Patent Grant
9835966
This application is based on and claims priority under 35 USC 119 from Japanese Patent Application No. 2016-024132 filed Feb. 10, 2016.
1. Technical Field
The present invention relates to an electrostatic charge image developer, a developer cartridge, and a process cartridge.
2. Related Art
Currently, a method for visualizing image information through an electrostatic charge image by electrophotography or the like is used in various fields. In the electrophotography, image information is visualized as an image via a transferring step in which the image information is formed on the surface of an image holding member (a photoreceptor) by charging and irradiating steps as an electrostatic charge image, and a toner image is developed on the surface of a photoreceptor using a developer including a toner to transfer this toner image on a recording medium such as paper; and a fixing step in which the toner image is fixed on the surface of the recording medium. In addition, as the toner, a toner in which various external additives are added to toner particles is used.
According to an aspect of the invention, there is provided an electrostatic charge image developer including:
an electrostatic charge image developing toner that includes toner particles, and an external additive which is added to the toner particles and which includes silica particles whose compression aggregation degree is from 60% to 95% and particle compression ratio is from 0.20 to 0.40; and
a carrier for developing an electrostatic charge image that includes a core particle and a resin coated layer which covers a surface of the core particle and that has a surface roughness Ra (based on JIS-B0601) of 0.5 μm or less and a circularity of 0.975 or more.
Exemplary embodiments of the present invention will be described in detail based on the following figures, wherein:
Hereinafter, the exemplary embodiment will be described as one example of the invention.
Electrostatic Charge Image Developer
The electrostatic charge image developer according to the exemplary embodiment includes an electrostatic charge image developing toner (hereinafter, simply referred to as a “toner”) having toner particles and an external additive added to the toner particles, and a carrier.
The carrier includes a core particle and a resin coated layer which covers the surface of the core particle. The surface roughness Ra (based on JIS-B0601) of the carrier 0.5 μm or less and the circularity of the carrier is 0.975 or more.
An external additive includes silica particles (hereinafter, referred to as a “specific silica particles”) whose compression aggregation degree is from 60% to 95%, and particle compression ratio is from 0.20 to 0.40.
In the developer according to the exemplary embodiment, even if the carrier satisfying the above requirement is used, a decrease in an image density is prevented by adding the specific silica particles to the toner particles. The reason is presumed as follows.
In the related art, as the carrier in the developer, a carrier includes a core particle and a resin coated layer coating the surface of the core particle is used. In this carrier, it is considered that the carrier whose surface roughness Ra and circularity are within the above range has ruggedness on the surface, and by providing such the surface ruggedness, it is possible to form a resin coated layer having high coverage and prevent a decrease in a charge imparting ability of the carrier.
Here, the silica particles added to the toner particles may flake from the toner particles due to mechanical load caused by stirring within a developing unit, and the silica particles flaked from the toner may be attached to the surface of the carrier. Since the carrier whose surface roughness Ra and circularity are within the above range has a rough surface, as illustrated in
In particular, since an adhesive power between the carriers is increased due to the influence of moisture in a high temperature and high humidity environment (for example, an environment of 25° C. or more and 65% or more), in an aspect in which a continuous traveling is performed at a low image density (for example, an image having an image density of 3% or less) in an high temperature and high humidity environment and then printing is further performed in a low temperature and low humidity environment (for example, an environment of 15° C. or less and 25% or less), a decrease in an image density more easily occurs.
In contrast, the specific silica particles whose aggregation degree and the particle compression ratio satisfy the above range and which is used in the exemplary embodiment are silica particles having properties in which fluidity and dispersivity to the toner particles are high, and cohesion and adhesion to the toner particles are high.
Here, since the silica particles generally have satisfactory fluidity but have low bulk density, the silica particles have low adhesion and are hardly aggregated.
Meanwhile, for the purpose of increasing fluidity of the silica particles and dispersivity to the toner particles, a technology, in which the surface of the silica particles is surface treated by using a hydrophobizing agent, is known. According to this technology, fluidity and dispersivity to the toner particles of the silica particles are improved, but cohesion are low as it is.
Also, a technology, in which the surface of the silica particles is surface treated by using a hydrophobizing agent and silicone oil in combination, is known. According to this technology, adhesion to the toner particles is improved and cohesion are improved as well. However, reversely, fluidity and dispersivity to the toner particles tend to be decreased.
In other words, in the silica particles, it may be said that fluidity and dispersivity to the toner particles, and cohesion and adhesion to the toner particles are in an opposite relationship.
In contrast, in the specific silica particles, as described above, if the compression aggregation degree and the particle compression ratio are within the above range, four properties, which are fluidity, dispersivity to the toner particles, cohesion, and adhesion to the toner particles become satisfactory.
Next, significance of setting the compression aggregation degree and the particle compression ratio of the specific silica particles within the above range will be described in an order.
First, significance of setting the compression aggregation degree of the specific silica particles from 60% to 95% will be described.
The compression aggregation degree is an index indicating cohesion and adhesion to the toner particles of the silica particles. This index indicates a degree in which how difficult the molded article is loosened when the molded article of the silica particles is made to be dropped, after a molded article of the silica particles is obtained by compressing the silica particles.
Accordingly, as the compression aggregation degree is higher, the bulky density of the silica particles is easily increased and a cohesive force (an intermolecular power) tends to be strengthened, and an adhesive power to the toner particles tends to be strengthened. In addition, a method for calculating the compression aggregation degree will be specifically described below.
Therefore, if the compression aggregation degree is from 60% to 95%, the highly controlled specific silica particles have satisfactory adhesion to the toner particles and cohesion. The upper limit of compression aggregation degree is 95%, from a viewpoint of securing fluidity and dispersivity to the toner particles, while adhesion to the toner particles and cohesion are maintained satisfactorily.
Next, significance of setting the particle compression ratio of the specific silica particles from 0.20 to 0.40 will be described.
The particle compression ratio is an index indicating fluidity of the silica particles. Specifically, the particle compression ratio is indicated by the ratio of a difference between a packed apparent specific gravity and an aerated apparent specific gravity of the silica particles to the packed apparent specific gravity ((packed apparent specific gravity−aerated apparent specific gravity)/packed apparent specific gravity).
Accordingly, as the particle compression ratio is lower, the silica particles have high fluidity. If fluidity is high, dispersivity to the toner particles tends to be increased. In addition, a method for calculating the particle compression ratio will be specifically described below.
Therefore, the specific silica particles whose particle compression ratio is controlled to be low, which is from 0.20 to 0.40, have satisfactory fluidity and dispersivity to the toner particles. However, the lower limit of the particle compression ratio is 0.20, from a viewpoint of improving adhesion to the toner particles and cohesion, while fluidity and dispersivity to the toner particles are maintained satisfactorily.
From the above, the specific silica particles have particular properties such as fluidity, dispersivity to the toner particles, a cohesive force, and an adhesive power to the toner particles. Therefore, the specific silica particles whose compression aggregation degree and the particle compression ratio satisfy the above range are the silica particles having high fluidity and dispersivity to the toner particles, and high cohesion and adhesion to the toner particles.
Next, a presumable action when the specific silica particles are added to the toner particles will be described.
First, since the specific silica particles have high fluidity and dispersivity to the toner particles, if the specific silica particles are added to the toner particles, the specific silica particles are easily attached to the surface of the toner particles almost uniformly. Since the specific silica particles attached to the toner particles have high adhesion to the toner particles, the specific silica particles are hardly flaked from the toner particles by the mechanical load caused by stirring within the a developing unit. As a result, the silica particles flaked to the carrier whose surface roughness Ra and circularity are within the above range are less attached and accumulation of the silica particles on the surface of the carrier is reduced. In addition, an increase in carrier resistance caused by prevention of the conductive path on the surface of the carrier by the silica particles is prevented.
In addition, even in a case where the specific silica particles are flaked from the toner particles and attached to the surface of the carrier whose surface roughness Ra and circularity are above range, high cohesion are exhibited on the surface of the carrier, and the particles are aggregated easily to be an aggregate. Thus, the particles are easily removed from the surface of the carrier. Therefore, the silica particles attached to the surface of the carrier are hardly kept on the surface of the carrier as it is, and accumulation of the silica particles on the surface of the carrier is reduced as well. In addition, an increase in carrier resistance caused by prevention of the conductive path on the surface of the carrier by the silica particles is prevented.
From the above, it is presumed that the developer according to the exemplary embodiment may prevent a decrease in an image density.
In the developer according to the exemplary embodiment, the particle dispersion degree of the specific silica particles is preferably from 90% to 100%.
Here, significance of setting the particle dispersion degree of the specific silica particles from 90% to 100% will be described.
The particle dispersion degree is an index indicating dispersivity of the silica particles. This index indicates a degree in which how easy the silica particles in the primary particle state are dispersed to the toner particles. Specifically, when a calculated coverage of the surface of the toner particles by the silica particles is set to C0 and an actually measured coverage is set to C, the particle dispersion degree indicates the ratio (actually measured coverage C/calculated coverage C0) of the calculate coverage C0 to the actually measured coverage C of the attachment target.
Accordingly, as the particle dispersion degree is higher, the silica particles are hardly aggregated on the surface of the toner particles and easily dispersed in the toner particles in a primary particle state. In addition, a method for calculating the particle dispersion degree will be specifically described below.
By controlling the particle dispersion degree to high, which is from 90% to 100%, while the compression aggregation degree and the particle compression ratio are controlled within the above range, the specific silica particles have further satisfactory dispersivity to the toner particles. By doing this, fluidity of the toner particles themselves is increased, and the high fluidity is maintained easily. As a result, further, the specific silica particles are easily attached to the surface of the toner particles almost uniformly and are hardly flaked from the toner particles, and the attachment of the silica particles flaked to the carrier whose surface roughness Ra and circularity are within the above range is reduced.
In the developer according to the exemplary embodiment, as the specific silica particles having high fluidity and dispersivity to the toner particles and high cohesion and adhesion to the toner particles, as described above, silica particles having a siloxane compound with a relatively high weight average molecular weight attached to the surface are preferably exemplified. Specifically, silica particles having the siloxane compound with viscosity from 1,000 cSt to 50,000 cSt attached to the surface (preferably attached in the surface attachment amount from 0.01% by weight to 5% by weight) are preferably exemplified. The specific silica particles are obtained by a method for surface treating the surface of the silica particles using, for example, a siloxane compound whose viscosity is from 1,000 cSt to 50,000 cSt, such that the surface attachment amount is from 0.01% by weight to 5% by weight.
Here, the surface attachment amount is based on the ratio to the silica particles (untreated silica particles) before the surface of the silica particles are surface treated. In below, the silica particles before surface treatment (in other words, untreated silica particles) are simply referred to as “silica particles”.
In the specific silica particles in which the surface of the silica particles are surface treated using a siloxane compound whose viscosity is from 1,000 cSt to 50,000 cSt, such that the surface attachment amount is from 0.01% by weight to 5% by weight, fluidity and dispersivity to the toner particles, and cohesion and adhesion to the toner particles are increased, and it is easy for the compression aggregation degree and the particle compression ratio to satisfy the above requirement. Also, a decrease in an image density is easily prevented. The reason for th not clear but it is considered that this is because of the following reasons.
If a siloxane compound having a relatively great viscosity, in which the viscosity is within the above range, is attached to the surface of the silica particles in a small amount of the above range, a function derived from the properties of the siloxane compound on the surface of the silica particles is exhibited. The mechanism thereof is not clear, but when the silica particles flow, since the siloxane compound having a relatively great viscosity is attached in a small amount of the above range, releasing properties derived from the siloxane compound are easily exhibited, or adhesion between the silica particles is reduced due to reduction of an interparticle force caused by steric hindrance of the siloxane compound. Due to the above, fluidity and dispersivity to the toner particles of the silica particles are further increased.
Meanwhile, when pressure is applied to the silica particles, long molecular chains of the siloxane compound on the surface of the silica particles are entangled, closely-packing properties of the silica particles are increased, and aggregation between the silica particles is strengthened. In addition, it is considered that the cohesive force of the silica particles caused by entanglement of the long molecular chains of the siloxane compound is loosened if the silica particles are made to flow. In addition to this, the adhesive power to the toner particles is also increased due to the long molecular chains of the siloxane compound on the surface of the silica particles.
From the above, in the specific silica particles in which the siloxane compound having viscosity of the above range is attached to the surface of the silica particles in a small amount of the above range, the compression aggregation degree and the particle compression ratio easily satisfy the above requirement, and the particle dispersion degree also easily satisfies the above requirement.
Hereinafter, the configuration of the developer will be described in detail.
Toner
Toner Particles
The toner particles are configured to include, for example, a binder resin, if necessary, a coloring agent, and a release agent, other additives.
Binder Resin
Examples of the binder resin include a vinyl resin including a homopolymer of a monomer such as styrenes (for example, styrene, parachlorostyrene, α-methyl styrene, or the like), (meth)acrylates (for example, methyl acrylate, ethyl acrylate, n-propyl acrylate, n-butyl acrylate, lauryl acrylate, 2-ethylhexyl acrylate, methyl methacrylate, ethyl methacrylate, n-propyl methacrylate, lauryl methacrylate, 2-ethylhexyl methacrylate, or the like), ethylenically unsaturated nitriles (for example, acrylonitrile, methacrylonitrile, or the like), vinylethers (for example, vinyl methyl ether, vinyl isobutyl ether, or the like), vinyl ketones (vinyl methyl ketone, vinyl ethyl ketone, vinyl isopropenyl ketone, or the like), and olefins (for example, ethylene, propylene, butadiene, or the like); or a copolymer where two or more types of the monomer are combined.
Examples of the binder resin include a nonvinyl resin such as an epoxy resin, a polyester resin, a polyurethane resin, a polyamide resin, a cellulose resin, a polyether resin, and a modified rosin, a mixture of these and the vinyl resin, or a graft polymer obtained by polymerizing the vinyl monomer in the presence of these resins.
The one type of the binder resin may be used alone or two or more types thereof may be used in combination.
A polyester resin is preferable as the binder resin.
Examples of the polyester resin include well-known polyester resins.
Examples of the polyester resin include a polycondensate of polyvalent carboxylic acid and polyalcohol. In addition, a commercially available product may be used or a synthesized resin may be used as the polyester resin.
Examples of the polyvalent carboxylic acid include aliphatic dicarboxylic acid (for example, oxalic acid, malonic acid, maleic acid, fumaric acid, citraconic acid, itaconic acid, glutaconic acid, succinic acid, alkenyl succinic acid, adipic acid, sebacic acid, or the like), alicyclic dicarboxylic acid (for example, cyclohexane dicarboxylic acid, or the like), aromatic dicarboxylic acid (for example, terephthalic acid, isophthalic acid, phthalic acid, naphthalene dicarboxylic acid, or the like), anhydrides thereof, or lower (for example, having 1 to 5 carbon atoms) alkyl ester thereof. Among these, for example, aromatic dicarboxylic acid is preferable as the polyvalent carboxylic acid.
