Patent Application
20100261112
1. Technical Field
The present invention relates to a toner, a method for forming an image, and an image forming apparatus.
2. Related Art
There have been image forming apparatuses that use a method including steps of rotatably mounting a photo-conductor such as a photosensitive drum or a photosensitive belt that is a latent image carrying unit onto a main body of an image forming apparatus, and during the image forming operation, forming an electrostatic latent image on a photosensitive layer of the photo-conductor, making the latent image visible in a contact or noncontact manner using toner, and directly transferring the visible image to a material to be transferred through corona transfer or using a transfer roller; or a method including steps of temporarily transferring the visible image to an intermediate transfer medium such as a transfer drum or a transfer belt and transferring the visible image to a material to be transferred again. In these image forming apparatuses, a two-component toner is publicly known, which can provide relatively stable development. However, the mixing ratio of a developer to a magnetic carrier easily varies, which requires the maintenance. On the other hand, a single-component magnetic toner cannot provide a clear color image because of the opacity of magnetic materials.
In recent years, there has been concern that dust is contained in a cooling airflow exhausted from electrophotographic image forming apparatuses to the outside, and the dust adversely affects the human body. An example of a standard that regulates dust in the air includes a standard regarding fine particulate matter (PM 2.5), which is reviewed by the Ministry of the Environment. In the near future, it is planned for legal guidelines to be disclosed as an environmental standard. It is expected that one of the causes of dust generation is that an external additive having charge-leaking properties is liberated from the surface of toner and emitted to the outside of the image forming apparatus during its operation. Furthermore, from the viewpoint of achieving clearness of an image, the particle size of toner has been decreased in recent years. It is believed that, in particular, toner having a small volume-average particle size of 2 to 4 μm becomes mainstream. However, in the system in which an image is formed by applying an alternating current (AC) electric field between the developing roller and the photo-conductor, toner particles move onto the photo-conductor while reciprocate under a development electric field. Therefore, there is also concern that part of the toner activated in a cloud form under the development electric field rides an airflow that flows in the image forming apparatus, whereby not only the external additives but also the toner particles themselves become dust.
Since the number of particles of such a small particle size toner increases exponentially compared with an ordinary toner, it is extremely difficult to achieve high-speed and uniform electrification of toner, which poses many problems such as fogging, scattering of toner, leakage, and development history caused by nonuniformity of toner electrification. Normally, to improve the toner electrification, a potential difference is provided using a regulating blade and a developing roller, which is known as so-called “regulation bias” (refer to JP-A-2005-331780). In the regulation bias, a larger potential difference further improves the toner electrification. However, when the potential difference is excessively large, the movement of electrons is locally concentrated, which causes the formations of toner aggregates, charge-polarity reversed toner, and white portions on a toner-carrying surface. The threshold of the potential difference is extremely low for small particle size toner. Therefore, only a method that uses regulation bias does not provide a sufficient effect.
The toner particles are carried on the surface of the developing roller and pressed by a layer thickness regulating member, whereby the toner particles are rubbed by the surface subjected to pressing, the layer thickness regulating member, and the like and charged. The developing roller may have minute projections and depressions on a toner carrying surface by being subjected to blasting. However, the size, depth, shape, and arrangement of the depressions are nonuniform. Thus, toner particles that have entered deep depressions are sometimes not rolled and thus not appropriately charged. The nonuniformity of projections and depressions on the surface of the developing roller may locally cause poor electrification of the toner particles. If the toner particles become stuck in the minute depressions, filming may be caused. If the toner particles are not charged appropriately, the toner particles may leak out from the developing apparatus and be scattered in an image forming apparatus or to the outside of the image forming apparatus or the transfer efficiency may be reduced.
An advantage of some aspects of the invention is to provide a toner that has uniform electrification and can be easily transferred even if the volume-average particle size is as small as 2 to 6 μm, particularly 2 to 4 μm, and a method for forming an image and an image forming apparatus that are suitable for the toner.
A toner according to a first aspect of the invention includes toner base particles containing at least a binder resin, a coloring agent, and a release agent and having a volume-average particle size of 2 to 6 μm; at least two types of silica each having a different average particle size; at least one type of electron-conductive oxide semiconductor fine particles selected from titania, transition alumina, zinc oxide, and tin oxide; and at least one type of ion-conductive oxide semiconductor fine particles selected from cerium oxide and stabilized zirconia.
It is preferable that the electron-conductive oxide semiconductor fine particles have an average particle size of 7 to 30 nm and the ion-conductive oxide semiconductor fine particles have an average particle size of 50 to 400 nm.
It is preferable that the amount of the ion-conductive oxide semiconductor fine particles added is 0.5 to 2.5 parts by mass and the amount of the electron-conductive oxide semiconductor fine particles added is 0.3 to 2.0 parts by mass relative to 100 parts by mass of the toner base particles while the amount of the ion-conductive oxide semiconductor fine particles added is larger than that of the electron-conductive oxide semiconductor fine particles added.
It is preferable that the toner base particles have an average particle size of 2 to 4 μm and are obtained by phase inversion emulsification.
A method for forming an image according to a second aspect of the invention includes preparing a photo-conductor that carries an electrostatic latent image and a developing apparatus facing the photo-conductor in a noncontact manner; supplying a toner to the developing apparatus; and developing the electrostatic latent image carried by the photo-conductor under an alternating current electric field. In the method, the toner includes toner base particles containing at least a binder resin, a coloring agent, and a release agent and having a volume-average particle size of 2 to 6 μm, at least two types of silica each having a different average particle size, at least one type of electron-conductive oxide semiconductor fine particles selected from titania, transition alumina, zinc oxide, and tin oxide, and at least one type of ion-conductive oxide semiconductor fine particles selected from cerium oxide and stabilized zirconia.
An image forming apparatus according to a third aspect of the invention includes a photo-conductor that carries an electrostatic latent image; and a developing apparatus facing the photo-conductor in a noncontact manner. In the image forming apparatus, a toner is supplied to the developing apparatus to develop the electrostatic latent image carried by the photo-conductor under an alternating current electric field. The toner includes toner base particles containing at least a binder resin, a coloring agent, and a release agent and having a volume-average particle size of 2 to 6 μm, at least two types of silica each having a different average particle size, at least one type of electron-conductive oxide semiconductor fine particles selected from titania, transition alumina, zinc oxide, and tin oxide, and at least one type of ion-conductive oxide semiconductor fine particles selected from cerium oxide and stabilized zirconia.
According to some aspects of the invention, there can be provided a toner that has uniform electrification and can be easily transferred even if the volume-average particle size is as small as 2 to 6 μm, particularly 2 to 4 μm, a method for forming an image and an image forming apparatus that are suitable for the toner.
The invention will be described with reference to the accompanying drawings, wherein like numbers reference like elements.
Toner base particles of the invention contain at least a binder resin, a coloring agent, and a release agent. The toner base particles may be obtained by emulsion aggregation, but are preferably obtained by phase inversion emulsification. The toner base particles of the invention are manufactured through (1) a first step of forming fine particles by emulsifying a mixture containing at least a polyester resin and an organic solvent in an aqueous medium under the presence of a basic compound; (2) a second step of aggregating the fine particles by adding a dispersion stabilizer and then an electrolyte to make aggregates of the fine particles; and (3) a third step of removing the organic solvent contained in the aggregates, separating the aggregates of the fine particles from the aqueous medium, and cleaning and drying the aggregates.
The polyester resin is synthesized by dehydration condensation between a polybasic acid and a polyhydric alcohol. Examples of the polybasic acid include aromatic carboxylic acids such as terephthalic acid, isophthalic acid, phthalic anhydride, trimellitic anhydride, pyromellitic acid, and naphthalene dicarboxylic acid; aliphatic carboxylic acids such as maleic anhydride, fumaric acid, succinic acid, alkenyl succinic anhydride, and adipic acid; and alicyclic carboxylic acids such as cyclohexane dicarboxylic acid. These polybasic acids can be used alone or in combination. Among the polybasic acids, an aromatic carboxylic acid is preferably used.
Examples of the polyhydric alcohol include aliphatic diols such as ethylene glycol, diethylene glycol, triethylene glycol, propylene glycol, butanediol, hexanediol, neopentyl glycol, glycerin, trimethylol propane, and pentaerythritol; alicyclic diols such as cyclohexanediol, cyclohexanedimethanol, and hydrogenated bisphenol A; and aromatic diols such as an ethylene oxide adduct of bisphenol A and a propylene oxide adduct of bisphenol A. These polyhydric alcohols can be used alone or in combination. Among the polyhydric alcohols, an aromatic diol or an alicyclic diol is preferably used. An aromatic diol is more preferably used.
