tray (1057).

  EXAMPLES The present invention will be further described below with reference to examples, but the present invention is not limited thereto. Hereinafter, a part shows a weight part.

(Example of polyester production)
In a reaction vessel equipped with a cooling tube, a stirrer, and a nitrogen introduction tube, 690 parts of bisphenol A ethylene oxide 2-mole adduct and 256 parts of terephthalic acid were subjected to polycondensation at 230 ° C. for 8 hours under normal pressure, and then reduced in pressure to 10 to 15 mmHg. And then cooled to 160 ° C., 18 parts of phthalic anhydride was added thereto and reacted for 2 hours to obtain unmodified polyester (1).
The obtained polyester (1) had a weight average molecular weight of 4,000, an acid value of 10 KOH mg / g, and a glass transition point of 50 ° C.

(Prepolymer production example)
In a reaction vessel equipped with a cooling tube, a stirrer and a nitrogen introduction tube, 800 parts of bisphenol A ethylene oxide 2-mol adduct, 180 parts of isophthalic acid, 60 parts of terephthalic acid, and 2 parts of dibutyltin oxide were placed at normal pressure. The mixture was reacted at 8 ° C. for 8 hours, further reacted for 5 hours while dehydrating at a reduced pressure of 10 to 15 mmHg, cooled to 160 ° C., 32 parts of phthalic anhydride was added thereto, and reacted for 2 hours.
Subsequently, it cooled to 80 degreeC and reacted with 170 parts of isophorone diisocyanate in ethyl acetate for 2 hours, and isocyanate group containing [Prepolymer 1] was obtained.

(Production example of ketimine compound)
In a reaction vessel equipped with a stir bar and a thermometer, 30 parts of isophoronediamine and 70 parts of methyl ethyl ketone were charged and reacted at 50 ° C. for 5 hours to obtain [ketimine compound 1].

(Production Example 1 of Wax Dispersion)
70 parts of ethyl acetate, 25 parts of the above polyester (1), 5 parts of paraffin wax (melting point: 70 ° C.): 5 parts are mixed, stirred at 70 ° C. for 30 minutes, then cooled to 23 ° C. with stirring, and further 60 Add 3% zirconia in the volume ratio and paint conditioner no. The mixture was stirred with Model 5400 (made by REDDEVIL, USA) for 12 hours to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.35 μm. D95wax1 was 0.48 μm.

(Production Example 2 of Wax Dispersion)
Ethyl acetate: 70 parts, polyester (1): 25 parts, paraffin wax as wax (melting point 70 ° C.): 5 parts, stirred at 70 ° C. for 30 minutes, then cooled to 23 ° C. with stirring, and further 60% volume ratio 3 mm of zirconia was added and stirred with a paint conditioner No. 5400 type (manufactured by REDDEVIL, USA) for 18 hours to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.20 μm. D95wax1 was 0.33 μm.

(Production Example 3 of Wax Dispersion)
Ethyl acetate: 70 parts, polyester (1): 25 parts, paraffin wax as wax (melting point 70 ° C.): 5 parts, stirred at 70 ° C. for 30 minutes, then cooled to 23 ° C. with stirring, and further 60% volume ratio 3 mm of zirconia was added and stirred with a paint conditioner No. 5400 (made by REDDEVIL, USA) for 24 hours to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.12 μm. D95wax1 was 0.16 μm.

(Production Example 4 of Wax Dispersion)
70 parts of ethyl acetate, 25 parts of the above polyester (1), 5 parts of paraffin wax (melting point: 70 ° C.): 5 parts, and 3% zirconia with a volume ratio of 60% were added. The mixture was stirred for 24 hours with Model 5400 (manufactured by REDDEVIL, USA) to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.28 μm. D95wax1 was 0.45 μm.

(Production Example of Wax Dispersion-5)
70 parts of ethyl acetate, 25 parts of the above polyester (1), 5 parts of paraffin wax (melting point 70 ° C.): 5 parts, and 3% zirconia with a volume ratio of 60%, paint conditioner No. 5400 type (US REDDEVIL) For 18 hours to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.46 μm. D95wax1 was 0.81 μm.