As the polyvalent carboxylic acid, trivalent or higher carboxylic acid having a crosslinking structure or a branched structure may be used in combination with dicarboxylic acid. Examples of the trivalent or higher carboxylic acid include trimellitic acid, pyromellitic acid, anhydrides thereof, or lower (for example, having 1 to 5 carbon atoms) alkyl ester.
The one type of the polyvalent carboxylic acid may be used alone or two or more types thereof may be used in combination.
Examples of the polyalcohol include aliphatic diol (for example, ethylene glycol, diethylene glycol, triethylene glycol, propylene glycol, butanediol, hexanediol, neopentyl glycol, or the like), alicyclic diol (for example, cyclohexane diol, cyclohexane dimethanol, hydrogenated bisphenol A, or the like), aromatic diol (for example, an ethylene oxide adduct of bisphenol A, a propylene oxide adduct of bisphenol A, or the like). Among these, for example, aromatic diol and alicyclic diol are preferable, and aromatic diol is more preferable as the polyalcohol.
As the polyalcohol, trivalent or higher polyalcohol having a crosslinking structure or a branched structure may be used in combination with diol. Examples of the trivalent or higher polyalcohol include glycerin, trimethylolpropane, and pentaerythritol.
The one type of the polyalcohol may be used alone or two or more types thereof may be used in combination.
The glass transition temperature (Tg) of the polyester resin is preferably from 50° C. to 80° C., and more preferably from 50° C. to 65° C.
In addition, the glass transition temperature is obtained by a DSC curve obtained by a differential scanning calorimeter (DSC) and, more specifically, is obtained from an “extrapolation glass transition start temperature” described in the method for obtaining a glass transition temperature of the JISK7121-1987 “method for measuring a plastic transition temperature”.
The weight average molecular weight (Mw) of the polyester resin is preferably from 5,000 to 1,000,000, and more preferably from 7,000 to 500,000.
The number average molecular weight (Mn) of the polyester resin is preferably from 2,000 to 100,000.
The molecular weight distribution Mw/Mn of the polyester resin is preferably from 1.5 to 100, and more preferably from 2 to 60.
In addition, the weight average molecular weight and the number average molecular weight are measured by gel permeation chromatography (GPC). The molecular weight measurement by GPC is performed by using GPC•HLC-8120GPC manufactured by TOSHO CORPORATION as a measuring apparatus, Column•TSKgel Super HM-M (15 cm) manufactured by TOSHO CORPORATION, and a THF solvent. The weight average molecular weight and the number average molecular weight are calculated by using a molecular weight calibration curve created by a monodispersed polystyrene standard sample from the measurement result.
The polyester resin is obtained by the well-known preparing method. Specifically, the polyester resin is obtained, for example, by a method in which the polymerization temperature is set to 180° C. to 230° C., and the pressure within a reaction system is decreased if necessary to perform a reaction, while water or alcohol generated at the time of condensation is removed.
In addition, in a case where a raw material monomer is not dissolved or compatible under the reaction temperature, a solvent having a high boiling point may be added as a solubilizing agent to cause the monomer to be dissolved. In this case, a polycondensation reaction is performed while the solubilizing agent is distilled. In a case where a monomer having low compatibility exists, the major component may be polycondensed, after the monomer having low compatibility and acid or alcohol to be polycondensed with this monomer are condensed.
The content of the binder resin is, for example, preferably from 40% by weight to 95% by weight, more preferably from 50% by weight to 90% by weight, and still more preferably from 60% by weight to 85% by weight, with respect to the total toner particles.
Coloring Agent
Examples of the coloring agent include various pigments such as Carbon Black, Chrome Yellow, Hansa Yellow, Benzidine Yellow, Threne Yellow, Quinolone Yellow, Pigment Yellow, Permanent Orange GTR, Pyrazolone Orange, Vulcan Orange, Watch Young Red, Permanent Red, Brilliant Carmine 3B, Brilliant Carmine 6B, Dupont Oil Red, Pyrazolone Red, Lithol Red, Rhodamine B Lake, Lake Red C, Pigment Red, Rose Bengal, Aniline Blue, Ultra Marine Blue, Calco Oil Blue, Methylene Blue Chloride, Phthalocyanine Blue, Pigment Blue, Phthalocyanine Green, and Malachite Green Oxalate; and various dyes such as an acridine dye, a xanthene dye, an azo dye, a benzoquinone dye, an azine dye, an anthraquinone dye, a thioindigo dye, a dioxazine dye, a thiazine dye, an azomethine dye, an indigo dye, a phthalocyanine dye, an aniline black dye, polymethine dye, a triphenylmethane dye, a diphenylmethane dye, and a thiazole dye.
The one type of the coloring agent may be used alone or two or more types thereof may be used in combination.
As the coloring agent, a coloring agent which is surface treated, if necessary, may be used, and the coloring agent may be used in combination with a dispersant. Also, plural types of the coloring agents may be used in combination.
The content of the coloring agent is, for example, preferably from 1% by weight to 30% by weight and more preferably from 3% by weight to 15% by weight, with respect to the total toner particles.
Release Agent
Examples of the release agent include hydrocarbon wax; natural wax such as carnauba wax, rice wax, and candelilla wax; synthesized or mineral•petroleum wax such as montan wax; and ester wax such as fatty acid ester and montanic acid ester. The release agent is not limited to these.
The melting temperature of the release agent is preferably from 50° C. to 110° C. and more preferably from 60° C. to 100° C.
In addition, the melting temperature is obtained from an “melting peak temperature” described in the method for obtaining a melting temperature of the JISK7121-1987 “method for measuring a plastic transition temperature”, from the DSC curve obtained by the differential scanning calorimeter (DSC).
The content of the release agent is, for example, preferably from 1% by weight to 20% by weight and more preferably from 5% by weight to 15% by weight, with respect to the total toner particles.
Other Additives
Examples of the other additives include the well-known additives such as a magnetic member, a charge-controlling agent, and an inorganic powder. These additives are included in the toner particles as an internal additive.
Properties of Toner Particles
The toner particles may be toner particles having a single-layer structure, and toner particles having a so-called core•shell structure configured by a core (core particles) and a coating layer (a shell layer) coating the core.
Here, the toner particles having a core•shell structure may be configured to include, for example, a core including other additives such as a binder resin, if necessary, a coloring agent, and a release agent and a coating layer including a binder resin.
The volume average particle diameter (D50v) of the toner particles is preferably from 2 μm to 10 μm and more preferably from 4 μm to 8 μm.
In addition, various average particle diameters, and various particle diameter distribution indices of the toner particles are measured by using a COULTER MULTISIZER II (manufactured by Beckman Coulter, Inc.) and ISOTON-II (manufactured by Beckman Coulter, Inc.) as an electrolyte.
At the time of measuring, a 0.5 mg to 50 mg of measurement sample is added to a 2 ml of 5% aqueous solution of a surfactant (sodium alkyl benzene sulfonate is preferable) as a dispersant. This is added to a 100 ml to 150 ml of electrolyte.
An electrolyte in which the sample is suspended is dispersed by an ultrasonic disperser for 1 minute, and particle diameter distribution of the particles having a particle diameter in a range from 2 μm to 60 μm is measured using an aperture with an aperture diameter of 100 μm, by a COULTER MULTISIZER II. Also, the number of particles for sampling is 50,000.
The cumulative distributions of the volume and the number are respectively drawn from a small diameter side with respect to the divided particle diameter range (channel) based on the measured particle diameter distribution. The particle diameter as cumulative 16% is defined as a volume particle diameter D16v and a number particle diameter D16p, the particle diameter as cumulative 50% is defined as a volume average particle diameter D50v and an cumulative number average particle diameter D50p, and the particle diameter as cumulative 84% is defined as a volume particle diameter D84v and a number particle diameter D84p.
By using these, the volume particle diameter distribution index (GSDv) is calculated as (D84v/D16v)1/2, the number particle diameter distribution index (GSDp) is calculated as (D84p/D16p)1/2.
The shape factor SF1 of the toner particles is preferably from 110 to 150 and more preferably from 120 to 140.
In addition, the shape factor SF1 is obtained according to the following equation.
SF1=(ML2/A)×(π/4)×100 Equation:
In the equation, ML represents an absolute maximum length of the toner, and A represents a projected area of the toner, respectively.
Specifically, the shape factor SF1 is digitized by analyzing a microscope image or a SEM (Scanning Electron Microscope) image using an image analyzer, and calculated as follows. In other words, the shape factor SF1 is obtained as follows: an optical microscope image of the particles distributed on a slide glass surface is taken in the LUZEX image analyzer using a video camera; the maximum length and the projected area of the 100 particles are obtained and calculated according to the above equation; and the average value thereof are obtained.
External Additive
The external additive in the toner includes the specific silica particles. The external additive may include other external additives other than the specific silica particles. In other words, only the specific silica particles are added to the toner particles or other external additives and the specific silica particles may be added to the toner particles.
Specific Silica Particles
Compression Aggregation Degree
The compression aggregation degree of the specific silica particles is from 60% to 95%, but the compression aggregation degree is preferably from 65% to 95% and more preferably from 70% to 95%, from a viewpoint of securing fluidity and dispersivity to the toner particles (in particular, from a viewpoint of preventing a decrease in an image density), while cohesion and adhesion to the toner particles are maintained satisfactorily in the specific silica particles.
The compression aggregation degree is calculated by the method shown below.
A disk-shaped mold having a diameter of 6 cm is filled with 6.0 g of the specific silica particles. Next, the mold is compressed under a pressure of 5.0 t/cm2 for 60 seconds using a compression molding machine (manufactured by Maekawa Testing Machine MFG. Co., LTD.) to obtain a compressed disk-shaped molded article of the specific silica particles (hereinafter, referred to as a “molded article before dropping”). After that, the weight of the molded article before dropping is measured.
Subsequently, the molded article before dropping is disposed on a classifying screen having an aperture of 600 μm, and the molded article before dropping is made to drop under vibration amplitude of 1 mm and vibration time of 1 minute by a vibrating classifier (manufactured by TSUTSUI SCIENTIFIC INSTRUMENTS CO., LTD.: Product No. VIBRATING MVB-1). By doing this, the specific silica particles are dropped from the molded article before dropping via the classifying screen, a molded article of the specific silica particles remains on the classifying screen. After that, the weight of the molded article of the remaining specific silica particles (hereinafter, referred to as a “molded article after dropping”) is measured.
Then, the compression aggregation degree is calculated from the ratio of the weight of the molded article after dropping to the weight of the molded article before dropping using the following Equation (1).
Compression aggregation degree=(weight of the molded article after dropping/weight of the molded article before dropping)×100 Equation (1):
Particle Compression Ratio
The particle compression ratio of the specific silica particles is from 0.20 to 0.40, but the particle compression ratio is preferably from 0.24 to 0.38 and more preferably from 0.28 to 0.36, from a viewpoint of securing fluidity and dispersivity to the toner particles (in particular, from a viewpoint of preventing a decrease in an image density), while cohesion and adhesion to the toner particles are maintained satisfactorily in the specific silica particles.
The particle compression ratio is calculated by the method shown below.
The aerated apparent specific gravity and packed apparent specific gravity of the silica particles are measured by using a powder tester (manufactured by Hosokawa Micro Group., Product No. PT-S type). Then, the particle compression ratio is calculated from the ratio of the difference between the packed apparent specific gravity and the aerated apparent specific gravity of the silica particles to the packed apparent specific gravity using the following Equation (2).
Particle compression ratio=(packed apparent specific gravity−aerated apparent specific gravity)/packed apparent specific gravity Equation (2):
In addition, the “aerated apparent specific gravity” is a measured value obtained by filling a container with a capacity of 100 cm3 with the silica particles and weighing the particles, and refers to a filling specific gravity in a state where the specific silica particles are made to naturally fall in the container. The “packed apparent specific gravity” refers to an apparent specific gravity in which the container is deaerated from the aerated apparent specific gravity state, by repetitively imparting shock (tapping) to the bottom of the container 180 times, at a slide stroke of 18 mm and a tapping speed of 50 times/min, and the specific silica particles are rearranged and fill the container more densely.
Particle Dispersion Degree
The particle dispersion degree of the specific silica particles is preferably from 90% to 100%, more preferably from 95% to 100% and still more preferably 100%, from a viewpoint of obtaining more satisfactory dispersivity to the toner particles (in particular, from a viewpoint of preventing a decrease in an image density).
The particle dispersion degree is the ratio of the actually measured coverage C to the toner particles to the calculated coverage C0 and calculated by the following Equation (3).
Particle dispersion degree=actually measured coverage C/calculated coverage C0 Equation (3):
Here, when the volume average particle diameter of the toner particles is set to dt (m), the average equivalent circle diameter of the specific silica particles is set to da (m), the specific gravity of the toner particles is set to ρt, the specific gravity of the specific silica particles is set to ρa, the weight of the toner particles is set to Wt (kg), and the addition amount of the specific silica particles is set to Wa (kg), the calculated coverage C0 to the surface of the toner particles using the specific silica particles may be calculated by the following Equation (3-1).
Calculated coverage C0=√3/(2π)×(ρt/ρa)×(dt/da)×(Wa/Wt)×100(%) Equation (3-1):
A signal intensity of a silicon atom derived from the specific silica particles is measured respectively, with respect to the only toner particles, the only specific silica particles, and the toner particles coated (attached) with the specific silica particles using XPS (X-ray Photoelectron Spectroscopy) (“JPS-9000 MX”: manufactured by JOEL Ltd.), and the results may be calculated by the following Equation (3-2) to obtain the actually measured coverage C to the surface of the toner particles using the specific silica particles.
Actually measured coverage C=(z−x)/(y−x)×100(%) Equation (3-2):
(In Equation (3-2), x represents a signal intensity of a silicon atom derived from specific silica particles of the only toner particles. y represents a signal intensity of a silicon atom derived from specific silica particles of the only specific silica particles. z represents a signal intensity of a silicon atom derived from specific silica particles of the toner particles coated (attached) with the specific silica particles.)
Average Equivalent Circle Diameter
The average equivalent circle diameter of the specific silica particles is preferably from 40 nm to 200 nm, more preferably from 50 nm to 180 nm, and still more preferably from 60 nm to 160 nm, from a viewpoint of obtaining satisfactory fluidity, dispersivity to the toner particles, cohesion, and adhesion to the toner particles of the specific silica particles (in particular, from a viewpoint of preventing a decrease in an image density).
The average equivalent circle diameter D50 of the specific silica particles is obtained as follows: primary particles after the specific silica particles are added to the toner particles are observed by SEM (Scanning Electron Microscope) (manufactured by Hitachi, Ltd.: S-4100) to capture an image; the image is taken in the image analyzer (LUZEXIII, manufactured by NIRECO.); the area of each particle is measured by image analysis of the primary particles; the equivalent circle diameter of the specific silica particles is calculated from this area value; and 50% diameter (D50) in the cumulative frequency of the volume basis of the obtained equivalent circle diameter is regarded as the average equivalent circle diameter D50 of the specific silica particles. In addition, the magnification of the electron microscope is adjusted such that from about 10 to 50 of the specific silica particles are captured within one view, and the equivalent circle diameter of the primary particles is obtained by combining the view with plural views observed.