A terminal hydroxyl group and/or a terminal carboxyl group is esterified by adding a monocarboxylic acid and/or a monoalcohol to the polyester resin obtained by condensation polymerization between the polyvalent carboxylic acid and the polyhydric alcohol, whereby the acid value of the polyester resin can be adjusted. Examples of the monocarboxylic acid used for such a purpose include acetic acid, acetic anhydride, benzoic acid, trichloroacetic acid, trifluoroacetic acid, and propionic anhydride. Examples of the monoalcohol include methanol, ethanol, propanol, octanol, 2-ethylhexanol, trifluoroethanol, trichloroethanol, hexafluoroisopropanol, and phenol.
The polyester resin can be prepared by condensing the polyhydric alcohol and the polyvalent carboxylic acid on the basis of a common method. For example, an intended reactant can be obtained through the steps of adding the polyhydric alcohol and the polyvalent carboxylic acid to a reaction vessel equipped with a thermometer, a stirrer, and a falling condenser; heating the mixture at 150 to 250° C. under the presence of inert gas such as nitrogen; continuously removing low-molecular-weight compounds that are by-products to the outside of the reaction system; stopping the reaction when desired physical properties are achieved; and cooling the resultant product.
The polyester resin can be synthesized under the presence of a catalyst. Examples of an esterification catalyst used include organic metals such as dibutyltin dilaurate and dibutyltin oxide and metal alkoxides such as tetrabutyl titanate. When a lower alkyl ester is used as a carboxylic acid component, a transesterification catalyst can be used. Examples of the transesterification catalyst include metal acetates such as zinc acetate, lead acetate, and magnesium acetate; metal oxides such as zinc oxide and antimony oxide; and metal alkoxides such as tetrabutyl titanate. The additive amount of the catalyst is preferably 0.01 to 1% by mass relative to the total amount of raw materials.
In particular, to manufacture a branched or cross-linked polyester resin in such condensation polymerization, a polybasic acid having three or more carboxyl groups per molecule or an anhydride thereof and/or a polyhydric alcohol having three or more hydroxyl groups per molecule needs to be used as an indispensable synthetic material.
The polyester resin preferably has the following properties when measured with a constant-load extrusion type capillary rheometer (hereinafter, referred to as a “flow tester”) in order that toner for use in a heat roller fixation system has a satisfactory fixing/offset temperature range without using an offset prevention liquid. That is, in measurement with the flow tester, the flow beginning temperature (Tfb) is in the range of 80 to 120° C., the T1/2 temperature is in the range of 100 to 160° C., and the flow ending temperature (Tend) is in the range of 110 to 210° C. The use of a polyester resin having such values measured with the flow tester results in good oilless fixing properties. Furthermore, the glass transition temperature (Tg) is preferably in the range of 40 to 75° C.
The flow beginning temperature Tfb, the T1/2 temperature, and the flow ending temperature Tend are determined with a flow tester (Model: CFT-500, available from Shimadzu Corporation). As shown in
The flow beginning temperature Tfb serves as an index of the sharp-melting property and the low-temperature fixing property of a polyester resin. An excessively high temperature degrades the low-temperature fixing property, which easily causes a cold offset. An excessively low temperature degrades storage stability, which easily causes a hot offset. Thus, the flow beginning temperature Tfb is preferably in the range of 90 to 115° C. and more preferably 90 to 110° C.
The melting temperature T1/2 of toner determined by a ½ method and the flow ending temperature Tend each serve as an index of anti-hot offset properties. In each case, an excessively high temperature increases the solution viscosity, which degrades the particle size distribution during the formation of particles. At an excessively low temperature, an offset easily occurs to degrade practicality. Thus, the melting temperature T1/2 in accordance with the ½ method needs to be in the range of 120 to 160° C. and preferably 130 to 160° C. The flow ending temperature Tend is preferably in the range of 130 to 210° C. and more preferably 130 to 180° C. When Tfb, T1/2, and Tend are set within the ranges, toner can be fixed in a wide temperature range.
The polyester resin contains a cross-linked polyester resin. The tetrahydrofuran-insoluble content of the binder resin is in the range of 0.1 to 20% by mass, preferably 0.2 to 10% by mass, and more preferably 0.2 to 6% by mass. The binder resin is preferably a polyester resin having a tetrahydrofuran-insoluble content of 0.1 to 20% by mass because good anti-hot offset properties are achieved. When the tetrahydrofuran-insoluble content is less than 0.1% by mass, the effect of improving the anti-hot offset properties is insufficient, which is not preferred. When the tetrahydrofuran-insoluble content is more than 20% by mass, the solution viscosity becomes excessively high, which increases the fixing initiation temperature. This disturbs fixing balance and thus is not preferred. Furthermore, this impairs the sharp-melting property to degrade transparency, color reproducibility, and gloss in a color image, which is not preferred.
The tetrahydrofuran-insoluble content of the binder resin is determined through the steps of weighing 1 g of the resin accurately; adding the resin to 40 ml of tetrahydrofuran to completely dissolve the resin; filtering the resulting mixture through 2 g of Radiolite (#700 available from Showa Chemical Industry Co., Ltd.) uniformly placed on Kiriyama filter paper (No. 3) in a filter funnel (diameter: 40 mm); placing the resulting cake on an aluminum dish; drying the cake at 140° C. for 1 hour; and weighing the resulting dry cake. The weight of the residual resin remaining in the dry cake is divided by the initial weight of the resin to express the resulting value in percentage. This value is defined as the tetrahydrofuran-insoluble content of the binder resin.
More preferably, the binder resin contains a high-viscosity cross-linked polyester resin and a low-viscosity branched or linear polyester resin. That is, in the polyester resin according to the invention, the binder resin may be composed of a single polyester resin. However, in general, the binder resin containing both a high-viscosity cross-linked polyester resin having a high molecular weight (cross-linked polyester resin) and a low-viscosity branched or linear polyester resin having a low molecular weight is practical and preferred in view of the production of the resin and in order to achieve a satisfactory fixing initiation temperature and satisfactory anti-hot offset properties. In the case where the binder resin contains both the cross-linked polyester resin and the branched or linear polyester resin, values of the binder resin measured using the flow tester need only to be within the above-described ranges. In the invention, the cross-linked polyester resin refers to a resin containing the tetrahydrofuran-insoluble component. The branched or linear polyester resin refers to a resin that is soluble in tetrahydrofuran and has no gel component determined through the measurement of the gel component.
In the invention, a plurality of polyester resins having different melt viscosities may be used as the binder resin. For example, in the case where a mixture of a low-viscosity branched or linear polyester resin and a high-viscosity cross-linked polyester resin is used, there is preferably used a mixture of a branched or linear polyester resin (A) and a cross-linked or branched polyester resin (B) that satisfy the following requirements. In this case, the melt viscosities and amounts of the resins (A) and (B) are appropriately adjusted such that values of the mixture measured using the flow tester are within the above-described ranges.
That is, the polyester resin (A) is a branched or linear polyester resin having a T1/2 temperature measured using the flow tester of 80° C. or more and less than 120° C. and a glass transition temperature Tg of 40 to 70° C. The polyester resin (B) is a cross-linked or branched polyester resin having a T1/2 temperature measured using the flow tester of 120° C. or more and 210° C. or less and a glass transition temperature Tg of 50 to 75° C. The ratio by weight of the polyester resin (A) to the polyester resin (B), i.e., (A)/(B), is in the range of 20/80 to 80/20. The T1/2 temperatures of the polyester resin (A) and the polyester resin (B) are defined as T1/2(A) and T1/2(B), respectively. The polyester resin (A) and the polyester resin (B) that satisfy the relationship 20° C.<T1/2(B)−T1/2(A)<100° C. are preferably used.
Regarding the temperature characteristics measured using the flow tester, the melting temperature T1/2(A) of the polyester resin (A) measured by the ½ method serves as an index for imparting the sharp-melting property and the low-temperature fixing property. The melting temperature T1/2(A) is more preferably in the range of 80 to 115° C. and particularly preferably 90 to 110° C.
The resin (A) specified in terms of these properties has a low softening temperature. In a fixing process using a heat roller, even when thermal energy is reduced because of a reduction in the temperature of the heat roller and an increase in process speed, the polyester resin (A) melts sufficiently and exhibits a satisfactory anti-cold offset property and a satisfactory low-temperature fixing property.