(Production Example of Wax Dispersion-6)
70 parts of ethyl acetate, 25 parts of the above polyester (1), 5 parts of paraffin wax (melting point: 70 ° C.): 5 parts are mixed, stirred at 55 ° C. for 30 minutes, then cooled to 23 ° C. with stirring, and further 60 % Volume ratio of 3 mm zirconia was added, and paint conditioner no. The mixture was stirred with Model 5400 (manufactured by REDDEVIL, USA) for 18 hours to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.37 μm. D95wax1 was 0.61 μm.

(Production Example of Wax Dispersion-7)
70 parts of ethyl acetate, 25 parts of the above polyester (1), 5 parts of paraffin wax (melting point: 70 ° C.): 5 parts are mixed, stirred at 70 ° C. for 30 minutes, then cooled to 23 ° C. with stirring, and further 60 Add 3% zirconia in the volume ratio and paint conditioner no. The mixture was stirred for 6 hours with Model 5400 (manufactured by REDDEVIL, USA) to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.43 μm. D95wax1 was 0.90 μm.

(Production Example of Wax Dispersion-8)
70 parts of ethyl acetate, 25 parts of the above polyester (1), 5 parts of paraffin wax (melting point: 70 ° C.): 5 parts, and 3% zirconia with a volume ratio of 60% were added. The mixture was stirred with Model 5400 (made by REDDEVIL, USA) for 12 hours to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.61 μm. D95wax1 was 1.36 μm.

(Production Example of Wax Dispersion-9)
70 parts of ethyl acetate, 25 parts of the above polyester (1), 5 parts of paraffin wax (melting point 70 ° C.): 5 parts are mixed, stirred at 55 ° C. for 15 minutes, then cooled to 23 ° C. with stirring, and further 60 Add 3% zirconia in the volume ratio and paint conditioner no. The mixture was stirred with Model 5400 (manufactured by REDDEVIL, USA) for 18 hours to obtain [Wax Dispersion 1]. The volume average particle diameter (Dv) of the wax dispersed particles contained in the obtained [Wax Dispersion 1] is measured by a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. As a result, Dwax1 was 0.39 μm. D95wax1 was 0.82 μm.

(Production of kneaded composite 1 of modified layered inorganic mineral and binder resin)
1200 parts by mass of water, 174 parts by mass of ELEMENTIS BENTONE57 (organic modified bentonite, quaternary ammonium cation modified product) and 1570 parts by mass of the above [Polyester 1] were mixed using a Henschel mixer (Mitsui Mining Co., Ltd.). . The mixture is kneaded with a two roll at 150 ° C. for 30 minutes, then rolled and cooled, and pulverized with a pulverizer (manufactured by Hosokawa Micron) to prepare [kneaded composite 1 of modified layered inorganic mineral and binder resin 1]. did.

(Preparation of organic resin fine particle dispersion)
In a reaction vessel in which a stir bar and a thermometer are set, 683 parts by mass of water, 20 parts by mass of a sodium salt of ethylene oxide methacrylate adduct sulfate ("Eleminol RS-30" manufactured by Sanyo Chemical Industries), 78 parts by mass of styrene , 78 parts by mass of methacrylic acid, 120 parts by mass of butyl acrylate, and 1 part by mass of ammonium persulfate were added and stirred at 400 rpm for 15 minutes to obtain a white emulsion. The emulsion was heated to raise the system temperature to 75 ° C. and reacted for 5 hours. Next, 30 parts by mass of a 1% by mass ammonium persulfate aqueous solution was added, and the mixture was aged at 75 ° C. for 5 hours. Vinyl resin particles (styrene-methacrylic acid-butyl acrylate-methacrylic acid ethylene oxide adduct sulfate sodium salt) Copolymer) aqueous dispersion (fine particle dispersion 1) was prepared.
The volume average particle diameter (Dv) of the organic resin fine particles contained in the obtained organic resin fine particle dispersion was measured by a particle size distribution measuring device (“nanotrac UPA-150EX”; manufactured by Nikkiso Co., Ltd.), and found to be 55 nm. .