Average Circularity
The shape of the specific silica particles may be either spherical or variant, but the average circularity of the specific silica particles is preferably from 0.85 to 0.98, more preferably from 0.90 to 0.98, and still more preferably from 0.93 to 0.98, from a viewpoint of obtaining satisfactory fluidity, dispersivity to the toner particles, cohesion, and adhesion to the toner particles in the specific silica particles (in particular, from a viewpoint of preventing a decrease in an image density).
The average circularity of the specific silica particles is measured by the method shown below.
First, the circularity of the specific silica particles are obtained as follows: primary particles after the silica particles are added to the toner particles are observed by a Scanning Electron Microscope; and the circularity is obtained as “100/SF2” calculated from the following equation from the obtained plane image analysis of the primary particles.
Circularity(100/SF2)=4π×(A/I2) Equation:
[In the equation, I represents a circumference length of the primary particles on the image, and A represents a projected area of the primary particles.]
In addition, the average circularity of the specific silica particles is obtained as 50% circularity in the cumulative frequency of the circularity of 100 primary particles obtained from the plane image analysis.
Here, a method for measuring respective properties (compression aggregation degree, particle compression ratio, particle dispersion degree, and average circularity) of the specific silica particles from the toner will be described.
First, the external additive (specific silica particles) is separated from the toner as follows.
After the toner is put into methanol, dispersed, and stirred, by treating the toner in an ultrasonic bath, the external additive may be separated from the toner. The particle diameter•specific gravity of the external additive determines easiness of separating the external additive from the toner, and the specific silica particles may be separated by adjusting the condition of the ultrasonic treatment. The toner particles are precipitated by centrifugation to collect only methanol having the external additive dispersed therein. After that, the specific silica particles may be extracted by volatilizing the methanol. Also, the respective properties are measured by using the separated specific silica particles.
Hereinafter, the configuration of the specific silica particles will be described in detail.
Specific Silica Particles
The specific silica particles are particles including silica (in other words, SiO2) as a major component, and the particles may be crystalline or amorphous. The specific silica particles may be particles prepared by using a silicon compound such as water glass and alkoxysilane as a raw material, or particles obtained by pulverizing quartz.
Specific examples of the specific silica particles include silica particles (hereinafter, “sol-gel silica particles”) prepared by a sol-gel method, aqueous colloidal silica particles, alcoholic silica particles, fumed silica particles obtained by a gas phase method, and molten silica particles, and among these, the sol-gel silica particles are preferable.
Surface Treatment
In order to cause the compression aggregation degree, the particle compression ratio, and the particle dispersion degree to be within the particular range, the specific silica particles are preferably surface treated by a siloxane compound.
As the surface treatment method, the surface of the silica particles are preferably surface treated in supercritical carbon dioxide, by using supercritical carbon dioxide. In addition, the surface treatment method will be described below.
Siloxane Compound
The siloxane compound is not particularly limited as long as a compound has a siloxane skeleton in a molecular structure.
Examples of the siloxane compound include silicone oil and a silicone resin. Among these, silicone oil is preferable, from a viewpoint of surface treating the surface of the silica particles in an almost uniform state.
Examples of the silicone oil include dimethyl silicone oil, methyl hydrogen silicone oil, methyl phenyl silicone oil, amino modified silicone oil, epoxy modified silicone oil, carboxyl modified silicone oil, carbinol modified silicone oil, methacryl modified silicone oil, mercapto modified silicone oil, phenol modified silicone oil, polyether modified silicone oil, methylstyryl modified silicone oil, alkyl modified silicone oil, higher fatty acid ester modified silicone oil, higher fatty acid amide modified silicone oil, and fluorine modified silicone oil. Among these, dimethyl silicone oil, methyl hydrogen silicone oil, and amino modified silicone oil are preferable.
The one type of the siloxane compound may be used alone or two or more types thereof may be used in combination.
Viscosity
The viscosity (kinetic viscosity) of the siloxane compound is preferably from 1,000 cSt to 50,000 cSt, more preferably from 2,000 cSt to 30,000 cSt, and still more preferably from 3,000 cSt to 10,000 cSt, from a viewpoint of obtaining satisfactory fluidity, dispersivity to the toner particles, cohesion, and adhesion to the toner particles in the specific silica particles (in particular, from a viewpoint of preventing a decrease in an image density).
The viscosity of the siloxane compound is obtained in the following order. Toluene is added to the specific silica particles and dispersed by an ultrasonic disperser for 30 minutes. After that, a supernatant is collected. At this time, a toluene solution of the siloxane compound having concentration of 1 g/100 ml is obtained. The specific viscosity [ηsp] (25° C.) at this time is obtained by the following Equation (A).
ηsp=(η/η0)−1 (η0:viscosity of toluene, η:viscosity of the solution) Equation (A):
Next, the specific viscosity [ηsp] is substituted into Huggins relational expression shown as the following Equation (B) to obtain intrinsic viscosity [η].
ηsp=[η]+K′[η]2 (K′: an integer of Huggins K′=0.3 (at the time when [η]=1 to 3)) Equation (B):
Next, the intrinsic viscosity [η] is substituted into A. Kolorlov equation shown as the following Equation (C) to obtain a molecular weight M.
[η]=0.215×10−4M0.65 Equation (C):
The molecular weight M is substituted in to A. J. Barry equation shown as the following Equation (D) to obtain siloxane viscosity [η].
log η=1.00+0.0123M0.5 Equation (D):
Surface Attachment Amount
The surface attachment amount of the siloxane compound to the surface of the specific silica particles is preferably from 0.01% by weight to 5% by weight, more preferably from 0.05% by weight to 3% by weight, and still more preferably from 0.10% by weight to 2% by weight, with respect to the silica particles (the silica particles before the surface treatment), from a viewpoint of obtaining satisfactory fluidity, dispersivity to the toner particles, cohesion, and adhesion to the toner particles in the specific silica particles (in particular, from a viewpoint of preventing a decrease in an image density).
The surface attachment amount is measured by the method shown below.
After 100 mg of the specific silica particles are dispersed in 1 mL of chloroform, and 1 μL of DMF (N,N-dimethyl formamide) is added thereto as an internal standard fluid, the resultant is ultrasonically treated by an ultrasonic cleaner for 30 minutes to extract a siloxane compound to a chloroform solvent. After that, hydrogen nuclear spectroscopy is measured by the JNM-AL400 type nuclear magnetic resonance (manufactured by JEOL Ltd.), the amount of the siloxane compound is obtained from the ratio of the peak area derived from the siloxane compound to the peak area derived from DMF. In addition, the surface attachment amount is obtained from the amount of the siloxane compound.
Here, the specific silica particles is surface treated by the siloxane compound having viscosity of 1,000 cSt to 50,000 cSt, and the surface attachment amount of the siloxane compound to the surface of the silica particles is preferably from 0.01% by weight to 5% by weight.
By satisfying the above requirement, it is easy to obtain the specific silica particles having satisfactory fluidity and dispersivity to the toner particles, and improved cohesion and adhesion to the toner particles.
External Addition Amount
The external addition amount of the specific silica particles (content) is preferably from 0.1% by weight to 6.0% by weight, more preferably from 0.3% by weight to 4.0% by weight, and still more preferably from 0.5% by weight to 2.5% by weight, with respect to the toner particles, from a viewpoint of preventing a decrease in an image density.
Method for Preparing Specific Silica Particles
The specific silica particles are obtained by surface treating the surface of the silica particles by the siloxane compound having viscosity of 1,000 cSt to 50,000 cSt, such that the surface attachment amount is from 0.01% by weight to 5% by weight with respect to the silica particles.
According to the method for preparing the specific silica particles, it is possible to obtain silica particles having satisfactory fluidity and dispersivity to the toner particles and improved cohesion and adhesion to the toner particles.
Examples of the surface treatment method include a method for surface treating the surface of the silica particles by the siloxane compound in supercritical carbon dioxide; and a method for surface treating the surface of the silica particles by the siloxane compound in the air.
Specific examples of the surface treatment method include a method for dissolving the siloxane compound in supercritical carbon dioxide using supercritical carbon dioxide to attach the siloxane compound to the surface of the silica particles; a method for imparting a solution including the siloxane compound and a solvent for dissolving the siloxane compound to the surface of the silica particles (for example, spray or coating) to attach the siloxane compound to the surface of the silica particles in the air; and a method in which after a solution including the siloxane compound and a solvent for dissolving the siloxane compound is added to a silica particle dispersion and kept in the air, a mixed solution of the silica particle dispersion and the solution is dried.
Among these, as the surface treatment method, a method for attaching the siloxane compound to the surface of the silica particles using supercritical carbon dioxide is preferable.
If the surface treatment is performed in supercritical carbon dioxide, the siloxane compound in supercritical carbon dioxide becomes a dissolved state. Since the supercritical carbon dioxide has properties of having low interfacial tension, it is considered that the siloxane compound in a dissolved state in supercritical carbon dioxide and the supercritical carbon dioxide are diffused to easily reach deep in the pores of the surface of the silica particles, so that the surface treatment is performed not only to the surface of the silica particles but also to the deep down of the pores by the siloxane compound.
Thus, it is considered that the silica particles having surface treated by the siloxane compound in supercritical carbon dioxide become silica particles whose surface is treated to be an almost uniform state by the siloxane compound (for example, the surface treated layer is formed in a thin film shape).
In addition, in the method for preparing the specific silica particles, the surface treatment for imparting hydrophobicity to the surface of the silica particles may be performed by using a hydrophobizing agent with the siloxane compound in supercritical carbon dioxide.
In this case, the hydrophobizing agent is in a dissolved state in supercritical carbon dioxide with the siloxane compound, it is considered that the hydrophobizing agent and the siloxane compound in a dissolved state in supercritical carbon dioxide are diffused to easily reach deep in the pores of the surface of the silica particles with the supercritical carbon dioxide, so that the surface treatment is performed not only to the surface of the silica particles but also to the deep down of the pores by the siloxane compound and the hydrophobizing agent.
As a result, in the silica particles having surface treated by the siloxane compound and the hydrophobizing agent in supercritical carbon dioxide, the surface thereof is treated to be an almost uniform state by the siloxane compound and the hydrophobizing agent and high hydrophobicity is easily imparted.
In addition, in the method for preparing the specific silica particles, supercritical carbon dioxide may be used in other preparing steps of the silica particles (for example, a solvent removing step, or the like).
In other preparing steps, examples of the method for preparing the specific silica particles using supercritical carbon dioxide include a method for preparing the silica particles including a step of preparing a silica particle dispersion containing the silica particles and a solvent including alcohol and water by a sol-gel method (hereinafter, referred to as a “dispersion preparing step); a step of removing the solvent from the silica particle dispersion causing supercritical carbon dioxide to flow (hereinafter, referred to as a “solvent removing step”); and a step of surface treating the surface of the silica particles by the siloxane compound after removing the solvent, in supercritical carbon dioxide (hereinafter, referred to as a “surface treatment step”).
If a removal of the solvent from the silica particle dispersion is performed by using supercritical carbon dioxide, it is easy to prevent occurrence of a coarse powder.
Although the reason is not clear, the reason is considered as follows: 1) in a case where the solvent of the silica particle dispersion is removed, the solvent may be removed without the particles aggregating to each other by a liquid bridge force at the time of removing the solvent, because of the properties of supercritical carbon dioxide, which is that “interfacial tension does not work”; and 2) because of the properties of supercritical carbon dioxide, which is that “supercritical carbon dioxide is carbon dioxide in a state under the temperature•pressure of the critical point or higher, and has both diffusibility of a gas and solubility of a liquid”, the solvent is dissolved by causing the solvent to contact with the supercritical carbon dioxide effectively at a relatively low temperature (for example, 250° C. or lower), the supercritical carbon dioxide having the solvent dissolved is removed, and accordingly, the solvent in the silica particle dispersion may be removed without forming a coarse powder such as a secondary aggregate due to condensation of a silanol group.
Here, the solvent removing step and the surface treatment step may be performed separately, but are preferably performed sequentially (in other words, each step is executed in a non-open state under atmospheric pressure). If each step is performed sequentially, after the solvent removing step, an opportunity of the silica particles to adsorb moisture is lost, and the surface treatment step is performed in a state where adsorption of excessive moisture to the silica particles is prevented. Due to this, it is not necessary to use the large amount of the siloxane compound or perform the solvent removing step and the surface treatment step at high temperature by excessively heating. As a result, it is easy to prevent occurrence of a coarse powder more effectively.
Hereinafter, details of the method for preparing the specific silica particles will be described for each step.
In addition, the method for preparing the specific silica particles is not limited to this and for example, may have 1) an aspect of using supercritical carbon dioxide only in the surface treatment step, or 2) an aspect of separately performing each step.
Hereinafter, each step will be described in detail.
Dispersion Preparing Step
In the dispersion preparing step, for example, a silica particle dispersion containing the silica particles and the solvent including alcohol and water is prepared.
Specifically, in the dispersion preparing step, the silica particle dispersion is prepared by for example, a wet method (for example, a sol-gel method, or the like), and this dispersion is prepared. In particular, the silica particle dispersion may be prepared by a sol-gel method, as a wet method, and specifically, it is preferable to prepare the silica particle dispersion by reacting tetraalkoxysilane (hydrolysis reaction, condensation reaction) in the solvent including alcohol and water in the presence of an alkali catalyst to form silica particles.
In addition, a preferable range of the average equivalent circle diameter and a preferable range of the average circularity of the silica particles are as described above.
In the dispersion preparing step, for example, in a case where the silica particles are obtained by a wet method, the silica particles are obtained in a state of dispersion where the silica particles are dispersed in the solvent (silica particle dispersion).
Here, when moving to the solvent removing step, in the prepared silica particle dispersion, the weight ratio of water to alcohol may be, for example, from 0.05 to 1.0, and is preferably from 0.07 to 0.5 and more preferably from 0.1 to 0.3.
In the silica particle dispersion, if the weight ratio of water to alcohol is within the above range, occurrence of a coarse powder of the silica particles after the surface treatment is less, and the silica particles having satisfactory electric resistance may be obtained easily.
If the weight ratio of water to alcohol is below 0.05, in the solvent removing step, since a silanol group on the surface of the silica particles when removing the solvent is less condensed, moisture adsorbed to the surface of the silica particles after removing the solvent becomes greater. Accordingly, electric resistance of the silica particles after the surface treatment may be excessively decreased. In addition, if the weight ratio of water exceeds 1.0, in the solvent removing step, a great amount of water may remain in the vicinity of the finishing point of the removal of the solvent in the silica particle dispersion, and the silica particles may be easily aggregated with each other by a liquid bridge force, which may be present as a coarse powder after the surface treatment.
In addition, when moving to the solvent removing step, in the prepared silica particle dispersion, the weight ratio of water to the silica particles may be, for example, from 0.02 to 3, and is preferably from 0.05 to 1 and more preferably from 0.1 to 0.5.
In the silica particle dispersion, if the weight ratio of water to silica particles is within the above range, occurrence of a coarse powder of the silica particles is less, and the silica particles having satisfactory electric resistance may be obtained easily.