In the case where each of the melting temperature T1/2(B) measured by the ½ method and the flow ending temperature Tend(B) of the polyester resin (B) is excessively low, hot offset easily occurs. In the case where each of the melting temperature T1/2(B) and the flow ending temperature Tend(B) is excessively high, a particle size distribution during the formation of particles is degraded to reduce productivity. Consequently, T1/2(B) is more preferably in the range of 125 to 210° C. and particularly preferably 130 to 200° C.
The resin (B) specified in terms of these properties tends to be elastomeric and has high melt viscosity. The internal cohesive force of a melted toner layer is maintained during a heating and melting step in a fixing process. Thus, hot offset does not easily occur. After fixing, the polyester resin (B) is tough and thus exhibits satisfactory abrasion resistance.
A well-balanced mixing of the resin (A) and the resin (B) provides toner that sufficiently satisfies the anti-offset properties in a wide temperature range and the low-temperature fixing property. An excessively low ratio by weight of the resin (A) to the resin (B), i.e., (A)/(B), adversely affects the fixing property. An excessively high ratio adversely affects the anti-offset properties. Consequently, the ratio is preferably in the range of 20/80 to 80/20 and more preferably 30/70 to 70/30.
Melting temperatures of the resin (A) and the resin (B) measured by the 1/2 method are defined as T1/2(A) and T1/2(B), respectively. From the viewpoint of achieving a balance between the low-temperature fixing property and the anti-offset properties and in order to uniformly mixing the mixture without causing problems due to the difference in viscosity between the resins, T1/2(B)−T1/2(A) is more preferably more than 20° C. and 90° C. or less and particularly preferably more than 20° C. and 80° C. or less.
The glass transition temperature (Tg) is a value measured at a heating rate of 10° C. per minute by a second-run method using a differential scanning calorimeter (DSC-50) available from Shimadzu Corporation. When the polyester resin (A) has a Tg of less than 40° C. or when the polyester resin (B) has a Tg of less than 50° C., the resulting toner tends to cause blocking (a phenomenon in which toner particles are coagulated to form aggregates) during storage or in a developing apparatus, which is not preferred. On the other hand, when the polyester resin (A) has a Tg of more than 70° C. or when the polyester resin (B) has a Tg of more than 75° C., the fixing temperature of the toner increases, which is not preferred. When the polyester resin (A) and the polyester resin (B) that satisfy the above-described relationship and serve as the binder resin are used, the resulting toner has more satisfactory fixing properties, which is preferred.
To provide satisfactory fixing properties, the binder resin composed of the polyester resin preferably satisfies all of the following requirements: the weight-average molecular weight is 30,000 or more and preferably 37,000 or more; the (weight-average molecular weight (Mw))/(number-average molecular weight (Mn)) is 12 or more and preferably 15 or more; the area ratio of a component having a molecular weight of 600,000 to the total is 0.3% or more and preferably 0.5% or more; and the area ratio of a component having a molecular weight of 10,000 or less to the total is 20 to 80% and preferably 30 to 70%, in the measurement of the molecular weight by gel permeation chromatography (GPC) of the tetrahydrofuran-soluble fraction (THF-soluble fraction). In the case where the binder resin contains a plurality of resins, the GPC measurement result of a final resin mixture needs only to be within the above-described ranges.
In the polyester resin according to the invention, a high-molecular weight component having a molecular weight of 600,000 or more is effective in ensuring the anti-hot offset property. On the other hand, a low-molecular weight component having a molecular weight of 10,000 or less is effective in reducing the melt viscosity of the resin, thereby attaining the sharp melting property and reducing the fixing initiation temperature. Thus, the polyester resin preferably contains the resin component having a molecular weight of 10,000 or less. To obtain satisfactory thermal properties such as fixation at a low temperature, anti-hot offset properties, and transparency in an oilless fixing system, the binder resin preferably has such a broad molecular weight distribution.
The molecular weight of the THF-soluble fraction in the binder resin is determined in the following manner. That is, the THF-soluble fraction is filtered through a filter (0.2 μm) and then measured with a THF solvent (flow rate: 0.6 ml/min, temperature: 40° C.) using GPC•HLC-8120 produced by Tosoh Corporation and three columns “TSKgel Super HM-M” (15 cm) produced by Tosoh Corporation. Then, the molecular weight is calculated by means of a molecular weight calibration curve made using a monodispersed polystyrene standard sample.
The acid value (mg of KOH required to neutralize 1 g of a resin) of the polyester resin is preferably within a range of 1 to 20 mg KOH/g for the following reasons: the above-described molecular weight distribution is easily obtained; ease of formation of fine particles by emulsification is readily ensured; and good environmental stability (stability of charge properties when the temperature and humidity change) of the resulting toner is easily retained. The acid value of the polyester resin can be adjusted by controlling a terminal carboxyl group of the polyester resin by means of the change in the mixing ratio and the reaction rate of the polybasic acid and the polyhydric alcohol as starting materials, as well as the addition of the monocarboxylic acid and/or the monoalcohol to the polyester resin obtained by condensation polymerization between the polyvalent carboxylic acid and the polyhydric alcohol, as described above. Alternatively, a polyester resin having a carboxyl group in the main chain thereof can be prepared using trimellitic anhydride as the polybasic acid component.
The toner base particles may contain a release agent. The release agent is selected from the group consisting of hydrocarbon waxes such as polypropylene wax, polyethylene wax, and Fischer-Tropsch wax; synthetic ester waxes; and natural ester waxes such as carnauba wax and rice wax. Among them, natural ester waxes such as carnauba wax and rice wax and synthetic ester waxes obtained from a polyhydric alcohol and a long-chain monocarboxylic acid are preferably used. An example of the synthetic ester wax suitably used is WEP-5 (available from NOF Corporation). When the content of the release agent is less than 1% by mass, the releasability is liable to be insufficient. When the content is more than 40% by mass, the wax is liable to be exposed on surfaces of the toner particles, which degrades the charge properties and storage stability. Therefore, the content of the release agent is preferably in the range of 1 to 40% by mass.
The toner base particles may contain a charge control agent. Examples of a negatively charged control agent include heavy-metal-containing acid dyes such as trimethylethane dye, metal complex salts of salicylic acid, metal complex salts of benzilic acid, copper phthalocyanine, perylene, quinacridone, azo dye, azo dye of metal complex salts, and azochromium complexes; calixarene type phenolic condensates; cyclic polysaccharide; and carboxyl- or sulfonyl-group-containing resins. The content of the charge control agent is preferably in the range of 0.01 to 10% by mass and particularly preferably 0.1 to 6% by mass.
The coloring agent is not particularly limited. Known coloring agents may be used, and in particular, a pigment is suitably used. Examples of black pigments include carbon black, cyanine black, aniline black, ferrite, and magnetite. Alternatively, coloring agents prepared from the following color pigments so as to develop a black color may be used.
Examples of yellow pigments include Chrome Yellow, Zinc Yellow, Cadmium Yellow, Yellow Ferric Oxide, ocher, Titanium Yellow, Naphthol Yellow S, Hansa Yellow 10G, Hansa Yellow 5G, Hansa Yellow G, Hansa Yellow GR, Hansa Yellow A, Hansa Yellow RN, Hansa Yellow R, Pigment Yellow L, Benzidine Yellow, Benzidine Yellow G, Benzidine Yellow GR, Permanent Yellow NCG, Vulcan Fast Yellow 5G, Vulcan Fast Yellow R, Quinoline Yellow Lake, Anthragen Yellow 6GL, Permanent Yellow FGL, Permanent Yellow H10G, Permanent Yellow HR, Anthrapyrimidine Yellow, Isoindolinone Yellow, Cromophthal Yellow, Novoperm Yellow H2G, Condensed Azo Yellow, Nickel Azo Yellow, and Copper Azomethine Yellow.
Examples of red pigments include Chrome Orange, Molybdenum Orange, Permanent Orange GTR, Pyrazolone Orange, Vulcan Orange, Indanthrene Brilliant Orange RK, Indanthrene Brilliant Orange GK, Benzidine Orange G, Permanent Red 4R, Permanent Red BL, Permanent Red F5RK, Lithol Red, Pyrazolone Red, Watching Red, Lake Red C, Lake Red D, Brilliant Carmine 6B, Brilliant Carmine 3B, Rhodamine Lake B, Alizarin Lake, Permanent Carmine FBB, Perinone Orange, Isoindolinone Orange, Anthanthrone Orange, Pyranthrone Orange, Quinacridone Red, Quinacridone Magenta, Quinacridone Scarlet, and Perylene Red.