(Preparation of aqueous phase)
Water: 990 parts, [fine particle dispersion 1]: 83 parts, 48.5% aqueous solution of dodecyl diphenyl ether disulfonate (Eleminol MON-7: Sanyo Chemical Industries): 37 parts, ethyl acetate: 90 parts The mixture was stirred to obtain a milky white liquid. This is designated as [Aqueous Phase 1].

(Synthesis of MB)
In a reaction vessel equipped with a condenser, a stirrer and a nitrogen introduction tube, 319 parts of bisphenol A propylene oxide 2-mole adduct: 449 parts, 449 parts of bisphenol A ethylene oxide 2-mole adduct, 243 parts of terephthalic acid, adipic acid: 53 parts and dibutyltin oxide: 2 parts were added, reacted at 230 ° C. at normal pressure for 8 hours, further reacted at 5 to 15 mm Hg under reduced pressure, and then put 7 parts of trimellitic anhydride into the reaction vessel, The reaction was carried out at 180 ° C. and normal pressure for 2 hours to obtain [Polyester 1 for MB]. [Polyester 1 for MB] had a number average molecular weight of 1,900, a weight average molecular weight of 6,100, a Tg of 43 ° C., and an acid value of 1.1.
Water: 30 parts, C.I. I. Pigment Red 122 (Magenta R: manufactured by Toyo Ink): 40 parts, [Polyester 1 for MB]: 60 parts are added, mixed with a Henschel mixer (manufactured by Mitsui Mining Co., Ltd.), and the mixture in which water is soaked into the pigment aggregate is obtained. Obtained. The mixture was kneaded for 45 minutes at 130 ° C. using two rolls, rolled and cooled, and pulverized with a pulverizer to obtain [Masterbatch 1].

[Example 1]
(Production of oil phase)
In a container equipped with a stir bar and thermometer, 30 parts of 65% ethyl acetate solution of [Polyester 1], 50 parts of [Wax dispersion 1], 20 parts of 50% ethyl acetate solution of [Masterbatch 1] The mixture was stirred and stirred at 23 ° C. for 24 hours to obtain [Pigment / Wax Dispersion 1].

(Emulsification → Desolvation)
[Pigment / Wax Dispersion 1]: 664 parts, [Prepolymer 1]: 139 parts, [Ketimine Compound 1]: 5.9 parts in a container, and 5,000 rpm with a TK homomixer (made by Tokushu Kika) After mixing for 1 minute, [Aqueous phase 1]: 1,200 parts was added to the container, and mixed with a TK homomixer at a rotation speed of 10,000 rpm for 20 minutes to obtain [Emulsion slurry 1].
[Emulsified slurry 1] was put into a container equipped with a stirrer and a thermometer, and the solvent was removed at 30 ° C. for 8 hours to obtain [Emulsified slurry 1].

(Washing → drying)
[Emulsified slurry 1]: After 100 parts were filtered under reduced pressure, 100 parts of ion-exchanged water was added to the filter cake, mixed with a TK homomixer (rotation speed: 12,000 rpm for 10 minutes), and then filtered. 100 parts of 10% aqueous sodium hydroxide solution was added to the filter cake, mixed with a TK homomixer (30 minutes at 12,000 rpm), and then filtered under reduced pressure. To this filter cake, 100 parts of 10% hydrochloric acid was added, mixed with a TK homomixer (rotation speed: 12,000 rpm for 10 minutes), and then filtered. To this filter cake, 300 parts of ion-exchanged water was added, mixed with a TK homomixer (rotation speed: 12,000 rpm for 10 minutes) and then filtered twice to obtain [Filter cake 1].
[Filtration cake 1] was dried at 40 ° C. for 48 hours in a circulating drier and sieved with a mesh of 75 μm, and the resulting toner base particles: 100 parts of hydrophobic silica (hexamethyldisilazane surface treatment) Product, specific surface area: 200 m 2 / g): 0.5 part and hydrophobized rutile type titanium oxide (isobutyltrimethoxysilane surface-treated product, average primary particle size: 0.02 μm): 0.5 part by Henschel mixer The toner (1) was obtained by mixing.
A cross section of 100 particles of the toner (1) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.38.