If the weight ratio of water to silica particles is below 0.02, in the solvent removing step, since a silanol group on the surface of the silica particles when removing the solvent is extremely less condensed, moisture adsorbed to the surface of the silica particles after removing the solvent becomes greater. Accordingly, electric resistance of the silica particles may be excessively decreased.
In addition, if the weight ratio of water exceeds 3, in the solvent removing step, a great amount of water may remain in the vicinity of the finishing point of the removal of the solvent in the silica particle dispersion, and the silica particles may be easily aggregated with each other by a liquid bridge force.
In addition, when moving to the solvent removing step, in the prepared silica particle dispersion, the weight ratio of silica particles to the silica particle dispersion may be, for example, from 0.05 to 0.7, and is preferably from 0.2 to 0.65 and more preferably 0.3 to 0.6.
If the weight ratio of silica particles to the silica particle dispersion is below 0.05, in the solvent removing step, the amount of supercritical carbon dioxide to be used becomes greater, and productivity may be degraded.
In addition, if the weight ratio of silica particles to the silica particle dispersion exceeds 0.7, the distance between the silica particles in the silica particle dispersion may become closer, and a coarse powder may be easily formed due to aggregation or gelation of the silica particles.
Solvent Removing Step
The solvent removing step is a step for removing the solvent of the silica particle dispersion by for example, causing supercritical carbon dioxide to flow.
In other words, in the solvent removing step, supercritical carbon dioxide is caused to flow, and the supercritical carbon dioxide is caused to contact with the silica particle dispersion to remove the solvent.
Specifically, in the solvent removing step, for example, the silica particle dispersion is put into a hermetically sealed reactor. After that, liquefied carbon dioxide is added to the hermetically sealed reactor and heated, and the pressure within the reactor is increased by a high pressure pump to cause carbon dioxide to be in a supercritical state. In addition, the supercritical carbon dioxide is introduced into the hermetically sealed reactor, discharged, and made to flow within the hermetically sealed reactor, that is, the silica particle dispersion.
Due to this, the supercritical carbon dioxide dissolves the solvent (alcohol and water), which leads the solvent to be discharged to the outside of the silica particle dispersion (outside of the hermetically sealed reactor), and the solvent is removed.
Here, the supercritical carbon dioxide is carbon dioxide in a state under the temperature•pressure of the critical point or higher, and has both diffusibility of a gas and solubility of a liquid.
The temperature condition for removing the solvent, in other words, the temperature of supercritical carbon dioxide may be, for example, from 31° C. to 350° C., and is preferably from 60° C. to 300° C. and more preferably from 80° C. to 250° C.
If this temperature is less than the above range, since it is difficult for the solvent to be dissolved in supercritical carbon dioxide, the removal of the solvent may be difficult. In addition, it is considered that a coarse powder may be easily formed by a liquid bridge force of the solvent or supercritical carbon dioxide. Meanwhile, if this temperature exceeds the above range, it is considered that a coarse powder such as a secondary aggregate is easily formed by condensation of the silanol group of the surface of the silica particles.
The pressure condition for removing the solvent, in other words, the pressure of supercritical carbon dioxide may be, for example, from 7.38 MPa to 40 MPa, and is preferably from 10 MPa to 35 MPa and more preferably from 15 MPa to 25 MPa.
If this pressure is less than the above range, there is a tendency that it is difficult for the solvent to be dissolved in supercritical carbon dioxide, and meanwhile, if this pressure exceeds the above range, the cost of facility tends to be high.
In addition, the introduction•discharge amount of the supercritical carbon dioxide to the hermetically sealed reactor may be, for example, from 15.4 L/min/m3 to 1,540 L/min/m3, and is preferably from 77 L/min/m3 to 770 L/min/m3.
If this introduction•discharge amount is less than 15.4 L/min/m3, since it takes time to remove the solvent, productivity tends to be degraded.
Meanwhile, if this introduction•discharge amount is 1,540 L/min/m3 or more, supercritical carbon dioxide short-passes, a contact time with the silica particle dispersion becomes short, and there is a tendency that it is difficult to be able to remove the solvent effectively.
Surface Treatment Step
The surface treatment step is, for example, a step for surface treating the surface of the silica particles by the siloxane compound in supercritical carbon dioxide, continued from the solvent removing step.
In other words, in the surface treatment step, for example, before moving from the solvent removing step, the surface of the silica particles is surface treated by the siloxane compound in supercritical carbon dioxide, without being open to the air.
Specifically, in the surface treatment step, for example, after introduction•discharging of supercritical carbon dioxide to the hermetically sealed reactor is stopped in the solvent removing step, the pressure and temperature within the hermetically sealed reactor are adjusted, and the siloxane compound having a predetermined ratio with respect to the silica particles are put into the hermetically sealed reactor, in a state where supercritical carbon dioxide is present. Then, the siloxane compound is reacted in the state where the above state is maintained, in other words, in supercritical carbon dioxide to perform surface treatment of the silica particles.
Here, in the surface treatment step, the reaction of the siloxane compound may be performed in supercritical carbon dioxide (in other words, under the atmosphere of supercritical carbon dioxide), the surface treatment may be performed, while supercritical carbon dioxide is made to flow (in other words, supercritical carbon dioxide is made to introduce•discharge to the hermetically sealed reactor), or the surface treatment may be performed, while supercritical carbon dioxide is not made to flow.
In the surface treatment step, the amount (charged amount) of the silica particles with respect to the capacity of the reactor may be, for example, from 30 g/L to 600 g/L, and is preferably from 50 g/L to 500 g/L and more preferably from 80 g/L to 400 g/L.
If this amount is smaller than the above range, the concentration of the siloxane compound with respect to supercritical carbon dioxide may be decreased, a contact probability with the silica surface may be decreased, and the reaction may be difficult to proceed. Meanwhile, if this amount is greater than the above range, the concentration of the siloxane compound with respect to supercritical carbon dioxide may be increased, the siloxane compound may be not dissolved completely in supercritical carbon dioxide, which is a dispersion failure, and a coarse aggregate may be easily formed.
The density of supercritical carbon dioxide may be, for example, from 0.10 g/ml to 0.80 g/ml, and is preferably from 0.10 g/ml to 0.60 g/ml, and more preferably from 0.2 g/ml to 0.50 g/ml.
If this density is lower than the above range, there is a tendency that solubility of the siloxane compound with respect to supercritical carbon dioxide is decreased, and an aggregate is formed. Meanwhile, if this density is higher than the above range, since diffusibility to the silica pore is decreased, the surface treatment may be insufficient. In particular, the surface treatment may be performed within the above density range, with respect to sol-gel silica particles containing many silanol groups.
In addition, the density of supercritical carbon dioxide is adjusted by temperature and pressure.
Specific examples of the siloxane compound are as described above. In addition, the preferable range of the viscosity of the siloxane compound is as described above.
Among the siloxane compounds, if silicone oil is applied, silicone oil is easily attached to the surface of the silica particles in an almost uniform state, and fluidity, dispersivity, and handling properties of the silica particles are easily improved.
The use amount of the siloxane compound may be, for example, from 0.05% by weight to 3% by weight, and is preferably from 0.1% by weight to 2% by weight, and more preferably from 0.15% by weight to 1.5% by weight with respect to the silica particles, from a viewpoint of easily controlling the surface attachment amount to the silica particles from 0.01% by weight to 5% by weight.
In addition, the siloxane compound may be used alone, but may be used as a solution mixed with a solvent in which the siloxane compound easily dissolves. Examples of the solvent include toluene, methyl ethyl ketone, and methyl isobutyl ketone.
In the surface treatment step, the surface treatment of the silica particles may be performed by a mixture including a hydrophobizing agent with the siloxane compound.
Examples of the hydrophobizing agent include a silane hydrophobizing agent. Examples of the silane hydrophobizing agent include the well-known silicon compound having an alkyl group (for example, a methyl group, an ethyl group, a propyl group, a butyl group, or the like), and specific examples thereof include a silazane compound (for example, a silane compound such as methyl trimethoxysilane, dimethyl dimethoxysilane, trimethyl chlorosilane, and trimethyl methoxysilane, hexamethyl disilazane, tetramethyl disilazane, or the like). The one type of the hydrophobizing agent may be used alone or plural types thereof may be used.
Among the silane hydrophobizing agent, a silicon compound having a trimethyl group such as trimethyl methoxysilane and hexamethyl disilazane (HMDS), in particular, hexamethyl disilazane (HMDS) is preferable.
The use amount of the silane a hydrophobizing agent is not particularly limited. The use amount thereof may be, for example, from 1% by weight to 100% by weight, and is preferably from 3% by weight to 80% by weight and more preferably from 5% by weight to 50% by weight with respect to the silica particles.
In addition, the silane a hydrophobizing agent may be used alone, but may be used as a solution mixed with a solvent in which the silane hydrophobizing agent easily dissolves. Examples of the solvent include toluene, methyl ethyl ketone, and methyl isobutyl ketone.
The temperature condition of the surface treatment, in other words, the temperature of supercritical carbon dioxide may be, for example, from 80° C. to 300° C., and is preferably from 100° C. to 250° C. and more preferably from 120° C. to 200° C.
If this temperature is less than the above range, the surface treatment ability by the siloxane compound may be degraded. Meanwhile, if this temperature exceeds the above range, a condensation reaction proceeds between the silanol groups of the silica particles, and particle aggregation may occur. In particular, with respect to the sol-gel silica particles containing many silanol groups, the surface treatment may be performed within the above range.
Meanwhile, the pressure condition of the surface treatment, in other words, the pressure of the supercritical carbon dioxide may be a condition satisfying the density. However, the pressure thereof may be, for example, from 8 MPa to 30 MPa and is preferably from 10 MPa to 25 MPa and more preferably from 15 MPa to 20 MPa.
Via the respective steps stated above, the specific silica particles are obtained.
Other External Additives
Examples of the other external additives include inorganic particles. Examples of the inorganic particles include SiO2 (however, excluding the specific silica particles), TiO2, Al2O3, CuO, ZnO, SnO2, CeO2, Fe2O3, MgO, BaO, CaO, K2O, Na2O, ZrO2, CaO.SiO2, K2O.(TiO2)n, Al2O3.2SiO2, CaCO3, MgCO3, BaSO4, and MgSO4.
The surface of the inorganic particles as the other external additives may be subjected to treatment with a hydrophobizing agent. The treatment with a hydrophobizing agent is performed, for example, by dipping the inorganic particles in the hydrophobizing agent. The hydrophobizing agent is not particularly limited, but examples thereof include a silane coupling agent, silicone oil, a titanate coupling agent, and an aluminium coupling agent. These may be used alone or two or more types thereof may be used in combination.
The amount of the hydrophobizing agent is normally, for example, from 1 part by weight to 10 parts by weight with respect to 100 parts by weight of the inorganic particles.
Examples of other external additive include resin particles (resin particles of polystyrene, polymethyl methacrylate (PMMA), and a melamine resin), a cleaning aid (for example, a metal salt of higher fatty acid represented by zinc stearate and particles of a fluorine polymer).
The external addition amount of the other external additives is, for example, preferably from 0% by weight to 4.0% by weight and more preferably from 0.3% by weight to 2.0% by weight with respect to the toner particles.
Method for Preparing Toner
Next, the method for preparing a toner used in the exemplary embodiment will be described.
The toner used in the exemplary embodiment is obtained by adding the external additive to the toner particles, after the toner particles are prepared.
The toner particles may be prepared by either a dry preparing method (for example, a kneading and pulverizing method, or the like) or a wet preparing method (for example, an aggregating and unifying method, a suspension polymerization method, a dissolution suspension method, or the like). The preparing method of the toner particles is not particularly limited to these preparing methods, and the well-known preparing method is adopted.
Among these, the toner particles may be obtained by the aggregating and unifying method.
Specifically, for example, in a case where the toner particles are prepared by the aggregating and unifying method,
the toner particles are prepared via the following steps: a step of preparing a resin particle dispersion in which the resin particles as a binder resin are dispersed (a resin particle dispersion preparing step); a step of aggregating the resin particles (according to the necessity, other particles) in the resin particle dispersion (according to the necessity, in a dispersion after a dispersion of the other particles is mixed) to form aggregated particles (an aggregated particle forming step); and a step of heating an aggregated particle dispersion in which the aggregated particles are dispersed, and coalescing the aggregated particles to form the toner particles (a coalescing step).
Hereinafter, each step will be described in detail.
In addition, in the following description, a method for obtaining the toner particles including a coloring agent and a release agent will be described, but the coloring agent and the release agent are used according to the necessity. Certainly, other additives may be added other than the coloring agent and the release agent.
Resin Particle Dispersion Preparing Step
First, a resin particle dispersion, in which the resin particles as a binder resin are dispersed, is prepared with, for example, a coloring agent particle dispersion where the coloring agent particles are dispersed, and a release agent particle dispersion where the release agent particles are dispersed.
Here, the resin particle dispersion is prepared by, for example, dispersing the resin particles in a dispersion medium by a surfactant.
As the dispersion medium used for the resin particle dispersion, for example, an aqueous medium is exemplified.
Examples of the aqueous medium include water such as distilled water and ion exchanged water, and alcohols. The one type of the aqueous medium may be used alone or two or more types thereof may be used in combination.
Examples of the surfactant include an anionic surfactant such as a sulfate salt surfactant, a sulfonic acid salt surfactant, a phosphate ester surfactant, and a soap surfactant; a cationic surfactant such as an amine salt surfactant and a quaternary ammonium salt surfactant; and a nonionic surfactant such as polyethylene glycol surfactant, an alkyl phenol ethylene oxide adduct surfactant, and a polyalcohol surfactant. Among these, in particular, the anionic surfactant and the cationic surfactant are exemplified. The nonionic surfactant may be used in combination with the anionic surfactant or the cationic surfactant.
The one type of the surfactant may be used alone or two or more types thereof may be used in combination.
In the resin particle dispersion, examples of the method for dispersing the resin particles in the dispersion medium include a general dispersion method such as a rotary shear type homogenizer, a ball mill, a sand mill, and a dyno mill, which have a media. In addition, depending on the type of the resin particles, for example, the resin particles may be dispersed in the resin particle dispersion using a phase inversion emulsification method.
In addition, the phase inversion emulsification method refers to a method, in which a resin to be dispersed is made to be dissolved in a hydrophobic organic solvent in which the resin may be dissolved, abase is added to an organic continuous phase (O phase) to neutralize, and then an aqueous medium (W phase) is put into thereto, an exchange of the resin (a so-called phase inversion) is performed from W/O to O/W to become a noncontinuous phase, and the resin is dispersed in the aqueous medium in a particle shape.
The volume average particle diameter of the resin particles dispersed in the resin particle dispersion is, for example, preferably from 0.01 μm to 1 μm, more preferably from μm 0.08 to μm 0.8, and still more preferably from 0.1 μm to 0.6 μm.