Examples of blue pigments include Cobalt Blue, Cerulean Blue, Alkali Blue Lake, Peacock Blue Lake, Phanatone Blue 6G, Victoria Blue Lake, Metal-free Phthalocyanine Blue, Copper Phthalocyanine Blue, Fast Sky Blue, Indanthrene Blue RS, Indanthrene Blue BC, and Indigo.
The amount of the coloring agent used is preferably in the range of 1 to 50 parts by mass and particularly preferably 2 to 15 parts by mass relative to 100 parts by mass of the binder resin.
A method for manufacturing the toner base particles will now be described. In a first step, the polyester resin is added to an organic solvent and dissolved (by heating, if necessary) to prepare a mixture containing the polyester resin and the organic solvent. In this case, as a raw material for the toner, at least one selected from the coloring agents, the release agents, the charge control agents, and other additives may be used together with the polyester resin. In the invention, the coloring agent is preferably dispersed in the organic solvent together with the polyester resin. The additives such as the release agent and the charge control agent are also particularly preferably dissolved or dispersed in the organic solvent.
The following method is preferably employed as a method for dissolving or dispersing the polyester resin and, if necessary, the additives such as the coloring agent, the release agent, and the charge control agent in the organic solvent. A mixture containing the polyester resin and the additives such as the coloring agent, the release agent, and the charge control agent is kneaded at a temperature in the range of the softening temperature to the thermal decomposition temperature of the polyester resin using a pressure kneader, a heated twin roll, a twin-screw extruder, or the like. For example, the coloring agent may be melt-kneaded as a master batch. The resulting kneaded chips are then dissolved or dispersed in the organic solvent using a stirrer such as Despa. Alternatively, the polyester resin and the additives such as the coloring agent, the release agent, and the charge control agent are mixed with the organic solvent. The resulting mixture is wet-kneaded using a ball mill or the like. In this case, the coloring agent, the release agent, and the like may be separately preliminarily dispersed in advance.
More specifically, there is provided a method for manufacturing a resin solution containing the coloring agent, the release agent, and the like finely dispersed in the organic solvent by placing a resin solution containing the polyester resin dissolved in the organic solvent in advance, the coloring agent, and the release agent into a mixing/dispersing apparatus such as a ball mill, a bead mill, a sand mill, a continuous bead mill, or the like that uses grinding media; stirring and dispersing the mixture to form a master batch; and mixing the polyester resin for dilution and the additional organic solvent. In this case, a master batch prepared by kneading and dispersing the low-viscosity polyester resin and the additives such as the coloring agent and the release agent using a pressure kneader or a heated twin roll in advance is preferably used rather than the direct addition of the additives such as the coloring agent and the release agent to the mixing/dispersing apparatus such as a ball mill without any treatment. This manufacturing method is preferred because the polymeric component (gel component) of the polyester resin is not cleaved, compared with a dispersing method by melt-kneading.
Examples of the organic solvent for dissolving or dispersing the polyester resin and, if necessary, the coloring agent, the release agent, and the like include hydrocarbons such as pentane, hexane, heptane, benzene, toluene, xylene, cyclohexane, and petroleum ether; halogenated hydrocarbons such as methylene chloride, chloroform, dichloroethane, dichloroethylene, trichloroethane, trichloroethylene, and carbon tetrachloride; ketones such as acetone, methyl ethyl ketone, and methyl isobutyl ketone; and esters such as ethyl acetate and butyl acetate. These solvents may be used alone or in combination. In view of the recovery of the solvent, a single type of solvent is preferably used. The organic solvent that can dissolve the binder resin, has relatively low toxicity, and has a low boiling point so as to be easily removed in the subsequent step is preferred. Methyl ethyl ketone is most preferred.
In a method for emulsifying the mixture containing the polyester resin and the organic solvent with an aqueous medium, the mixture that contains the polyester resin, the organic solvent, and, if necessary, the coloring agent and the like and is prepared by the above-described method is preferably mixed and emulsified with the aqueous medium under the presence of a basic neutralizer. In this step, preferably, the aqueous medium (water or a liquid medium mainly composed of water) is gradually added to the mixture containing the polyester resin, the organic solvent, the coloring agent, and the like. In this case, gradual addition of water to the continuous organic phase of the mixture produces discontinuous water-in-oil phases. Further addition of water causes inversion of the discontinuous water-in-oil phases to produce discontinuous oil-in-water phases and forms a suspension or an emulsified liquid in which the mixture is suspended as particles (droplets) in the aqueous medium (hereinafter, this method is referred to as “phase inversion emulsification”). In phase inversion emulsification, water is added such that the ratio of the amount of water to the total amount of the organic solvent and water added is 30 to 70%, more preferably 35 to 65%, and particularly preferably 40 to 60%. The aqueous medium used is preferably water and more preferably deionized water.
The polyester resin is preferably an acidic group-containing polyester resin. The polyester resin is preferably a polyester resin converted into a self-water dispersible resin by neutralizing the acidic groups. The acid value of the self-water dispersible polyester resin is preferably in the range of 1 to 20 mg KOH/g. The acidic groups of the self-water dispersible resin are neutralized with a basic neutralizer to form anionic groups. This increases the hydrophilicity of the resin. The resulting resin (anionic self-water dispersible polyester resin) can be stably dispersed in an aqueous medium without a dispersion stabilizer or a surfactant. Examples of the acidic group include acidic groups such as a carboxyl group, a sulfonic acid group, and a phosphoric acid group. Among them, a carboxyl group is preferred in view of charge properties of toner. Non-limiting examples of the basic compound used for neutralization include inorganic bases such as sodium hydroxide, potassium hydroxide, and ammonia; and organic bases such as diethylamine, triethylamine, and isopropylamine. Among them, the inorganic bases such as ammonia, sodium hydroxide, and potassium hydroxide are preferred. To disperse the polyester resin in an aqueous medium, there is a method in which a dispersion stabilizer such as a suspension stabilizer or a surfactant is added to the aqueous medium. However, the method for forming an emulsion by addition of the suspension stabilizer or the surfactant requires a high shearing force. Such an emulsion system is not preferred because of the formation of coarse particles and a broad particle size distribution. Therefore, preferably, the self-water dispersible resin is used, and the acidic groups of the resin are neutralized with the basic compound.
Examples of a method for neutralizing the acidic groups (carboxyl groups) of the polyester resin with the base include (1) a method including the steps of manufacturing a mixture of an acidic group-containing polyester resin, a coloring agent, a wax, and an organic solvent and then neutralizing the acidic groups with a base; and (2) a method including the steps of adding a basic neutralizer to an aqueous medium in advance and neutralizing the acidic groups of the polyester resin in the mixture during phase inversion emulsification. Methods of phase inversion emulsification include (A) an emulsifying method including a step of adding the mixture to an aqueous medium; and (B) an emulsifying method including a step of adding an aqueous medium to the mixture. A combination of the method (1) and the method (B) achieves a narrow particle size distribution, which is preferred.
In phase inversion emulsification, examples of high-shear emulsification apparatuses and continuous emulsification apparatuses that can be used include Homomixer (produced by Tokushu Kika Kogyo Co., Ltd.), Slasher (produced by Mitsui Mining Co., Ltd.), Cavitron (produced by Eurotec, Ltd.), Microfluidizer (produced by Mizuho Kogyo Co., Ltd.), Manton-Gaulin Homogenizer (produced by Gaulin Co.), Nanomizer (produced by Nanomizer Inc.), and Static Mixer (produced by Noritake Company). However, for example, a stirrer, an anchor blade, a turbine blade, a pfaudler blade, a full-zone blade, a max blend blade, a semicircular blade, or the like disclosed in JP-A-9-114135 is preferably used rather than the above-described high-shear emulsification apparatuses. Among them, a large blade such as the full-zone blade or the max blend blade capable of uniformly mixing a mixture is more preferred. In an emulsification step (phase inversion emulsification step) of forming fine particles of the mixture in an aqueous medium, the peripheral speed of the stirring blade is preferably in the range of 0.2 to 10 m/s. A method of adding water dropwise under low-shear stirring at a peripheral speed of 0.2 to less than 8 m/s is more preferred. Most preferably, the peripheral speed is in the range of 0.2 to 6 m/s. When the peripheral speed of the stirring blade is more than 10 m/s, the particle size in a dispersion formed during phase inversion emulsification is increased, which is not preferred. When the peripheral speed is less than 0.2 m/s, the stirring becomes nonuniform and nonuniform phase inversion is caused. As a result, coarse particles are readily formed, which is not preferred. The temperature during phase inversion emulsification is not particularly limited. Higher temperatures increase the number of coarse particles formed, which is not preferred. Excessively low temperatures increase the viscosity of the mixture containing the polyester resin and the organic solvent to increase the number of coarse particles formed, which is not preferred. The temperature during phase inversion emulsification is preferably in the range of 10 to 40° C. and more preferably 20 to 30° C.