[Example 2]
(Production of oil phase)
[Pigment / Wax Dispersion 2] was obtained in the same manner as in Example 1 except that [Wax Dispersion 1] added during oil phase preparation was changed to [Wax Dispersion 2].

(Emulsification → Desolvation)
[Pigment / Wax Dispersion 2]: 664 parts, [Prepolymer 1]: 139 parts, [Ketimine Compound 1]: 5.9 parts, [Kneaded Composite 1 of Modified Layered Inorganic Mineral and Binder 1] 120% ethyl acetate solution in a container and mixed with a TK homomixer (manufactured by Tokushu Kika) at 5,000 rpm for 1 minute, then [aqueous phase 1]: 1,200 parts are added to the container, and the TK homomixer is added. The mixture was mixed for 20 minutes at 10,000 rpm to obtain [Emulsified slurry 2].
[Emulsified slurry 2] was put into a container equipped with a stirrer and a thermometer, and the solvent was removed at 30 ° C. for 8 hours to obtain [Emulsified slurry 2]. Thereafter, washing, drying and external additive treatment were performed in the same manner as in Example 1 to obtain a toner (2). A cross section of 100 particles of the toner (2) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.20.

[Example 3]
Toner (3) was obtained in the same manner as in Example 2, except that [Wax Dispersion 2] added during the preparation of the oil phase was changed to [Wax Dispersion 3]. A cross section of 100 particles of the toner (3) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.12.

[Example 4]
Toner (4) was obtained in the same manner as in Example 2 except that [Wax Dispersion 2] added during oil phase preparation was changed to [Wax Dispersion 4]. A cross section of 100 particles of the toner (4) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.27.

[Example 5]
Toner (5) was obtained in the same manner as in Example 2 except that [Wax Dispersion 2] added during oil phase preparation was changed to [Wax Dispersion 5]. A cross section of 100 particles of the toner (5) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.46.

[Example 6]
Toner (6) was obtained in the same manner as in Example 2 except that [Wax Dispersion 2] added during the preparation of the oil phase was changed to [Wax Dispersion 6]. A cross section of 100 particles of the toner (6) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.37.

[Comparative Example 1]
Toner (7) was obtained in the same manner as in Example 1 except that [Wax Dispersion 1] added during oil phase preparation was changed to [Wax Dispersion 7]. A cross section of 100 particles of the toner (7) was stained with RuO ₂ and observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.45.

[Comparative Example 2]
Toner (8) was obtained in the same manner as in Example 2 except that [Wax Dispersion 2] added during oil phase preparation was changed to [Wax Dispersion 8]. A cross section of 100 particles of the toner (8) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.59.

[Comparative Example 3]
Toner (9) was obtained in the same manner as in Example 2 except that [Wax Dispersion 2] added during the preparation of the oil phase was changed to [Wax Dispersion 9]. A cross section of 100 particles of the toner (9) was stained with RuO ₂ , observed with a TEM, and the wax particle size was measured. As a result, Dwax2 was 0.39.

(Measurement of particle size of wax dispersion)
The particle size was measured using “LA-920” (manufactured by Horiba, Ltd.). During the measurement of LA-920, analysis was performed using an application dedicated to LA-920 (Ver3.32) (manufactured by Horiba, Ltd.). Specifically, LA-920 was measured by measuring the background with the solvent (ethyl acetate) used in the wax dispersion, adjusting the optical axis, then dropping the dispersion agent dispersion, and measuring the transmittance of LA-920. The dispersed particle size was measured under the condition that the value was in the range of 70 to 95%. It is important for this measuring apparatus to measure under the condition that the transmittance value of LA-920 is in the range of 70 to 95% from the viewpoint of measurement reproducibility of the particle diameter. In order to obtain the transmittance value, it is necessary to adjust the dripping amount of the dispersion.
Measurement and analysis conditions were set as follows.
Data acquisition frequency: 15 times Relative refractive index: 1.20
Circulation: 5
Ultrasonic intensity: 7
Ultrasonic irradiation time: 3 minutes