In addition, the volume average particle diameter of the resin particles is measured in which the particle diameter distribution obtained by measurement of a laser diffraction particle diameter distribution measuring apparatus (for example, manufactured by HORIBA, Ltd., LA-700) is used, a cumulative distribution of the volume is drawn from a small particle diameter side with respect to the divided particle range (channel), and the particle diameter as cumulative 50% with respect to the total particles is measured as the volume average particle diameter D50v. Also, the volume average particle diameter of the particles in other dispersions is measured in the same manner.
The content of the resin particles included in the resin particle dispersion is, for example, preferably from 5% by weight to 50% by weight and more preferably from 10% by weight to 40% by weight.
In addition, in the same manner as the resin particle dispersion, for example, the coloring agent particle dispersion and the release agent particle dispersion are prepared. In other words, with regard to the volume average particle diameter of the particles, the dispersion medium, the dispersion method, and the content of the particles in the resin particle dispersion, the same applies to the coloring agent particles dispersed in the coloring agent particle dispersion, and the release agent particles dispersed in the release agent particle dispersion.
Aggregated Particles Forming Step
Next, the coloring agent particle dispersion and the release agent particle dispersion are mixed with the resin particle dispersion.
In addition, the aggregated particles are formed, which have the target diameter close to the diameter of the toner particles, by causing the resin particles, the coloring agent particles and the release agent particles to be hetero-aggregated in the mixed dispersion, and include the resin particles, the coloring agent particles, and the release agent particles.
Specifically, for example, an aggregating agent is added to a mixed dispersion, the pH of the mixed dispersion is adjusted to be acidic (for example, pH is from 2 to 5), a dispersion stabilizer is added thereto according to the necessity, and then the resin particles are heated up to the glass transition temperature (specifically, for example, glass transition temperature of the resin particles −30° C. or higher, glass transition temperature −10° C. or lower), and the particles dispersed in the mixed dispersion are aggregated to form the aggregated particles.
In the aggregated particles forming step, for example, after the mixed dispersion is stirred by the rotary shear type homogenizer, the aggregating agent is added thereto at room temperature (for example, 25° C.), the pH of the mixed dispersion is adjusted to be acidic (for example, pH is from 2 to 5), the dispersion stabilizer is added thereto according to the necessity, and then the heating may be performed.
Examples of the aggregating agent include a surfactant having reverse polarity to the surfactant used as the dispersant added in the mixed dispersion, an inorganic metal salt, and a divalent or higher metal complex. In particular, in a case where the metal complex is used as the aggregating agent, the use amount of the surfactant is reduced and charging properties are improved.
An additive having a complex or a similar bonding to the metal ion of the aggregating agent may be used according to the necessity. As the additive, a chelating agent is preferably used.
Examples of the inorganic metal salt include a metal salt such as calcium chloride, calcium nitrate, barium chloride, magnesium chloride, zinc chloride, aluminium chloride, and aluminium sulfate; and an inorganic metal salt copolymer such as polyaluminum chloride, polyaluminium hydroxide, and calcium polysulfide.
As the chelating agent, a water-soluble chelating agent may be used. Examples of the chelating agent include oxycarboxylic acid such as tartaric acid, citric acid, and gluconic acid, iminodiacetic acid (IDA), nitrilotriacetic acid (NTA), ethylenediaminetetraacetic acid (EDTA).
The addition amount of the chelating agent is, for example, preferably from 0.01 parts by weight to 5.0 parts by weight and more preferably from 0.1 parts by weight to less than 3.0 parts by weight with respect to 100 parts by weight of the resin particles.
Coalescing Step
Next, an aggregated particle dispersion having the aggregated particles dispersed therein is heated, for example, up to the glass transition temperature of the resin particles (for example, equal to or higher than the temperature from 10° C. to 30° C. higher than the glass transition temperature of the resin particles), and the aggregated particles are coalesced to form the toner particles.
Via the above steps, the toner particles are obtained.
In addition, the toner particles may be prepared via the following steps: a step of forming second aggregated particles in which after the aggregated particle dispersion having the aggregated particles dispersed therein is obtained, the aggregated particle dispersion and the resin particle dispersion having the resin particles dispersed therein are further mixed to each other so as to aggregate such that the resin particles are further attached to the surface of the aggregated particles; and a step of forming the toner particles having a core/shell structure in which a second aggregated particle dispersion having the second aggregated particles dispersed therein is heated to coalesce the second aggregated particles.
Here, after the coalescing step is finished, the toner particles formed in the solution is subjected to a well-known cleansing step, a solid liquid separating step, and a drying step to obtain the toner particles in a dried state.
As the cleansing step, it is preferable to sufficiently perform displacement cleansing using ion exchanged water from a viewpoint of charging properties. In addition, the solid liquid separating step is not particularly limited, but it is preferable to perform a suction filtration, a pressurization filtration, or the like from a viewpoint of productivity. In addition, the drying step is not particularly limited, but it is preferable to perform freeze drying, flash drying, fluidized drying, vibrating fluidized drying, or the like, from a viewpoint of productivity.
In addition, the toner used in the exemplary embodiment is prepared by for example, adding an external additive to the obtained dried toner particles and mixing the particles. It is preferable to perform mixing by for example, V blender, HENSCHEL MIXER, LOEDIGE MIXER, or the like. Further, coarse particles may be removed by using a vibrating classifier, wind classifier, or the like, if necessary.
Carrier
The carrier used in the exemplary embodiment includes a core particle and a resin coated layer which covers the surface of the core particle, and has a surface roughness Ra (based on JIS-B0601) of 0.5 μm or less and a circularity of 0.975 or more.
Specific examples of the carrier include the carrier (packed carrier) shown in the following. In the packed carrier, a raw material for core particles is finely pulverized before baking according to the method in the related art, the packing ratio within the core particles of the raw material is increased, and the temperature is increased in an almost uniform state at the time of baking, so as to cause the surface to be uniform. Further, by finely pulverizing and dispersing the raw material and increasing the temperature in an almost uniform state, crystal growth is controlled. Thus, the above core particles are obtained. As a method for increasing the temperature in an almost uniform state, a method of using a rotary furnace is exemplified.
As the core particles, any particles known in the related art may be used, but particularly preferably, ferrite or magnetite is selected. As other core particles, for example, iron powder is known. Ferrite or magnetite is excellent in stability from a viewpoint of toner deterioration. An example of ferrite is generally represented by the following formula.
(MO)X(Fe2O3)Y
(In the formula, M includes at least one selected from Cu, Zn, Fe, Mg, Mn, Ca, Li, Ti, Ni, Sn, Sr, Al, Ba, Co, and Mo, and X and Y indicate a weight mol ratio, which satisfy the condition of X+Y=100.)
M is preferably ferrite particles which are obtained by combining one or two or more of Li, Mg, Ca, Mn, Sr, and Sn and which have the content of a component other than the above of 1% by weight or less. Examples of the magnetic particles contained in the magnetic particle dispersing type resin core to be used include ferromagnetic iron oxide particle powder such as magnetite and maghemite, spinel ferrite particle powder containing one or more metals (Mn, Ni, Zn, Mg, Cu, or the like) other than iron, a magnetoplumbite type ferrite particle powder such as barium ferrite, and a particle powder of iron or an iron alloy having an oxide film on the surface.
Specific examples of the core particles include iron oxides such as magnetite, γ iron oxide, Mn—Zn ferrite, Ni—Zn ferrite, Mn—Mg ferrite, Li ferrite, and Cu—Zn ferrite. Among these, inexpensive magnetite is more preferably used.
In a case where a ferrite core is used as core particles, as an example of the method for preparing a ferrite core, first, after each oxide is blended, pulverized by a wet ball mill for 8 hours to 10 hours, mixed, and dried, pre-baking is performed at a temperature from 800° C. to 1,000° C. for 8 hours to 10 hours using a rotary kiln. After that, a pre-baked product is dispersed in water and pulverized using a ball mill until the average particle diameter becomes 0.3 μm to 1.2 μm. This slurry is granulated and dried using a spray drier, and the slurry is kept at a temperature from 800° C. to 1,200° C. for 4 hours to 8 hours, while the oxygen concentration is controlled, for the purpose of adjusting magnetic properties and resistance. Then, the resultant is pulverized, and further classified by a desired particle diameter distribution so as to obtain a ferrite core. In addition, a rotary electric furnace is preferably used in order to cause the core surface shape to be almost uniform.
In the surface roughness of the core particles, the mean width Sm with respect to the ruggedness preferably satisfies Sm≦2.0 μm and the surface roughness Ra (based on JIS-B0601) is preferably ≧0.1 μm. By prescribing the surface roughness of the core particles as described above, the internal gap is prevented and the core particles have ruggedness only on the surface. Due to the core particles having this structure, it is easy to form a resin coated layer having high coverage, and it is possible to prevent a decrease in a charge imparting ability of the carrier. Also, a decrease in magnetic force may be improved due to the prescribed core particles, feeding properties of the obtained carrier may be improved, and a control of the concentration of a magnetic permeability type toner may be improved.
In addition, in the surface roughness of the core particles, since the mean width Sm with respect to the ruggedness is 2.0 μm or less, in the preparation of the core particles, the internal gap of the core particles are prevented, and later, a resin coated layer is easily formed. Also, since the surface roughness Ra (based on JIS-B0601) of the core particles is 0.1 μm or more, an anchor effect with respect to the resin coated layer to be coated on the surface of the core particles later is obtained, separation of the resin coated layer from the core particles is prevented at the time of using the developer, a specific gravity of the carrier particles is reduced, a desired low specific gravity is easily achieved, and a decrease in collision energy is exhibited.
Further, the surface roughness Ra (based on JIS-B0601) of the carrier with the resin coated layer formed on the surface of the core particles satisfies Ra 0.5 μm and the circularity of the carrier is 0.975 or more. Also, the core exposure percentage on the core surface is preferably 2% or less.
Due to the above, concealment of the core particle surface due to the resin coated layer is increased, and by reducing the ruggedness on the carrier surface, friction energy may be reduced, an anchor effect of the resin coated layer due to the core particles more effectively functions, and separation of the resin coated layer is improved. Furthermore, depending on the carrier shape, a charge may be effectively imparted to the toner and a stress between the carriers or within a developing device is reduced.
In a case where the surface roughness Ra (based on JIS-B0601) of the carrier surface exceeds 0.5 μm, it is easy to scrap off the toner component on the carrier surface, and further the toner component is accumulated in the nonprojection portion of the carrier to be coalesced. Thus, a so-called toner spent may occur.
In addition, circularity of the carrier is 0.975 or more. As the circularity is closer to 1, the shape becomes almost perfect spherical, and as the surface roughness is greater, an even finer ruggedness exists on the surface. Since the circularity of the core particles is 0.975 or more and the shape becomes almost perfect spherical, fluidity of the carrier may be improved, coating of the resin layer in an almost uniform state may be easy, and aggregation of the core particles may be prevented. Thus, the production yield may be improved.
In addition, the measurement of Ra is performed based on JIS-B0601. In addition, even in Examples described below, the measurement is performed.
The circularity is measured by a LPF measurement mode using FPIA-3000 (manufactured by Sysmex Corporation). In addition, at the time of the measurement, 0.03 g of the carrier is dispersed in 25% by weight of an ethylene glycol aqueous solution, the particles having a particle diameter of less than 10 μm and more than 50 μm are cut to be analyzed, and the average circularity is obtained.
In addition, the core exposure percentage on the surface of the carrier is preferably 2% or less. In a case where the core particles having ruggedness on the surface are used, the exposed portion on the core surface is frequently a projection portion. In a case where a carrier resin coated layer is separated by a stress of the developing device, the resin coated layer is separated by using the core exposed portion on the carrier surface as a nucleus. Since the exposure percentage of the core is 2% or less, portions where the resin coated layer is separated are reduced and separation of the resin coated layer due to the use for a long period of time is prevented. That is, a decrease in a carrier charging function is prevented.
Since a fine ruggedness exists on the surface of the core particles used in the carrier, a coated resin layer may be strongly fixed by an anchor effect. Thus, flaking of the coating layer from the carrier is prevented. In addition, since the surface of the core particles has the surface roughness and a protruded portion, in a case where the toner concentration is high, an electric circuit is formed on the protruded portion and a resistance value of the developer is hardly changed depending on the toner concentration.
The magnetic susceptibility σ of the core particles used in the carrier is measured by a BH tracer method using a vibration sample method (VSM) measuring device in the magnetic field of 1 kOe. The appropriate range of the magnetized value σ1000 is from 50 Am2/kg (emu/g) to 90 Am2/kg (emu/g) and preferably from 55 Am2/kg (emu/g) to 70 Am2/kg (emu/g). Since the σ1000 is 50 Am2/kg (emu/g) or more, a magnetism adsorption power to a developing member (developing roll, or the like) is increased and occurrence of an image defect due to attachment to the photoreceptor is prevented. Also, since the σ1000 is 90 Am2/kg (emu/g) or less, a magnetic brush becomes soft, the scraping strength to the photoreceptor is prevented, and occurrence of damage in the photoreceptor is prevented.
The volume average particle diameter of the core particles of the carrier is preferably from 10 μm to 100 μm and more preferably from 20 μm to 50 μm. Since the volume average particle diameter is 10 μm or more, scattering of the developer from the developing device is prevented, and since the volume average particle diameter is 100 μm or less, an image density is increased.
Here, a method for measuring the volume average particle diameter is as follows.
A particle diameter distribution is measured using a laser diffraction/scattering particle diameter distribution measuring apparatus (LS Particle Size Analyzer (manufactured by Beckman Coulter, Inc.)). The ISOTON-II (manufactured by Beckman Coulter, Inc.) is used as an electrolyte. The number of particles to be measured is 50,000.
In addition, in the measured particle diameter distribution, a cumulative distribution of the volume is drawn from a small particle diameter side with respect to the divided particle range (channel), and the particle diameter as cumulative 50% (represented by “D50v”) is defined as a “volume average particle diameter”.
The electric resistance of the carrier in which the coated resin layer is formed is preferably from 1×105 Ω·cm to 1×1014 Ω·cm and more preferably from 1×109 Ω·cm to 1×1012 Ω·cm, when the measurement electric field is 10,000 V/cm.
The charging properties of the carrier in which the coated resin layer is formed are preferably from 15 μC/g to 50 μC/g. Since the charging properties of the carrier are 15 μC/g or more, toner containment (fogging) in a non-image portion is prevented and a color image having high quality is obtained. Meanwhile, since the charging properties of the carrier are 50 μC/g or less, a sufficient image density is obtained.
If the electric resistance of the carrier in which the coated resin layer is formed is 1×105 Ω·cm or more, the movement of an electric charge on the carrier surface is prevented and an image defect such as a brush mark is prevented. Also, a deterioration of charging properties when a printer is allowed to stand in a state where the printing operation is not performed for a while is prevented, and print background fogging at an initial period (for example, the first sheet) is prevented. Since the electric resistance of the carrier in which the coated resin layer is formed is 1×1014 Ω·cm or less, a satisfactory solid image is obtained, an increase in an electric charge of the toner, which may be caused when a continuous printing is repeated plural times, is prevented, and a decrease in an image density is prevented.