Phase inversion emulsification is performed using the self-water dispersible resin under low shear, whereby the formation of a fine powder and coarse particles can be inhibited. Thus, in the subsequent coalescence step, aggregates of fine particles having a uniform particle size distribution are easily formed. In the case where a polyester resin not having self-water dispersibility is used or phase inversion emulsification is performed under high shear, the particle size distribution of the toner particles is broadened because of the formation of coarse particles and the formation of a fine powder composed of a low-molecular-weight component in the resin. Furthermore, the particles composed of the low-molecular-weight component are removed by screening in the subsequent step, which disadvantageously degrades the low-temperature fixing properties of the toner. The use of the self-water dispersible resin and the performance of phase inversion emulsification under low shear eliminate such problems.
The 50% volume-average particle size of the fine particles formed in the first step is preferably in the range of above 1 μm and 6 μm or less and more preferably above 1 μm and 4 μm or less. At a 50% volume-average particle size of 1 μm or less, in the case where the coloring agent and the release agent are used, they are insufficiently encapsulated in the polyester resin to adversely affect charge properties and development properties, which is not preferred. A large particle size limits the particle size of the resulting toner. Thus, the particle size of the fine particles formed in this step needs to be smaller than an intended particle size of the toner. A particle size of more than 6 μm is not preferred because coarse particles are easily formed. In the particle size distribution of the fine particles formed in the first step, the content of fine particles having a volume particle size of 10 μm or more is 2% or less and preferably 1% or less. The content of fine particles having a volume particle size of 5 μm or more is 10% or less and preferably 6% or less.
In a second step, the resulting fine particles obtained in the first step coalesce to form aggregates of the fine particles, and thus toner particles having a desired particle size are formed. In the second step, the amount of a solvent, temperature, the types and amounts of a dispersion stabilizer and an electrolyte, stirring conditions, and the like are appropriately controlled to obtain intended aggregates. There is widely known a method for manufacturing aggregates by forming fine particles by emulsion polymerization, coagulating the resulting fine particles, and fusing the coagulated particles by heating. Unlike the above-described method including two steps, the coagulating step and the fusing step, the manufacturing method (manufacturing method by coalescence) according to the invention includes a single step of simultaneously performing coagulation and fusion to form aggregates. In the method, spherical or substantially spherical particles can be obtained in a short time without heating.
In the second step, the resulting fine particle dispersion solution obtained in the first step is diluted with water to adjust the amount of the solvent. A dispersion stabilizer is then added thereto. An aqueous electrolyte solution is added dropwise thereto under the presence of the dispersion stabilizer to allow coalescence to proceed, whereby aggregates having a predetermined particle size are formed. The fine particles formed from the self-water dispersible resin in the first step are stably dispersed in an aqueous medium due to the effect of the electric double layer composed of a carboxylic acid salt. In the second step, the fine particles are destabilized by adding an electrolyte capable of destroying or reducing the electric double layer to the aqueous medium containing the fine particles dispersed therein.
Examples of the electrolyte include acidic materials such as hydrochloric acid, sulfuric acid, phosphoric acid, acetic acid, and oxalic acid. Furthermore, a water-soluble organic or inorganic salt such as sodium sulfate, ammonium sulfate, potassium sulfate, magnesium sulfate, sodium phosphate, sodium dihydrogenphosphate, sodium chloride, potassium chloride, ammonium chloride, calcium chloride, or sodium acetate may be effectively used. These electrolytes used for coalescence may be used alone or in combination. Among them, a sulfate of a monovalent cation such as sodium sulfate or ammonium sulfate is preferred in view of uniform coalescence. The resulting fine particles obtained in the first step are swollen with the solvent and become unstable because of the electric double layer shrunk by addition of the electrolyte. Therefore, even a collision of particles with each other even under low-shear stirring facilitates coalescence.
However, the addition of the electrolyte or the like alone results in nonuniform coalescence due to the unstable dispersion of the fine particles in the system, which produces coarse particles and aggregates. The aggregates of the fine particles formed by addition of the electrolyte and the acidic material may coalesce repeatedly to form aggregates each having a particle size of an intended particle size or more. To prevent this, an inorganic dispersion stabilizer such as hydroxyapatite or an ionic or nonionic surfactant needs to be added as a dispersion stabilizer before the addition of the electrolyte or the like. The dispersion stabilizer used needs to have a property to retain dispersion stability even under the presence of the electrolyte to be added. Examples of the dispersion stabilizer having such a property include nonionic emulsifiers such as polyoxyethylene nonyl phenyl ether, polyoxyethylene octyl phenyl ether, polyoxyethylene dodecyl phenyl ether, polyoxyethylene alkyl ether, polyoxyethylene fatty acid ester, sorbitan fatty acid ester, polyoxyethylene sorbitan fatty acid ester, and Pluronic; anionic emulsifiers such as alkyl sulfates; and cationic dispersion stabilizers such as quaternary ammonium salts. Among them, an anionic or nonionic dispersion stabilizer is preferred because even a small amount of the dispersion stabilizer can stabilize the dispersion in the system. The clouding point of the nonionic surfactant is preferably 40° C. or more. These surfactants may be used alone or in combination. The addition of the electrolyte under the presence of the dispersion stabilizer (emulsifier) can prevent nonuniform coalescence. As a result, a narrow particle size distribution is obtained and thus the yield is improved.
Stirring conditions during coalescence are important to achieve uniform coalescence. For example, a stirrer, an anchor blade, a turbine blade, a pfaudler blade, a full-zone blade, a max blend blade, a cone cape blade, a helical blade, a double helical blade, or a semicircular blade disclosed in JP-A-9-114135 is appropriately selected and used. Among them, a large blade such as the full-zone blade or the max blend blade capable of uniformly mixing a mixture is more preferred. The fine particles swollen with the solvent collide with each other under stirring and coalesce to form aggregates. Thus, the use of a high-shear apparatus such as a Homomixer including a stator and a rotor or the use of a stirring blade such as a turbine blade that locally applies high shear and has a low ability to uniformly stir the entirety results in nonuniform coalescence, leading to the formation of coarse particles. Thus, in the stirring conditions, the peripheral speed is preferably in the range of 0.2 to 10 m/s, more preferably 0.2 to less than 8 m/s, and particularly preferably 0.2 to 6 m/s. When the peripheral speed is more than 10 m/s, nonuniform coalescence is caused and coarse particles are easily formed, which is not preferred. When the peripheral speed is less than 0.2 m/s, nonuniform coalescence due to the lack of a shear force for stirring is caused and coarse particles are easily formed, which is not preferred. Only the collision between the fine particles facilitates coalescence, and the resulting aggregates subjected to coalescence are not dissociated or dispersed again. Therefore, ultrafine particles are hardly formed and a narrow particle size distribution is achieved, which improves the yield.
In the second step, if necessary, the resulting fine-particle dispersion solution obtained by phase inversion emulsification in the first step is preferably further diluted with water. The dispersion stabilizer and the electrolyte are successively added thereto to perform coalescence. Alternatively, the solvent content of the dispersion solution is preferably adjusted by adding an aqueous solution of the dispersion stabilizer and/or the electrolyte to obtain particles each having an intended particle size. The solvent content in the system after the addition of the electrolyte is preferably in the range of 5 to 25% by mass, more preferably 5 to 20% by mass, and particularly preferably 5 to 18% by mass. When the solvent content is less than 5% by mass, the amount of the electrolyte required for coalescence increases, which is not preferred. When the solvent content is more than 25% by mass, the amount of aggregates increases due to nonuniform coalescence and the amount of the dispersion stabilizer added also increases, which is not preferred.