(Glass transition point Tg (℃))
The glass transition point is measured with a Rigaku THRMOFLEX TG8110 manufactured by Rigaku Corporation at a temperature increase rate of 10 ° C./min.
A method for measuring Tg will be outlined. As an apparatus for measuring Tg, a TG-DSC system TAS-100 manufactured by Rigaku Corporation was used.
First, about 10 mg of a sample is placed in an aluminum sample container, which is placed on a holder unit and set in an electric furnace. First, after heating from room temperature to 150 ° C. at a temperature rising rate of 10 ° C./min, the sample was allowed to stand at 150 ° C. for 10 minutes, the sample was cooled to room temperature and left for 10 minutes, and the temperature rising rate was again increased to 150 ° C. under a nitrogen atmosphere. DSC measurement was performed by heating at min. Tg was calculated from the tangent of the endothermic curve near the Tg and the base line using the analysis system in the TAS-100 system.

(Image graininess, sharpness)
Using a digital full-color copying machine (imageColor 2800, manufactured by Ricoh), a photographic image was output in a single color, and the degree of graininess and sharpness was visually evaluated. In order from the best, “◎” is equivalent to offset printing, “○” is slightly worse than offset printing, “△” is much worse than offset printing, “×” is about the same as conventional electrophotographic images (very much Bad).

(Fixability evaluation)
Ricoh Copier Co., Ltd. using a Teflon (registered trademark) roller as a fixing roller MF2200 A machine having a modified fixing unit was set with Ricoh type 6200 paper and subjected to a copying test. The cold offset temperature (fixing lower limit temperature) and the hot offset temperature (hot offset resistant temperature) were determined by changing the fixing temperature. The minimum fixing temperature of the conventional low-temperature fixing toner is about 140 to 150 ° C. The evaluation conditions for low-temperature fixing are as follows: the paper feed linear speed is 120 to 150 mm / sec, the surface pressure is 1.2 kgf / cm ² , the nip width is 3 mm, and the high temperature offset is the paper feed linear speed of 50 mm / sec. The contact pressure was set to 2.0 kgf / cm ² and the nip width was 4.5 mm. The criteria for each characteristic evaluation are as follows.
Low-temperature fixability (5-level evaluation)
Good ◎: Less than 140 ° C., ○: 140-149 ° C., □: 150-159 ° C., Δ: 160-170 ° C., X: 170 ° C. or more
Good: 201 ° C. or higher, ○: 200-191 ° C., □: 190-181 ° C., Δ: 180-171 ° C., X: 170 ° C. or lower

(Heat resistant storage stability)
After the toner was stored at 50 ° C. for 8 hours, it was sieved with a 42 mesh sieve for 2 minutes, and the residual ratio on the wire mesh was regarded as heat resistant storage stability. A toner having better heat-resistant storage stability has a lower residual ratio. The following four levels were evaluated.
×: 30% or more
Δ: 20-30%
○: 10 to 20%
A: Less than 10%

  The results of each example and comparative example are shown in Table 2.

FIG. 2 is a cross-sectional configuration diagram of a main part of an example of an image forming apparatus. FIG. 2 is a partially enlarged view of the image forming apparatus illustrated in FIG. 1.

Explanation of symbols

1010K electrostatic latent image carrier for black 1010Y electrostatic latent image carrier for yellow 1010M electrostatic latent image carrier for magenta 1010C electrostatic latent image carrier for cyan 1014 support roller 1015 support roller 1016 support roller 1017 intermediate transfer cleaning device DESCRIPTION OF SYMBOLS 1018 Image formation means 1021 Exposure apparatus 1022 Secondary transfer apparatus 1023 Roller 1024 Secondary transfer belt 1025 Fixing apparatus 1026 Fixing belt 1027 Pressure roller 1028 Sheet reversing apparatus 1032 Contact glass 1033 First traveling body 1034 Second traveling body 1035 Imaging lens 1036 Reading sensor 1049 Registration roller 1050 Intermediate transfer member 1053 Manual feed path 1054 Manual feed tray 1055 Switching claw 1056 Ejection roller 1057 Ejection tray 1058 Separation Over La 61 developing device 1062 transfer charger 63 cleaning device 64 discharger 65
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DESCRIPTION OF SYMBOLS 120 Tandem type developing device 130 Document stand 142 Paper feed roller 143 Paper bank 144 Paper feed cassette 145 Separation roller 146 Paper feed path 147 Transport roller 148 Paper feed path 150 Copying device main body 160 Charging device 200 Paper feed table 300 Scanner 400 Automatic document transport Equipment (ADF)