The kinetic electric resistance which is measured when the carrier is in the shape of a magnetic brush is preferably from 1×10 Ω·cm to 1×109 Ω·cm and more preferably from 1×103 Ω·cm to 1×108 Ω·cm in the electric field of 104 V/cm. If the kinetic electric resistance is 1×10 Ω·cm or more, an image defect such as a brush mark is prevented. If the kinetic electric resistance is 1×108 Ω·cm or less, a satisfactory solid image is obtained. The electric field of 104V/cm is close to a developing electric field in a test device and the kinetic electric resistance is a value in this electric field.
As the above, the kinetic electric resistance when the carrier and the toner are mixed to each other is preferably in a range from 1×105 Ω·cm to 1×109 Ω·cm in the electric field of 104V/cm. In addition, since the kinetic electric resistance is 1×105 Ω·cm or more, background fogging caused by a deterioration of toner charging properties after the printer is allowed to stand after printing, or a decrease in resolution in the thickness of the line image caused by over-development is prevented. Since the kinetic electric resistance is 1×109 Ω·cm or less, a deterioration of developing properties at the end of the solid image is prevented and an image having high quality is obtained.
The kinetic electric resistance of the carrier is obtained as follows. A magnetic brush is formed by putting a 30 cm3 carrier on a developing roll (1 kOe of the magnetic field on the sleeve surface of the developing roll is generated), a plate electrode having an area of 3 cm2 is made to face the developing roll at an interval of 2.5 mm. A voltage is applied between the developing roll and the plate electrode while the the developing roll is rotated at the speed of revolution of 120 rpm, and the current flowing at this time is measured. The kinetic electric resistance is obtained using Ohm's law from the obtained current-voltage properties. In addition, at this time, it is generally known that there is a relationship of ln(I/V)∝V×½ between the applied voltage V and the current I. In addition, in a case where the kinetic electric resistance of the carrier is very low, a large amount of the current flows in the high electric field of 103 V/cm or more and the measurement may not be possible. In such a case, 3 points or more are measured in a low electric field and the previous relational expression is used to obtain the kinetic electric resistance by extrapolation to the electric field of 104 V/cm according a least-squares method.
Examples of the coating resin formed on the core particles include a polyolefin resin, for example, polyethylene and polypropylene; a polyvinyl and polyvinylidene resin, for example, polystyrene, an acryl resin, polyacrylonitrile, polyvinyl acetate, polyvinyl alcohol, polyvinyl butyral, polyvinyl chloride, polyvinyl carbazole, polyvinyl ether, and polyvinyl ketone; a vinyl chloride-vinyl acetate copolymer; a styrene-acrylic acid copolymer; a straight silicon resin including an organosiloxane bond or modified product thereof; a fluorine resin, for example, polytetrafluoroethylene, polyvinyl fluoride, polyvinylidene fluoride, polychlorotrifluoroethylene; polyester; polyurethane; polycarbonate, an amino resin, for example, an urea-formaldehyde resin; and an epoxy resin. These resins may be used alone or may be used by mixing plural resins.
The thickness of the coated resin layer is preferably from 0.1 μm to 5 μm and more preferably in a range from 0.3 μm to 3 μm. If the thickness of the coated resin layer is 0.1 μm or more, the coated resin layer is easily formed almost uniformly on the surface of the core particles and in an almost flat state. In addition, if the thickness of the coated resin layer is 5 μm or less, aggregation between the carriers is prevented and it is easy to obtain an almost uniform carrier.
Examples of a method for forming the coated resin layer on the core particles include a dip method for dipping the core particles in a solution for forming the coated resin layer, a spray method for spraying the solution for forming the coated resin layer on the surface of the core particles, a fluidized bed method for spraying the solution for forming the coated resin layer in a state where the core particles are floated by fluidized air, and a kneader coater method for mixing the core particles and the solution for forming the coated resin layer in a kneader coater to remove a solvent.
The solvent used for the solution for forming the coated resin layer is not particularly limited, as long as the solvent dissolves the coating resin, but for example, aromatic hydrocarbons such as toluene and xylene, ketones such as acetone and methyl ethyl ketone, and ethers such as tetrahydrofuran and dioxane may be used. In addition, examples of a method for dispersing a conductive powder include a sand mill, a dyno mill, and a homomixer.
The mixing ratio (weight ratio) of the toner to the carrier (toner:carrier) in the developer according to the exemplary embodiment is preferably 1:100 to 30:100 and more preferably 3:100 to 20:100.
Image Forming Apparatus/Image Forming Method
The image forming apparatus/image forming method according to the exemplary embodiment will be described.
The image forming apparatus according to the exemplary embodiment includes an image holding member; a charging unit that charges the surface of the image holding member; an electrostatic charge image forming unit that forms an electrostatic charge image on the charged surface of the image holding member; a developing unit that contains an electrostatic charge image developer and develops the electrostatic charge image formed on the surface of the image holding member by the electrostatic charge image developer as a toner image; a transferring unit that transfers the toner image formed on the surface of the image holding member to the surface of a recording medium; and a fixing unit that fixes the toner image transferred on the surface of the recording medium. In addition, the electrostatic charge image developer according to the exemplary embodiment is applied as the electrostatic charge image developer.
In the image forming apparatus according to the exemplary embodiment, an image forming method (the image forming method according to the exemplary embodiment) is executed, which includes charging a surface of an image holding member; forming an electrostatic charge image on the charged surface of the image holding member; developing the electrostatic charge image formed on the surface of the image holding member by the electrostatic charge image developer according to the exemplary embodiment as a toner image; transferring the toner image formed on the surface of the image holding member to the surface of a recording medium; and fixing the toner image transferred to the surface of the recording medium.
As the image forming apparatus according to the exemplary embodiment, the well-known image forming apparatus is applied, such as an apparatus of a direct transfer system which directly transfers a toner image formed to the surface of an image holding member to a recording medium; an apparatus of an intermediate transfer system which primarily transfers a toner image formed on the surface of an image holding member to the surface of an intermediate transfer member and secondarily transfer the toner image transferred to the surface of the intermediate transfer member to the surface of a recording medium; an apparatus which includes a cleaning unit for cleaning the surface of an image holding member after a toner image is transferred and before being charged; and an apparatus which includes an erasing unit for erasing a toner image by irradiating the surface of an image holding member with erasing light after the toner image is transferred and before being charged.
In a case of the apparatus of an intermediate transfer system, as the transferring unit, for example, a configuration is applied, which include an intermediate transfer member where a toner image on the surface is transferred; a primary transferring unit for primarily transfer a toner image formed on the surface of an image holding member to the surface of an intermediate transfer member; and a secondary transferring unit for secondarily transfer the toner image transferred to the surface of the intermediate transfer member to the surface of a recording medium.
In addition, in the image forming apparatus according to the exemplary embodiment, for example, a portion including the developing unit may have a cartridge structure (a process cartridge) detachable from the image forming apparatus. As the process cartridge, for example, a process cartridge which includes a developing unit where the electrostatic charge image developer according to the exemplary embodiment is contained.
Hereinafter, one example of the image forming apparatus according to the exemplary embodiment will be shown, but the image forming apparatus is not limited to this. Also, main parts shown in the drawing will be described and description of other parts will be omitted.
The image forming apparatus shown in
An intermediate transfer belt 20 is extensively provided as an intermediate transfer member through respective units in the above of the drawing of respective units 10Y, 10M, 10C, and 10K. The intermediate transfer belt 20 is provided by being wounded by a driving roll 22 disposed being separated to each other from a left to right direction in the drawing and a support roll 24 contacting with the inner surface of the intermediate transfer belt 20, and is configured to travel in a direction from a first unit 10Y to a fourth unit 10K. Also, a force is added to the support roll 24 in a direction separating from the driving roll 22 by a spring or the like (not illustrated), and tension is imparted to the intermediate transfer belt 20 wounded by both rolls. In addition, an intermediate transfer member cleaning device 30 facing the driving roll 22 is included on the side surface of the image holding member of the intermediate transfer belt 20.
In addition, a toner including four colors of yellow, magenta, cyan, and black contained in toner cartridges 8Y, 8M, 8C, and 8K is supplied to each developing device (a developing unit) 4Y, 4M, 4C, or 4K of each unit 10Y, 10M, 10C, or 10K.
Since the first to fourth units 10Y, 10M, 10C, and 10K have the same configuration, here, the first unit 10Y which forms a yellow image and is disposed on the upstream side in the traveling direction of the intermediate transfer belt will be representatively described. In addition, the descriptions for the second to fourth units 10M, 10C, and 10K will be omitted by attaching reference symbols of magenta (M), cyan (C), and black (K) to the same part as that of the first unit 10Y, instead of yellow (Y).
The first unit 10Y has a photoreceptor 1Y acting as an image holding member. In the periphery of the photoreceptor 1Y, a charging roll (one example of the charging unit) 2Y for charging the surface of the photoreceptor 1Y to a predetermined electric potential, an exposing device (one example of the electrostatic charge image forming unit) 3 for forming an electrostatic charge image by exposing the charged surface to a laser beam 3Y based on a color separated image signal, a developing device (one example of the developing unit) 4Y for developing the electrostatic charge image by supplying a charged toner to the electrostatic charge image, a primary transfer roll 5Y (one example of the primary transferring unit) for transferring the developed toner image to the intermediate transfer belt 20, and a photoreceptor cleaning device (one example of the cleaning unit) 6Y for removing the toner remaining on the surface of the photoreceptor 1Y after the primary transfer, are sequentially disposed.
In addition, the primary transfer roll 5Y is disposed in the inner side of the intermediate transfer belt 20, and is provided in a position facing the photoreceptor 1Y. Further, a bias power supply (not illustrated) for applying a primary transfer bias is respectively connected to the respective primary transfer rolls 5Y, 5M, 5C, and 5K. The respective bias power supplies may change the transfer bias to be applied to the respective primary transfer rolls by control of a control unit (not illustrated).
Hereinafter, an operation for forming a yellow image of the first unit 10Y will be described.
First, prior to the operation, the surface of the photoreceptor 1Y is charged to an electric potential of −600 V to −800 V by a charging roll 2Y.
The photoreceptor 1Y is formed by laminating a photosensitive layer on a conductive (for example, volume resistivity at a temperature of 20° C.: 1×10−6 Ωcm or less) base member. This photosensitive layer has commonly high resistance (in general, resistance of a resin), and if the photosensitive layer is irradiated with a laser beam 3Y, the photosensitive layer has properties in which the specific resistance of the portion having been irradiated with a laser beam is changed. In addition, the laser beam 3Y is output to the surface of the charged photoreceptor 1Y via the exposing device 3, according to image data for yellow delivered from the control unit (not illustrated). The photosensitive layer on the surface of the photoreceptor 1Y is irradiated with the laser beam 3Y and an electrostatic charge image of a yellow image pattern is formed on the surface of the photoreceptor 1Y.
The electrostatic charge image is an image formed on the surface of the photoreceptor 1Y by charging, and is a so-called negative latent image, which is formed as follows: specific resistance of a portion of the photosensitive layer to be irradiated with the laser beam 3Y is decreased, and an electric charge charged on the surface of the photoreceptor 1Y flows, but the electric charge remains on the portion not having been irradiated with the laser beam 3Y.
The electrostatic charge image formed on the photoreceptor 1Y is rotated to the predetermined developing position according to the traveling of the photoreceptor 1Y. In addition, in this developing position, the electrostatic charge image on the photoreceptor 1Y becomes a visualized image (developed image) as a toner image by the developing device 4Y.
The electrostatic charge image developer including, for example, at least the yellow toner and the carrier is contained within the developing device 4Y. The yellow toner is frictionally charged by being stirred within the developing device 4Y, and has an electric charge with the same polarity (negative polarity) as that of the electric charge charged on the photoreceptor 1Y so as to be kept on a developer roll (one example of a developer holding member). In addition, as the surface of the photoreceptor 1Y passes through the developing device 4Y, the yellow toner is electrostatically attached to a latent image portion erased on the surface of the photoreceptor 1Y, and the latent image is developed by the yellow toner. Subsequently, the photoreceptor 1Y where a yellow toner image is formed travels at a predetermined speed, and the toner image developed on the photoreceptor 1Y is fed to a predetermined primary transfer position.
Here, the developing device 4Y may be a developing device of a trickle developing system which develops an image while a part of the carrier in the contained developer is exchanged (discharge and supply). In addition, in a case where the developing device 4Y is a developing device of a trickle developing system, a configuration may be adopted in the developing device, in which a developer for supplying is supplied by connecting a developer cartridge having a developer including the yellow toner and the carrier contained therein, instead of the toner cartridge 8Y, with a developer supply tube (not illustrated).
In addition, the carrier to be discharged includes a carrier deteriorated by stirring within the developing device 4Y.
If the yellow toner image on the photoreceptor 1Y is fed to a primary transfer roll, a primary transfer bias is applied to the primary transfer roll 5Y, an electrostatic force from the photoreceptor 1Y toward the primary transfer roll 5Y acts on the toner image, and the toner image on the photoreceptor 1Y is transferred on the intermediate transfer belt 20. The transfer bias to be applied at this time has (+) polarity which is a reverse polarity to the polarity (−) of the toner, and for example, in the first unit 10Y, the bias is controlled to +10 μA by the control unit (not illustrated).
Meanwhile, the toner remaining on the photoreceptor 1Y is removed by the photoreceptor cleaning device 6Y and collected.
In addition, the primary transfer bias to be applied to the primary transfer rolls 5M, 5C, and 5K after the second unit 10M is controlled based on the first unit.
In this way, the intermediate transfer belt 20 where the yellow toner image is transferred by the first unit 10Y is sequentially fed through the second to fourth units 10M, 10C, and 10K and the toner images with respective colors are overlapped and transferred in a multiple manner.
The intermediate transfer belt 20 where four-color toner images are transferred in a multiple manner through the first to fourth units reaches a secondary transfer portion configured to include the intermediate transfer belt 20, the support roll 24 contacting with the inner surface of the intermediate transfer belt, and a secondary transfer roll (one example of the secondary transferring unit) 26 disposed on the image holding surface side of the intermediate transfer belt 20. Meanwhile, a recording sheet (one example of the recording medium) P is supplied via a supplying mechanism at a predetermined timing to the space where the secondary transfer roll 26 and the intermediate transfer belt 20 contact with each other, and the secondary transfer bias is applied to the support roll 24. The transfer bias to be applied at this time has (−) polarity which is the same polarity as the polarity (−) of the toner, the electrostatic force from the intermediate transfer belt 20 toward the recording sheet P acts on the toner image, and the toner image on the intermediate transfer belt 20 is transferred to the recording sheet P. In addition, the secondary transfer bias at this time is determined depending on resistance detected by a resistance detection unit (not illustrated) for detecting resistance of the secondary transfer portion, and voltage-controlled.
After that, the recording sheet P is fed to a nip portion of a pair of fixing rolls in a fixing device (one example of the fixing unit) 28, the toner image is fixed on the recording sheet P, and the fixed image is formed.
As the recording sheet P on which the toner image is transferred, a plain paper used for an electrophotographic copying machine, a printer, or the like is exemplified. As the recording medium, an OHP sheet is exemplified other than the recording sheet P.