The shape of the toner particles after coalescence can be controlled by adjusting the solvent content. When the solvent content is in the range of 13 to 25% by mass, spherical to substantially spherical fine particles are easily formed by coalescence because of a large degree of swelling of the fine particles with the solvent. When the solvent content is in the range of 5 to 13% by mass, deformed to substantially spherical fine particles are easily formed because of a small degree of swelling of the fine particles with the solvent.
The content of the dispersion stabilizer used is preferably in the range of 0.5 to 3.0% by mass, more preferably 0.5 to 2.5% by mass, and particularly preferably 1.0 to 2.5% by mass relative to the solid content of the fine particles. At a dispersion stabilizer content of less than 0.5% by mass, the intended effect of preventing the formation of coarse particles is not produced. At a dispersion stabilizer content of more than 3.0% by mass, even when the electrolyte content is increased, coalescence does not proceed sufficiently. Thus, particles each having a predetermined particle size are not formed. As a result, the fine particles are left and thus the yield is decreased, which is not preferred.
The content of the electrolyte used is preferably in the range of 0.5 to 15% by mass, more preferably 1 to 12% by mass, and particularly preferably 1 to 10% by mass relative to the solid content of the fine particles. At an electrolyte content of less than 0.5% by mass, coalescence does not proceed sufficiently, which is not preferred. An electrolyte content of more than 15% by mass results in nonuniform coalescence and thus the yield is decreased due to the formation of aggregates and coarse particles, which is not preferred.
The temperature during coalescence is preferably in the range of 10 to 50° C., more preferably 20 to 40° C., and particularly preferably 20 to 35° C. At a temperature of less than 10° C., coalescence does not easily proceed, which is not preferred. At a temperature of more than 50° C., the rate of coalescence is increased and thus aggregates and coarse particles are easily formed, which is not preferred. Therefore, it is possible to form aggregates by coalescence at a low temperature of 20 to 40° C.
In the first and second steps, various embodiments can be made. Preferred embodiments are as follows: (1) a method in which in the first step, the fine particles are manufactured using the resin solution containing the polyester resin, the coloring agent, and, if necessary, the release agent and the charge control agent, and then the second step (coalescence step) is performed; (2) a method in which in the first step, the fine particles are manufactured using the resin solution containing the polyester resin, the coloring agent, and, if necessary, the release agent, the charge-control-agent dispersion solution is added thereto, and then the second step (coalescence step) is performed; (3) a method in which in the first step, the fine particles composed of the polyester resin are manufactured, at least one of the coloring-agent dispersion solution and, if necessary, the release-agent dispersion solution and the charge-control-agent dispersion solution is separately prepared, they are mixed, and then the second step (coalescence step) is performed; (4) a method in which in the first step, the fine particles are manufactured using the resin solution containing the polyester resin and the release agent, the coloring-agent dispersion solution and, if necessary, the charge-control-agent dispersion solution are added thereto, and then the second step (coalescence step) is performed.
These dispersion solutions such as the coloring-agent dispersion solution, the charge-control-agent dispersion solution, and the release-agent dispersion solution can be prepared as follows. For example, each of the agents is added to water together with a nonionic surfactant such as a polyoxyethylenealkyl phenyl ether, an anionic surfactant such as an alkyl benzene sulfonate or an alkyl sulfate, or a cationic surfactant such as a quaternary ammonium salt, and then the mixture is mechanically pulverized with grinding media to prepare a dispersion solution corresponding to one of the dispersion solutions. Alternatively, the dispersion solution can be prepared in the same manner as described above under the presence of the basic neutralizer using the self-water dispersible polyester resin instead of the surfactant. For the coloring agent, the release agent, and the charge control agent used herein, each of them may be melt-kneaded with the polyester resin in advance. In this case, since a resin adsorbs the materials, the degree of exposure of the materials on the surfaces of the particles is reduced and desirable properties are imparted in terms of charge properties and development properties.
To retain satisfactory triboelectrification properties, it is effective to prevent the coloring agent and the like from being exposed to the surfaces of the toner base particles, that is, it is effective to provide a toner structure in which the coloring agent and the like are encapsulated in the toner base particles. The degradation of charge properties due to a reduction in the particle size of the toner is also caused by the fact that the coloring agent and other additives (e.g., a wax) are partially exposed to the surfaces of the toner base particles. Even if the content (% by mass) of the coloring agent or the like is the same, the surface area of the toner base particles increases as the particle size decreases. Furthermore, the percentages of the coloring agent, wax, and the like exposed to the surfaces of the toner base particles are increased. As a result, the composition of the surfaces of the toner base particles markedly changes, and the triboelectrification properties of the toner base particles markedly change, which makes it difficult to obtain proper charge properties.
In the toner base particles, the coloring agent, the wax, and the like are preferably encapsulated in the binder resin. This encapsulated structure provides a satisfactory printed image. To actively encapsulate the coloring agent and the release agent in the binder resin, the above-described method (1) or (2) is preferably employed. It can be easily determined, for example, by observing the cross section of the particles using a transmission electron microscope (TEM) that the coloring agent and wax are not exposed to the surfaces of the toner base particles. Specifically, the toner base particles are embedded in a resin and cut using a microtome. The resulting cross section is optionally stained with ruthenium oxide or the like. TEM observation demonstrates that the coloring agent and wax are encapsulated in the binder resin and dispersed in the particles almost uniformly. Furthermore, the method (2) is preferred in order to localize the charge control agent on the surfaces of the toner particles to provide the function thereof.
The shape of the aggregates of the fine particles obtained in the second step can be changed from an irregular shape to a spherical shape in accordance with the degree of coalescence. For example, the average circularity can be changed between 0.94 and 0.99. The average circularity can be determined by taking a scanning electron microscope (SEM) photograph of the toner particles obtained by drying the aggregates of the fine particles and then by performing measurements and calculations. However, the average circularity is more easily determined using a flow type particle image analyzer FPIA 2100 produced by SYSMEX Corporation.
The toner particles are spherical or substantially spherical. The toner particles preferably have an average circularity of 0.97 or more, whereby powder flowability and transfer efficiency are improved. When the shape of the toner particles approaches from a spherical shape to an irregular shape, the particles have poor flowability in a stirrer described below during the external addition treatment. The yield is reduced even if the peripheral speed of the stirring blade is reduced. Furthermore, the amount of positively charged toner particles is increased, and thus a charge distribution is disadvantageously broadened. When the shape of the toner particles approaches to the spherical shape, it is difficult to uniformly attach the external-additive particles to the toner base particles. Thus, the peripheral speed of the stirring blade needs to increase. This causes adhesion to the tip of the blade and the wall of the tank, which reduces the yield. Furthermore, the amounts of free external-additive particles and positively charged toner particles are increased, which broadens the charge distribution.
In a third step, an organic solvent is removed from a slurry, that is, the dispersion solution of the aggregates of the fine particles obtained in the second step. The slurry is filtered through a wet vibration screen to remove foreign matter such as resin pieces and coarse particles. Solid-liquid separation can be performed by a known method using a centrifuge, a filter press, a belt filter, or the like. Subsequently, by drying the particles, toner base particles can be obtained. Preferably, the toner base particles manufactured using an emulsifier and a dispersion stabilizer are sufficiently cleaned.
Any publicly known method can be employed as a drying method. Examples of the drying method include a method for drying the toner base particles at a normal pressure or a reduced pressure at a temperature at which the toner base particles are not heat-sealed or coagulated; a method for freeze-drying the toner base particles; and a method for simultaneously separating the toner base particles from the aqueous medium and drying the toner base particles using a spray dryer. In particular, examples of the effective and preferable drying method include a method for drying the toner base particles under the mixing of powder at a reduced pressure at a temperature at which the toner base particles are not heat-sealed or coagulated; and a method for drying the toner base particles using a Flush Jet Dryer (produced by Seishin Enterprise Co., Ltd.) that instantly dries an object with a dry heated airflow.
For the particle size distribution of the toner base particles, the ratio of 50% volume particle size to 50% number particle size measured using Multisizer TA III available from Beckman Coulter, Inc. is preferably 1.25 or less and more preferably 1.20 or less. At a ratio of 1.25 or less, a satisfactory image is easily obtained, which is preferred. Furthermore, GSD is preferably 1.30 or less and more preferably 1.25 or less. The term “GSD” refers to a value determined from the square root of (16% volume particle size/84% volume particle size) measured by Multisizer III available from Beckman Coulter, Inc. A lower GSD value results in a narrower particle size distribution, which provides a satisfactory image.