Claims (17)

In a method for producing a toner obtained by granulating toner base particles from an aqueous liquid medium obtained by emulsifying / dispersing an oil phase containing at least a wax and a binder resin material,
A wax dispersion manufacturing process for forming a wax dispersion in which the wax is dispersed in an organic solvent, an oil phase forming process for forming an oil phase containing a binder resin component and a wax using the wax dispersion, and the oil phase An emulsifying and dispersing step of dispersing and / or emulsifying in an aqueous medium,
The wax average particle diameter Dwax1 in the wax dispersion and the average particle diameter Dwax2 of the wax dispersion domain in the toner particles are:
Dwax2 = 0.9 to 1.1 × Dwax1,
The particle size D95wax1 of 95/100 from the bottom of the wax particle size distribution in the wax dispersion is D95wax1 ≦ 1.8 × Dwax1
A method for producing a toner, wherein   The toner production method according to claim 1, wherein the oil phase includes at least a wax, a binder resin component, and an organic solvent.   The oil phase is formed by mixing at least an organic solvent and the wax to 50 ° C. or higher and then mixing a wax dispersion obtained by lowering the temperature and other toner composition components. The method for producing a toner according to 1 or 2.   4. The method for producing a toner according to claim 3, wherein the other toner composition components are mixed with the wax dispersion in the form of an organic solvent liquid containing the other toner composition components to form the oil phase.   The toner manufacturing method according to claim 1, wherein the wax dispersion contains a part of a binder resin component.   An oil phase obtained by dissolving at least the binder resin component and a binder resin precursor composed of a modified polyester resin in an organic solvent and dispersing the wax is elongated or crosslinked with the binder resin precursor. After the compound to be dissolved is dissolved, the oil phase is dispersed in the form of droplets in an aqueous medium containing a fine particle dispersant to obtain an emulsified dispersion, and the binder resin precursor is crosslinked in the emulsified dispersion. And / or a step of removing the organic solvent by an extension reaction.   The oil phase is obtained by dissolving or dispersing a layered inorganic mineral obtained by modifying at least part of ions between layers of the layered inorganic mineral with organic ions. Toner production method.   The method for producing a toner according to claim 1, wherein the binder resin is a polyester resin.   The toner production method according to claim 1, wherein the content of the polyester resin in the binder resin is 50 to 100% by weight.   The toner production method according to any one of claims 1 to 9, wherein the polyester resin has a THF-soluble component having a weight average molecular weight of 1,000 to 30,000.   11. The method for producing a toner according to claim 1, wherein the acid value of the acidic group-containing polyester resin is 1.0 to 50.0 (KOH mg / g).   The method for producing a toner according to claim 1, wherein the acidic group-containing polyester resin has a glass transition point of 35 to 65 ° C.   13. The method for producing a toner according to claim 1, wherein the polymer having a site capable of reacting with the compound having an active hydrogen group has a weight average molecular weight of 3,000 to 20,000.   14. The toner production method according to claim 1, wherein the toner has an acid value of 0.5 to 40.0 (KOH mg / g).   The method for producing a toner according to any one of claims 1 to 14, wherein the toner has a glass transition point of 40 to 70 ° C.   The toner production method according to claim 1, wherein the volume average particle diameter Dv / number average particle diameter Dn of the toner is 1.30 or less.   The toner production method according to claim 1, wherein the number of particles of 2 μm or less of the toner is 20% by number or less.

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