In order to improve smoothness of the surface of the fixed image, the surface of the recording sheet P is preferably smooth, and for example, a coated paper in which the surface of the plain paper is coated with a resin, an art paper for printing, or the like is preferably used.
The recording sheet P in which fixing of the color image is completed is discharged to a discharging portion and an operation of forming a series of color images is finished.
Process Cartridge/Developer Cartridge
The process cartridge according to the exemplary embodiment will be described.
The process cartridge according to the exemplary embodiment is a process cartridge detachable from the image forming apparatus, which contains the electrostatic charge image developer according to the exemplary embodiment, and includes a developing unit for developing an electrostatic charge image formed on the surface of an image holding member by an electrostatic charge image developer as a toner image.
In addition, the process cartridge according to the exemplary embodiment is not limited to the above configuration, and may have a configuration which includes a developing device, additionally, for example, at least one selected from other units such as an image holding member, a charging unit, an electrostatic charge image forming unit, and a transferring unit, if necessary.
Hereinafter, one example of the process cartridge according to the exemplary embodiment will be shown, but the process cartridge is not limited to this example. In addition, major portions shown in the drawing will be described and the description of others will be omitted.
The process cartridge 200 shown in
In addition, in
Next, the developer cartridge according to the exemplary embodiment will be described.
The developer cartridge according to the exemplary embodiment is a developer cartridge which contains the developer according to the exemplary embodiment and is detachable from the image forming apparatus. The developer cartridge is a cartridge which contains a developer for supplying to supply a developer to the developing unit provided within the image forming apparatus. The developer cartridge according to the exemplary embodiment may have a container which contains the developer according to the exemplary embodiment.
The developer cartridge according to the exemplary embodiment is preferably applied to the image forming apparatus including a trickle system developing device.
For example, the image forming apparatus shown in
In addition, in a case where the developer contained within the developer cartridge is reduced, the developer cartridge is exchanged.
Hereinafter, the exemplary embodiment will be described using Examples, but the exemplary embodiment is not limited to these Examples. In addition, in the following description, particularly, unless otherwise mentioned, all of the “parts” and “%” means “parts by weight” and “% by weight”.
Preparation of Toner Particles
Preparation of Resin Particle Dispersion (1)
After 10 parts by mole of polyoxyethylene(2,0)-2,2-bis(4-hydroxyphenyl)propane, 90 parts by mole of polyoxypropylene(2,2)-2,2-bis(4-hydroxyphenyl)propane, 10 parts by mole of terephthalic acid, 67 parts by mole of fumaric acid, 3 parts by mole of n-dodecenyl succinic acid, 20 parts by mole of trimellitic acid, and 0.05 parts by mole of dibutyltin oxide are put into a heated and dried two necked flask, a nitrogen gas is introduced into the container and heated retaining an inert atmosphere. Then, the resultant is co-condensation polymerized for 15 hours while the temperature is retained from 150° C. to 230° C., and then is slowly evacuated while the temperature is retained from 210° C. to 250° C., thereby synthesizing a polyester resin (1). The weight average molecular weight Mw of the polyester resin (1) is 130,000 and the glass transition temperature Tg is 73° C.
After 3,000 parts of the obtained polyester resin (1), 10,000 parts of ion exchanged water, and 90 parts of a surfactant sodium dodecyl benzenesulfonate are put into an emulsifying tank of a high temperature•high pressure emulsifying apparatus (Cavitron CD1010, slit: 0.4 mm), the resultant is heated and melted at a temperature of 130° C. and then dispersed at a temperature of 110° C., a flow rate of 3 L/minutes, a rotation of 10,000, and for 30 minutes, so as to pass through a cooling tank and collect a resin particle dispersion, thereby obtaining a resin particle dispersion (1).
Preparation of Resin Particle Dispersion (2)
After 44 parts by mole of 1,9-nonanediol, 56 parts by mole of dodecane dicarboxylic acid, and 0.05 parts by mole of dibutyltin oxide as a catalyst are put into a heated and dried three necked flask, the air within the container is made to an inert atmosphere using a nitrogen gas by an evacuating operation, and the resultant is mechanically stirred at a temperature of 180° C. for 2 hours. After that, the temperature of the resultant is slowly increased up to a temperature of 230° C. under evacuation, stirred for 5 hours, and cooled when the resultant becomes a viscous state, and the reaction is stopped so as to synthesize a polyester resin (2). The weight average molecular weight Mw of the polyester resin (2) is 27,000 and the melting temperature Tm is 72° C. After that, a resin particle dispersion (2) is obtained using a high temperature•high pressure emulsifying apparatus (Cavitron CD1010, slit: 0.4 mm), under the same condition as the preparation of the resin particle dispersion (1) except that the polyester resin (2) is used instead of the polyester resin (1).
Preparation of Coloring Agent Dispersion
The above components are mixed, dissolved, and dispersed using a high pressure shocking disperser Altimizer (manufactured by SUGINO MACHINE LIMITED, HJP30006) for 1 hour, and a coloring agent dispersion obtained by dispersing a coloring agent (carbon black) is prepared. The volume average particle diameter of the coloring agent (carbon black) in the coloring agent dispersion is 0.12 μm and the concentration of the coloring agent particles is 24% by weight.
Preparation of Release Agent Dispersion
After the above components are heated at a temperature of 95° C. and dispersed using a homogenizer (manufactured by IKA, ULTRA-TURRAX T50), the resultant is dispersed by a pressure discharging GAULIN homogenizer (Gaulin Co.), and a release agent dispersion (concentration of the release agent: 20% by weight) obtained by dispersing the releasing agent whose volume average particle diameter is 200 nm is prepared.
Preparation of Toner Particles (1)
After the above components are contained in a round-bottom flask made of a stainless steel and dispersed using a homogenizer (manufactured by IKA, ULTRA-TURRAX T50), the resultant is heated while the resultant is stirred in an oil bath for heating up to a temperature of 45° C. After the resultant is kept at a temperature of 48° C., in the stage in which it is confirmed that aggregated particles whose average particle diameter is 5.2 μm are formed, 100 parts of additional resin particle dispersion (2) is added thereto and then kept for 30 minutes. Subsequently, after 0.5 parts of 10% EDTA (ethylenediaminetetraacetic acid) metal salt aqueous solution (CHELEST Mg•40, manufactured by CHELEST CORPORATION) is added thereto, 1N sodium hydroxide aqueous solution is gently added thereto until the pH reaches 7.0. After that, the resultant is heated to a temperature of 90° C. while the resultant is continuously stirred, and kept for 2 hours. Then, a reaction product is filtrated, washed with ion exchanged water, and then dried using a vacuum drier so as to obtain toner particles (1). As a result of measuring the volume average particle diameter D50v of the toner particles (1), the volume average particle diameter D50v is 6.2 μm and the volume particle diameter distribution index GSDv is 1.20. As a result of observing the toner particles using LUZEX image analyzer manufactured by LUZEX, it is observed that the shape factor SF1 of the particles is 135 and the particles are non-spherical. Also, the glass transition temperature of the toner particles (1) is 52° C.
Preparation of External Additive
Preparation of Silica Particle Dispersion (1)
300 parts of methanol and 70 parts of 10% ammonia aqueous solution are added to a 1.5 L reaction vessel made of a glass equipped with a stirrer, a dripping nozzle, and a thermometer and mixed so as to obtain an alkali catalyst solution.
After this alkali catalyst solution is adjusted to a temperature of 30° C., 185 parts of tetramethoxysilane and 50 parts of 8.0% ammonia aqueous solution are added dropwise to the solution, while the solution is stirred, and a hydrophilic silica particle dispersion (solid content concentration of 12.0% by weight) is obtained. Here, the dripping time is 30 minutes.
After that, the obtained silica particle dispersion is concentrated to the solid content concentration of 40% by weight using a rotary filter R-FINE (manufactured by KOTOBUKI KOGYOU CO., LTD.). This concentrated dispersion is a silica particle dispersion (1).
Preparation of Silica Particle Dispersions (2) to (8)
In the preparation of the silica particle dispersion (1), silica particle dispersions (2) to (8) are prepared in the same manner as the silica particle dispersion (1), except that the alkali catalyst solution (methanol amount and 10% ammonia aqueous solution amount) and a preparation condition of the silica particles (tetramethoxysilane (written as TMOS) to the alkali catalyst solution, total dripping amount of 8% ammonia aqueous solution, and dripping time) are changed according to Table 1.
Hereinafter, the details of the silica particle dispersions (1) to (8) are summarized in Table 1.
Preparation of Surface Treated Silica Particles (S1)
The silica particles are surface treated by a siloxane compound under the atmosphere of supercritical carbon dioxide using the silica particle dispersion (1) as shown below. In addition, for the surface treatment, an apparatus including a carbon dioxide bombe, a carbon dioxide pump, an entrainer pump, an autoclave with a stirrer (capacity of 500 ml), and a pressure valve is used.
First, 250 parts by weight of the silica particle dispersion (1) is put into the autoclave with a stirrer (capacity of 500 ml) and the stirrer is rotated at 100 rpm. After that, liquefied carbon dioxide is injected into the autoclave, the pressure thereof is increased by the carbon dioxide pump while the temperature thereof is increased by a heater, and the inside of the autoclave is made to a supercritical state of 150° C. and 15 MPa. The supercritical carbon dioxide is made to circulate by the carbon dioxide pump while the inside of the autoclave is retained to 15 MPa by the pressure valve and the methanol and water are removed from the silica particle dispersion (1) (the solvent removing step) so as to obtain silica particles (untreated silica particles).
Next, circulation of the supercritical carbon dioxide is stopped at the time when the amount of circulated supercritical carbon dioxide (estimated amount: measured as the circulation amount of carbon dioxide in a standard state) becomes 900 parts.
After that, in a state where the temperature is retained to 150° C. by the heater and the pressure is retained to 15 MPa by the carbon dioxide pump so as to retain the supercritical state of the carbon dioxide within the autoclave, a solution of a treating agent obtained by dissolving 0.3 parts of dimethyl silicone oil (DSO: trade name “KF-96 (manufactured by Shin-Etsu Chemical Co., Ltd.)”) having a viscosity of 10,000 cSt as the siloxane compound in 20 parts of hexamethyl disilazane (HMDS: manufactured by YUKI GOSEI KOGYO CO., LTD.) as the hydrophobizing agent, is injected into the autoclave by an entrainer pump in advance with respect to 100 parts of the above silica particles (untreated silica particles). Then, the resultant is reacted at a temperature of 180° C. for 20 minutes while the resultant is stirred. After that, the supercritical carbon dioxide is circulated again and a residual solution of the treating agent is removed. After that, the stirring is stopped, the pressure within the autoclave is released to atmospheric pressure by opening the pressure valve, and the temperature is decreased to room temperature (25° C.)
As such, the solvent removing step and the surface treatment by the siloxane compound are performed sequentially so as to obtain surface treated silica particles (S1).
Preparation of Surface Treated Silica Particles (S2) to (S5), (S7) to (S9), and (S12) to (S17)
Surface treated silica particles (S2) to (S5), and (S7) to (S9) are prepared in the same manner as the surface treated silica particles (S1), except that the silica particle dispersion and the surface treatment condition (the treatment atmosphere, the siloxane compound (type, viscosity, and addition amount thereof), and the hydrophobizing agent and the addition amount thereof) are changed according to Table 2, in the preparation of the surface treated silica particles (S1).
Preparation of Surface Treated Silica Particles (S6)
The surface treatment by the siloxane compound is performed with respect to the silica particles under air atmosphere using the same dispersion as the silica particle dispersion (1) used in the preparation of the surface treated silica particles (S1) as shown below.
An ester adapter and a cooling tube are amounted to the reaction vessel used in the preparation of the silica particle dispersion (1), the silica particle dispersion (1) is heated to a temperature of 60° C. to 70° C., and methanol is distilled. At that time, water is added thereto, and the dispersion is further heated to a temperature of 70° C. to 90° C., and methanol is distilled, thereby obtaining an aqueous dispersion of the silica particles. 3 parts of methyl trimethoxysilane (MTMS: manufactured by Shin-Etsu Chemical Co., Ltd.) is added to 100 parts of silica solid content in this aqueous dispersion at room temperature and reacted for 2 hours so as to perform surface treatment of the silica particles. After methyl isobutyl ketone is added to this surface treated dispersion, the resultant is heated to a temperature of 80° C. to 110° C., methanol water is removed, 80 parts of hexamethyl disilazane (HMDS: manufactured by YUKI GOSEI KOGYO CO., LTD.) and 1.0 part of dimethyl silicone oil (DSO: trade name “KF-96 (manufactured by Shin-Etsu Chemical Co., Ltd.)”) having a viscosity of 10,000 cSt as the siloxane compound are added to 100 parts of silica solid content in the obtained dispersion at room temperature, reacted at a temperature of 120° C. for 3 hours, and cooled. Then, the resultant is dried by a spray drier and the surface treated silica particles (S6) are obtained.
Preparation of Surface Treated Silica Particles (S10)
The surface treated silica particles (S10) are prepared based on the surface treated silica particles (S1), except that fumed silica OX50 (AEROSILOX 50, manufactured by NIPPON AEROSIL CO., LTD) is used instead of the silica particle dispersion (1). In other words, 100 parts of OX50 is injected into the autoclave with a stirrer in the same manner as the preparation of the surface treated silica particles (S1) and the stirrer is rotated at 100 rpm. After that, liquefied carbon dioxide is injected into the autoclave, the pressure thereof is increased by the carbon dioxide pump while the temperature thereof is increased by a heater, and the inside of the autoclave is made to a supercritical state of 180° C. and 15 MPa. While the inside of the autoclave is retained to 15 MPa by the pressure valve, a solution of a treating agent obtained by dissolving 0.3 parts of dimethyl silicone oil (DSO: trade name “KF-96 (manufactured by Shin-Etsu Chemical Co., Ltd.)”) having a viscosity of 10,000 cSt as the siloxane compound in 20 parts of hexamethyl disilazane (HMDS: manufactured by YUKI GOSEI KOGYO CO., LTD.) as the hydrophobizing agent, is injected into the autoclave by an entrainer pump in advance. Then, the resultant is reacted at a temperature of 180° C. for 20 minutes, while the resultant is stirred. After that, the supercritical carbon dioxide is circulated and a residual solution of the treating agent is removed so as to obtain surface treated silica particles (S10).
Preparation of Surface Treated Silica Particles (S11)
The surface treated silica particles (S11) are prepared based on the surface treated silica particles (S1), except that fumed silica A50 (AEROSIL A50, manufactured by NIPPON AEROSIL CO., LTD) is used instead of the silica particle dispersion (1). In other words, 100 parts of A50 is injected into the autoclave with a stirrer in the same manner as the preparation of the surface treated silica particles (S1) and the stirrer is rotated at 100 rpm. After that, liquefied carbon dioxide is injected into the autoclave, the pressure thereof is increased by the carbon dioxide pump while the temperature thereof is increased by a heater, and the inside of the autoclave is made to a supercritical state of 180° C. and 15 MPa. While the inside of the autoclave is retained to 15 MPa by the pressure valve, a solution of a treating agent obtained by dissolving 1.0 part of dimethyl silicone oil (DSO: trade name “KF-96 (manufactured by Shin-Etsu Chemical Co., Ltd.)”) having a viscosity of 10,000 cSt as the siloxane compound in 40 parts of hexamethyl disilazane (HMDS: manufactured by YUKI GOSEI KOGYO CO., LTD.) as the hydrophobizing agent, is injected into the autoclave by an entrainer pump in advance. Then, the resultant is reacted at a temperature of 180° C. for 20 minutes, while the resultant is stirred. After that, the supercritical carbon dioxide is circulated and a residual solution of the treating agent is removed so as to obtain surface treated silica particles (S11).