The volume-average particle size of the toner base particles is preferably in the range of 2 to 6 μm and more preferably in the range of 2 to 4 μm in view of the resulting image quality and the like. A smaller volume-average particle size improves definition and gradation and reduces the thickness of the toner layer for forming the printed image. Consequently, the effect of reducing the amount of the toner to be consumed per page is produced, which is preferable.
The synthesis example and physical properties of the polyester resin and the synthesis example of the toner base particles will now be described. The term “part” means a part by mass, and the term “water” means deionized water, unless otherwise specified.
In a separable flask, terephthalic acid (TPA) and isophthalic acid (IPA) as the divalent carboxylic acid, polyoxypropylene(2.4)-2,2-bis(4-hydroxyphenyl)propane (BPA-PO) and polyoxyethylene(2.4)-2,2-bis(4-hydroxyphenyl)propane (BPA-EO) as the aromatic diol, ethylene glycol (EG) as the aliphatic diol, and trimethylolpropane (TMP) as the aliphatic triol were placed at each molar ratio shown in Table 1, and 0.3% by mass of tetrabutyltitanate as the polymerization catalyst was placed thereto relative to the total amount of the monomers. The flask was equipped with a thermometer, a stirrer, a condenser, and a nitrogen introducing tube at the upper portion thereof. The mixture was subjected to reaction in an electric mantle heater at 220° C. for 15 hours in a nitrogen gas flow at normal pressure. After gradual evacuation, the reaction was continued at 10 mmHg. The reaction was monitored by measuring the softening point in accordance with the ASTM•E28-517 standard. The reaction was ended by terminating the evacuation when the softening point reached a predetermined temperature. Table 1 shows the composition and values of the physical properties (values of properties) of the thus-synthesized resin.
In Table 1,
>600,000: the area ratio of a component having a molecular weight of 600,000 or more.
<10,000: the area ratio of a component having a molecular weight of 10,000 or less
TPA: terephthalic acid
IPA: isophthalic acid
BPA-PO: polyoxypropylene(2.4)-2,2-bis(4-hydroxyphenyl)propane
BPA-EO: polyoxyethylene(2.4)-2,2-bis(4-hydroxyphenyl)propane
EG: ethylene glycol
TMP: trimethylolpropane
FT value: a value measured by a flow tester
In Table 1, the term “T1/2 temperature” means, as described above, a value measured using a flow tester (CFT-500 produced by Shimadzu Corporation) with a nozzle having a diameter of 1.0 mm and a length of 1.0 mm by applying a load of 10 kg per unit area (cm2) at a heating speed of 6° C./min. The term “glass transition temperature Tg (° C.)” means a value measured at a heating rate of 10° C./min by the second-run method using a differential scanning calorimeter (DSC-50 produced by Shimadzu Corporation).
First, 50 parts of carnauba wax (Carnauba wax No. 1, product imported by Kato Yoko) and 50 parts of a polyester resin (R1 in Table 1) were kneaded using a pressure kneader. The kneaded mixture and 185 parts of methyl ethyl ketone were placed in a ball mill. After stirred for 6 hours, the mixture was taken out from the ball mill. The solid content was adjusted to 20% by mass to obtain a release-agent microdispersion solution (W1).
According to the composition shown in Table 2, a color pigment and a resin were kneaded in a ratio by weight of 50/50 to prepare a coloring-agent masterchip. The color pigment and the resin were kneaded using a twin roll. The resulting kneaded mixture and methyl ethyl ketone were placed in a ball mill such that the solid content was 40% by mass. After stirred for 36 hours, the mixture was taken out from the ball mill. The solid content was adjusted to 20% by mass to obtain a coloring-agent dispersion solution.
The coloring agent shown in Table 2 is described below.
Cyan pigment: Fastogen Blue TGR (produced by Dainippon Ink and Chemicals, Inc.)
The release-agent dispersion solution, the coloring-agent dispersion solution, the dilution resin (additional resin), and methyl ethyl ketone were mixed using Despa. The solid content was adjusted to 55% to obtain a mill base. Table 3 shows the composition of the mill base.
Table 4 shows properties of the resin mixture shown in Table 3. The resin particles passing through 200 mesh were mixed at the above-described ratio by weight, and the properties were measured.
In Table 4,
>600,000: the area ratio of a component having a molecular weight of 600,000 or more.
<10,000: the area ratio of a component having a molecular weight of 10,000 or less
First, 545.5 parts of the mill base and 23.8 parts of 1N aqueous ammonia were placed in a 2 L cylindrical separable flask provided with a max blend blade as a stirring blade. The mixture was thoroughly stirred at 350 rpm using a Three-One Motor. Subsequently, 133 parts of deionized water was added thereto. The resulting mixture was further stirred and the temperature of the mixture was set to 30° C. Under the same conditions, 133 parts of deionized water was added dropwise to form a fine particle dispersion by phase inversion emulsification. In this case, the peripheral speed of the stirring blade was 1.19 m/s. Next, 333 parts of deionized water was added thereto to adjust the solvent content.
Subsequently, 4.1 parts of Epan 450 (produced by Dai-Ichi Kogyo Seiyaku Co., Ltd.) as a nonionic emulsifier was diluted with water and added to the fine particle dispersion. The temperature of the mixture was set to 30° C. The number of revolutions was set to 250 rpm. Next, 410 parts of 3% aqueous ammonium sulfate solution was added dropwise thereto to adjust the solvent content in the dispersion solution to 15.5% by mass. Under the same conditions, the stirring was continued for 70 minutes to complete coalescence. In this case, the peripheral speed was 0.85 m/s. Solid-liquid separation was performed on the resulting slurry using a centrifuge. The resulting solid was cleaned and then dried using a vacuum dryer to obtain toner base particles. Table 5 shows the properties of the toner base particles.
The particle size and the particle size distribution were measured using Multisizer III available from Beckman Coulter, Inc. with a 100 μm aperture tube. The term “Dv50” means a 50% volume-average particle size. The term “Dv50/Dn50” means the ratio of the 50% volume-average particle size to the 50% number-average particle size. The term “GSD” means a value determined from the square root of (16% volume particle size/84% volume particle size).
The 50% volume-average particle size (D50) of the colored particles (toner base particles) of the invention is 2.0 to 6.0 μm and preferably 2.0 to 4.0 μm. At an average particle size of 6.0 μm or less, even if a latent image is formed at a high resolution of 600 dpi or higher, good reproducibility of resolution can be achieved. At an average particle size of 2.0 μm or less, the hiding power of toner is degraded due to a decrease in a development efficiency. Furthermore, the amount of the external additive used is increased in order to improve flowability, which tends to decrease the fixing property.
The toner base particles preferably have a shape close to a spherical shape. Specifically, the toner base particles have an average circularity (R) of 0.94 to 0.99 and preferably 0.97 to 0.98, the average circularity being represented by the following formula:
R=L
0
/L
1
where L1 (μm) is a circumference of a projected image of a toner particle measured and L0 (μm) is a circumference of a perfect circle (geometrically perfect circle) having an area equal to a projected image of a toner particle measured. Thus, there can be provided toner that causes less variation in transfer efficiency during continuous printing and has a high transfer efficiency, a sufficient charge quantity, and ease of cleaning. The circularity of the toner base particles is measured using a flow type particle image analyzer FPIA 2100 produced by SYSMEX Corporation.
External-additive particles of the invention will now be described. The average particle size (may be simply referred to as “particle size”) of the external-additive particles is determined by observing the particles using a transmission electron microscope and measuring the particle sizes of 100 particles in a field of view. The BET specific surface area is determined using an automatic surface area analyzer Macsorb HM model-1201 available from Mountech Co., Ltd.
Examples of small particle size silica having a primary particle size of 7 to 15 nm and preferably 10 to 12 nm include R8200 available from NIPPON AEROSIL Co., Ltd. (bulk density: 0.1 to 0.2 g/cm3, two-component charge quantity (5-minute value): −20 to −80 μC/g) and RX200 available from NIPPON AEROSIL Co., Ltd. (bulk density: 0.02 to 0.06 g/cm3, two-component charge quantity (5-minute value): −100 to −300 μC/g). Both of them can be obtained by vapor phase oxidation (dry method) of silicon halide compounds and are different from each other in terms of the bulk density and two-component charge quantity (5-minute value).
In the hydrophobic small silica particles, the flowability of the toner obtained increases as the primary particle size decreases. However, when the number-average primary particle size is less than 7 nm, the silica fine particles may be buried between toner base particles during external addition. In contrast, when the primary particle size is more than 16 nm, the flowability may decrease. The hydrophobic small silica particles are added to 100 parts by mass of toner base particles at an amount of 0.5 to 3.0 parts by mass and preferably 1.0 to 2.0 parts by mass.