Preparation of Surface Treated Silica Particles (SC1)
The surface treated silica particles (SC1) are prepared in the same manner as the surface treated silica particles (S1), except that the siloxane compound is not added in the preparation of the surface treated silica particles (S1).
Preparation of Surface Treated Silica Particles (SC2) to (SC4)
The surface treated silica particles (SC2) to (SC4) are prepared in the same manner as the surface treated silica particles (S1), except that the silica particle dispersion and a surface treatment condition (the treatment atmosphere, the siloxane compound (type, viscosity, and addition amount thereof), the hydrophobizing agent, and the addition amount thereof) are changed according to Table 3 in the preparation of the surface treated silica particles (S1).
Preparation of Surface Treated Silica Particles (SC5)
The surface treated silica particles (SC5) are prepared in the same manner as the surface treated silica particles (S6), except that the siloxane compound is not added in the preparation of the surface treated silica particles (S6).
Preparation of Surface Treated Silica Particles (SC6)
After the silica particle dispersion (8) is filtrated and dried at a temperature of 120° C., the resultant is put into an electric furnace and baked at a temperature of 400° C. for 6 hours. Then, 10 parts of HMDS is sprayed with respect to the silica particles by a spray drier and dried, thereby preparing the surface treated silica particles (SC6).
Physical Properties of Surface Treated Silica Particles
With respect to the obtained surface treated silica particles, the average equivalent circle diameter, the average circularity, the attachment amount of the siloxane compound to the untreated silica particles (in Tables, written as “surface attachment amount”), the compression aggregation degree, the particle compression ratio, and the particle dispersion degree are measured by the above methods.
Hereinafter, Table 2 and Table 3 show a list of details of the surface treated silica particles. In addition, the abbreviation in Table 2 and Table 3 are as follows.
Preparation of Carrier
Preparation of Core Particles A
MnO, MgO, and Fe2O3 are respectively mixed in the amount of 29 parts, 1 part, and 70 parts, and this raw material mixture is mixed by a wet ball mill for 10 hours and pulverized. Then, the raw material is finely pulverized and dispersed using a rotary kiln and kept at a temperature of 900° C. for 1 hour so as to perform pre-baking. The pre-baked product obtained in this way is pulverized by a wet ball mill for 10 hours so as to obtain an oxide slurry having an average particle diameter of 0.8 μm. A dispersant and polyvinyl alcohol are added to the obtained slurry in the appropriate amount (0.3% with respect to 100% of the oxide slurry) and subsequently the resultant is granulated and dried by a spray drier. Then, the resultant is kept in a rotary electric furnace at a temperature of 1,100° C. and an oxygen concentration of 0.3% for 7 hours so as to perforom baking. The obtained ferrite particles are magnetic-separated and mixed to obtain core particles A.
Preparation of Core Particles B
Li2O, MgO, CaO, and Fe2O3 are respectively mixed in the amount of 15 parts by weight, 7 parts by weight, 3 parts by weight and 75 parts by weight, and this raw material mixture is mixed by a wet ball mill for 10 hours and pulverized. Then, the raw material is finely pulverized and dispersed using a rotary kiln and kept at a temperature of 900° C. for 1 hour so as to perform pre-baking. The pre-baked product obtained in this way is pulverized by a wet ball mill for 10 hours so as to obtain an oxide slurry having an average particle diameter of 0.8 μm. A dispersant and polyvinyl alcohol are added to the obtained slurry in the appropriate amount (0.3% by weight with respect to 100% by weight of the oxide slurry) and subsequently the resultant is granulated and dried by a spray drier. Then, the resultant is kept in a rotary electric furnace at a temperature of 1,100° C. and an oxygen concentration of 0.3% for 7 hours so as to perforom baking. The obtained ferrite particles are magnetic-separated and mixed to obtain core particles B.
Preparation of Core Particles C
MnO, MgO, and Fe2O3 are respectively mixed in the amount of 29 parts by weight, 1 part by weight, and 70 parts by weight, and this raw material mixture is mixed by a wet ball mill for 10 hours and pulverized. Then, the raw material is finely pulverized and dispersed using a rotary kiln and kept at a temperature of 900° C. for 1 hour so as to perform pre-baking. The pre-baked product obtained in this way is pulverized by a wet ball mill for 8 hours so as to obtain an oxide slurry having an average particle diameter of 1.8 μm. A dispersant and polyvinyl alcohol are added to the obtained slurry in the appropriate amount (0.3% by weight with respect to 100% by weight of the oxide slurry) and subsequently the resultant is granulated and dried by a spray drier. Then, the resultant is kept in a rotary electric furnace at a temperature of 1, 100° C. and an oxygen concentration of 0.3% for 7 hours so as to perforom baking. The obtained ferrite particles are magnetic-separated and mixed to obtain core particles C.
Preparation of Core Particles D
MnO, MgO, and Fe2O3 are respectively mixed in the amount of 29 parts by weight, 1 part by weight, and 70 parts by weight, and this raw material mixture is mixed by a wet ball mill for 10 hours and pulverized. Then, the raw material is finely pulverized and dispersed using a rotary kiln and kept at a temperature of 900° C. for 1 hour so as to perform pre-baking. The pre-baked product obtained in this way is pulverized by a wet ball mill for 10 hours so as to obtain an oxide slurry having an average particle diameter of 0.8 μm. A dispersant and polyvinyl alcohol are added to the obtained slurry in the appropriate amount (0.3% by weight with respect to 100% by weight of the oxide slurry) and subsequently the resultant is granulated and dried by a spray drier. Then, the resultant is kept in a rotary electric furnace at a temperature of 1,300° C. and an oxygen concentration of 0.3% for 7 hours so as to perforom baking. The obtained ferrite particles are magnetic-separated and mixed to obtain core particles D.
Preparation of Carrier CA1
A raw material solution for forming a resin coated layer A composed of the following components is stirred by a stirrer for 60 minutes and dispersed to prepare a raw material solution for forming a coating layer A. Next, this raw material solution for forming a resin coated layer A and 100 parts by weight of the core particles A are put into a vacuum degassing type kneader and stirred at a temperature of 70° C. for 30 minutes. Then, the resultant are further evacuated, degassed, and dried. Further, the resultant is made to pass a mesh having an aperture of 75 μm to prepare a carrier CA1. The Ra of the obtained carrier CA1 is 0.22 and circularity is 0.993.
<Raw Material Solution for Forming a Resin Coated Layer A>
Toluene: 18 parts
Styrene-methacrylate copolymer (component ratio 30:70): 4.5 parts
Carbon black (REGAL 330; manufactured by Cabot Corporation): 0.7 parts
Preparation of Carrier CA2
A raw material solution for forming a resin coated layer B composed of the following components is stirred by a stirrer for 60 minutes and dispersed to prepare a raw material solution for forming a coating layer B. Next, this raw material solution for forming a resin coated layer B and 100 parts by weight of the core particles B are put into a vacuum degassing type kneader and stirred at a temperature of 70° C. for 30 minutes. Then, the resultant are further evacuated, degassed, and dried. Further, the resultant is made to pass a mesh having an aperture of 75 μm to prepare a carrier CA2. The Ra of the obtained carrier CA2 is 0.45 and circularity is 0.982.
<Raw Material Solution for Forming a Resin Coated Layer B>
Methanol: 20 parts
γ-amino triethoxysilane (KBE903, manufactured by Shin-Etsu Chemical Co., Ltd.): 2.2 parts
Carbon black (REGAL 330; manufactured by Cabot Corporation): 0.34 parts
Preparation of Carrier CA3
A raw material solution for forming a resin coated layer C composed of the following components is stirred by a stirrer for 60 minutes and dispersed to prepare a raw material solution for forming a coating layer C. Next, this raw material solution for forming a resin coated layer C and 100 parts by weight of the core particles A are put into a vacuum degassing type kneader and stirred at a temperature of 70° C. for 30 minutes. Then, the resultant are further evacuated, degassed, and dried. Further, the resultant is made to pass a mesh having an aperture of 75 μm to prepare a carrier CA3. The Ra of the obtained carrier CA3 is 0.31 and circularity is 0.972.
<Raw Material Solution for Forming a Resin Coated Layer C>
Toluene: 8.6 parts
Styrene-methacrylate copolymer (component ratio 30:70): 1.30 parts
Carbon black (REGAL 330; manufactured by Cabot Corporation): 0.20 parts
Preparation of Carrier CA4
A raw material solution for forming a resin coated layer A composed of the above components is stirred by a stirrer for 60 minutes and dispersed to prepare a raw material solution for forming a coating layer A. Next, this raw material solution for forming a resin coated layer A and 100 parts by weight of the core particles C are put into a vacuum degassing type kneader and stirred at a temperature of 70° C. for 30 minutes. Then, the resultant are further evacuated, degassed, and dried. Further, the resultant is made to pass a mesh having an aperture of 75 μm to prepare a carrier CA4. The Ra of the obtained carrier CA4 is 0.65 and circularity is 0.991.
The silica particles shown in Table 4 are added to 100 parts of the toner particles shown in Table 4 according to the number of parts shown in Table 4, and the resultant is mixed by HENSCHEL MIXER at 2,000 rpm for 3 minutes, thereby obtaining a toner of each example.
In addition, the obtained each toner and the carrier shown in Table 4 are put into a V blender at a ratio (toner:carrier) of 5:95 (weight ratio) and stirred for 20 minutes, thereby obtaining each developer.
Evaluations
A decrease in an image density of the toner is evaluated with respect to the developer obtained in each example. In addition, the attachment degree (coating degree) of the silica particles flaked from the toner to the carrier is evaluated. The results are shown in Table 4.
Decrease in Image Density
An image is formed according to the following method and the degree of occurrence of a decrease in the image density is evaluated.
A solid image is printed using a modified apparatus of APEORPORT IV C5570 manufactured by Fuji Xerox Co., Ltd. and using a reflection densitometer (X-RITE 938) manufactured by X-Rite Inc., and an initial image density (SAD) is confirmed. Then, printing is performed at an image density of 1% in an environment of 30° C./RH 80% on 5,000 pieces, 10,000 pieces, and 15,000 pieces of sheets respectively, and then printing is performed at an image density of 100% in an environment of 15° C./RH 20% on the 10 pieces of sheets, and the image density of 5 points per one piece of sheet is measured. The average SAD is calculated and the decreasing degree from the initial SAD is measured.
The evaluation standard is as follows.
A: A decrease in density is hardly observed (ΔSAD≦0.05)
B: A decrease in density is slightly observed, but there is no problem in practical use (0.05<ΔSAD≦0.10)
C: A decrease in density is observed, but there is no problem in practical use (0.10<ΔSAD≦0.20)
D: A decrease in density is remarkably observed (ΔSAD>0.20)
Attachment Degree of Silica Particles Flaked from Toner to Carrier
In the above evaluation test, the initial attachment degree of the silica particles flaked from the toner to the carrier is evaluated according to the following evaluation method.
A developer before and after the test is put into a gauge with a mesh of an aperture of 20 μm and the toner and the carrier are separated by air blowing. The Si element content of the obtained carrier is measured using XRF 1500, which is an X-ray fluorescence measuring apparatus manufactured by Shimazu Corporation and the Net strength of the Si element is obtained. A value obtained by subtracting the Net strength obtained by measuring the Si element content of the carrier only from the obtained Net strength is regarded as a movement amount of the silica to the carrier, and the evaluation is performed according to the following standard.
In addition, the decrease in an image density tends to be deteriorated if the carrier movement amount exceeds about 1.0. Thus, the evaluation standard is set as follows.
A: Movement amount to the carrier ≦0.5
B: 0.5<Movement amount to the carrier ≦0.8
C: 0.8<Movement amount to the carrier ≦1.0
D: Movement amount to the carrier >1.0
From the above result, it is understood that the decrease in an image density is prevented in Examples, compared to Comparative Examples.
In particular, it is understood that in Examples 1 to 5, 14, and 18 to 20 in which the silica particles having the compression aggregation degree of 70% to 95% and the particle compression ratio of 0.28 to 0.36 are applied as the external additive, the decrease in an image density is prevented compared to other Examples.
The foregoing description of the exemplary embodiments of the present invention has been provided for the purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise forms disclosed. Obviously, many modifications and variations will be apparent to practitioners skilled in the art. The embodiments were chosen and described in order to best explain the principles of the invention and its practical applications, thereby enabling others skilled in the art to understand the invention for various embodiments and with the various modifications as are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the following claims and their equivalents.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2016-024132 | Feb 2016 | JP | national |
| Number | Name | Date | Kind |
|---|---|---|---|
| 6057073 | Hagiwara | May 2000 | A |
| 6316155 | Kudo et al. | Nov 2001 | B1 |
| 20010051270 | Yamashita et al. | Dec 2001 | A1 |
| 20030232185 | Shimamura | Dec 2003 | A1 |
| 20070201917 | Teshigawara | Aug 2007 | A1 |
| 20090067894 | Yamada | Mar 2009 | A1 |
| 20100203441 | Kataoka et al. | Aug 2010 | A1 |
| 20110177444 | Mattison, Jr. et al. | Jul 2011 | A1 |
| 20120189851 | Zenitani | Jul 2012 | A1 |
| 20140057107 | Zenitani | Feb 2014 | A1 |
| 20160139521 | Tsuda et al. | May 2016 | A1 |
| Number | Date | Country |
|---|---|---|
| 1 845 419 | Oct 2007 | EP |
| 2 479 208 | Jul 2012 | EP |
| 2000-330328 | Nov 2000 | JP |
| 2009-098700 | May 2009 | JP |
| 4347201 | Oct 2009 | JP |
| 2009-292915 | Dec 2009 | JP |
| 2010-185999 | Aug 2010 | JP |
| 4758655 | Aug 2011 | JP |
| 4828032 | Nov 2011 | JP |
| 2014-162678 | Sep 2014 | JP |
| 2014-185069 | Oct 2014 | JP |
| Entry |
|---|
| Apr. 10, 2017 Office Action issued in U.S Appl. No. 15/211,974. |
| U.S Appl. No. 15/211,974, filed Jul. 15, 2016 in the name of Kadokura et al. |
| U.S Appl. No. 15/001,950, filed Jan. 20, 2016 in the name of Okuno et al. |
| Jul. 26, 2017 Office Action issued in U.S Appl. No. 15/211,974. |
| Number | Date | Country | |
|---|---|---|---|
| 20170227876 A1 | Aug 2017 | US |