The bulk density is obtained by inserting powder into a 100 ml graduated cylinder using a funnel until the volume reaches 100 ml, measuring the weight, and substituting the weight into the following formula:
Bulk density(g/cm3)={(weight after sample is inserted)−(weight before sample is inserted)}/{volume of graduated cylinder(100 ml)}
Large particle size silica has a primary particle size of 50 to 400 nm. The large particle size silica has a spherical shape with a Wadell's sphericity of 0.6 or more and preferably 0.8 or more. The large particle size silica is obtained by a sol-gel method that is a wet method, and the specific gravity is 1.3 to 2.1. When the average particle size is less than 50 nm, a spacer effect is not produced and the maintenance of the flowability and charge stability achieved by preventing silica fine particles with a small particle size from being buried onto the surface of toner base particles cannot be achieved. When the average particle size is more than 400 nm, the large particle size silica is not easily attached to toner base particles and is easily detached from the surface of the toner base particles.
SEAHOSTAR KE-P10S available from NIPPON SHOKUBAI Co., Ltd. is exemplified as the large particle size silica. SEAHOSTAR is amorphous (but may be partially crystalline) and is hydrophobized with silicone oil, and has a spherical shape, a primary particle size of 100 nm, an absolute specific gravity of 2.2, a bulk density of 0.25 to 0.35, a BET specific surface area of 10 to 14 m2/g, and a two-component charge quantity (5-minute value) of 0 to −50 μC/g.
The large particle size silica is added to 100 parts by mass of toner base particles at an amount of 0.2 to 2.0 parts by mass and preferably 0.5 to 1.5 parts by mass. When the amount of the large particle size silica added is less than 0.2 parts by mass, the packing density of toner increases. Consequently, when a toner layer is regulated to be thin using a regulating blade during the rotation of a developing roller, the toner layer is not easily thinned, which poses problems such as leakage during regulation and scattering. When the amount is more than 2.0 parts by mass, the packing density of toner excessively decreases. Consequently, when a toner layer passes through a regulating blade during the rotation of a developing roller, part of the toner leaks out without being held by the developing roller. Furthermore, because of the variation in the thickness of a toner layer formed that occurs in a developing roller cycle, the uniformity of the concentration in a direction of sheet feeding is impaired when a full page solid image is output, which poses a problem such as unevenness due to a developing roller cycle.
The addition ratio (by mass) of the large particle size silica to the small particle size silica is 1:4 to 4:1 and preferably 2:3 to 3:2. In that ratio, the flowability is imparted to toner and the long-term charge stability is achieved. The total amount of the large particle size silica and the small particle size silica is 1.25 to 5.0 parts by mass and preferably 2.0 to 3.0 parts by mass relative to 100 parts by mass of toner base particles while the addition ratio thereof is taken into account.
The silica fine particles are preferably hydrophobized. By hydrophobizing the surface of silica fine particles, the flowability and charge properties of the toner are further improved. The silica fine particles can be hydrophobized by a wet or dry method normally employed by a person skilled in the art, using a silane compound such as hexamethyldisilazane or dimethyldichlorosilane; or a silicone oil such as dimethyl silicone, methyl phenyl silicone, a fluorine-modified silicone oil, an alkyl-modified silicone oil, or an epoxy-modified silicone oil.
The silica fine particles may be positively charged. The positively charged silica fine particles have a primary particle size of 20 to 40 nm. The positively charged silica fine particles are preferably hydrophobized, and added in order to decrease the variation in charge properties with respect to the change of an external environment, maintain stable charge properties, and improve the flowability of toner. The positively charged silica fine particles are hydrophobized with an aminosilane coupling agent, an amino-modified silicone oil, or the like. Examples of the hydrophobized positively charged silica fine particles include commercially available NA50H produced by NIPPON AEROSIL Co., Ltd. and TG820F produced by Cabot Corporation. NA50H is amorphous and is hydrophobized with hexamethyldisilazane and aminosilane, and has a spherical shape, a number-average primary particle size of 30 nm, an absolute specific gravity of 2.2, a bulk density of 0.0671, a BET specific surface area of 44.17 m2/g, a carbon amount of 2% or less, and a two-component charge quantity (5-minute value) of 40 μC/g.
In the invention, at least one type of electron-conductive oxide semiconductor fine particles selected from titania, transition alumina, zinc oxide, and tin oxide and at least one type of ion-conductive oxide semiconductor fine particles selected from cerium oxide and stabilized zirconia are further added as the external additives.
The electron conduction speed is higher than the ion conduction speed, whereby electron-conductive oxide semiconductor fine particles have a better effect of charging the charged sites on the surface of toner uniformly at a high speed. Thus, it is believed that, by decreasing the particle size of the electron-conductive oxide semiconductor fine particles, the charge reception/provision with minute charged sites represented by the small particle size silica is activated. On the other hand, for charged paths connecting toner particles, ion-conductive oxide semiconductor fine particles are added as a charge-leaking external additive having a particle size larger than that of the small particle size silica that represents charged sites, whereby uniform electrification occurs to some extent due to the electron conduction between the charged sites on the surface of each of the toner particles and then uniform electrification between the toner particles occurs. As a result, good charge properties can be achieved across the entire toner and bulk.
Accordingly, the ion-conductive oxide semiconductor fine particles preferably have a larger particle size than the electron-conductive oxide semiconductor fine particles. Specifically, the electron-conductive oxide semiconductor fine particles preferably have an average particle size of 7 to 30 nm and the ion-conductive oxide semiconductor fine particles preferably have an average particle size of 50 to 400 nm. Preferably, the amount of the ion-conductive oxide semiconductor fine particles added is 0.5 to 2.5 parts by mass and the amount of the electron-conductive oxide semiconductor fine particles added is 0.3 to 2.0 parts by mass relative to 100 parts by mass of toner base particles while the addition amount of the ion-conductive oxide semiconductor fine particles is larger than that of the electron-conductive oxide semiconductor fine particles. When the addition amount is larger than the above-described amount, a charge-leaking effect is excessively produced and a free external additive appears. When the amount is smaller than the above-described amount, a desired effect is not achieved.
The electron-conductive oxide semiconductor fine particles are composed of at least one selected from titania, transition alumina, zinc oxide, and tin oxide having an average particle size of 7 to 30 nm.
Examples of titania include STT30S available from Titan Kogyo, Ltd. having a primary particle size of 15 nm and STR100A available from Titan Kogyo, Ltd. having a primary particle size of 30 nm.
For the transition alumina, θ-alumina, γ-alumina, δ-alumina, and η-alumina can favorably fulfill such a function. In particular, transition alumina mainly composed of θ-alumina and γ-alumina is preferred. Examples of the method for manufacturing transition alumina include a dawsonite method, a direct current arc plasma method, and a high-temperature flame hydrolysis deposition method, and θ-alumina obtained by a dawsonite method is preferred. Examples of the transition alumina obtained by a dawsonite method include TAIMICRON TM-100 (Al2O3) whose main phase is a θ-alumina phase and that has a primary particle size of 14 nm and a BET specific surface area of 132 m2/g (TAIMEI CHEMICALS Co., Ltd.) and TAIMICRON TM-300 (Al2O3) whose main phase is a γ-alumina phase and that has a primary particle size of 7 nm and a BET specific surface area of 225 m2/g (TAIMEI CHEMICALS Co., Ltd.). An example of the transition alumina obtained by a direct current arc plasma method is Nano•Tek having a γ-alumina phase as a main phase, a primary particle size of 30 nm, and a BET specific surface area of 49.3 m2/g (C. I. Kasei Company, Limited). An example of the transition alumina obtained by a high-temperature flame hydrolysis deposition method is C805 having a γ-alumina phase as a main phase and a δ-alumina phase and a primary particle size of 13 nm (NIPPON AEROSIL Co., Ltd.).
Examples of zinc oxide include FINEX-50S-LP2 having a primary particle size of 20 nm and FINEX-50W-LP2 having a primary particle size of 20 nm (Sakai Chemical Industry Co., Ltd.).
An example of tin oxide is Nano•Tek SnO2 having a primary particle size of 20 nm (C. I. Kasei Company, Limited).
The amount of the electron-conductive oxide semiconductor fine particles added is 0.3 to 2.0 parts by mass and preferably 0.5 to 1.5 parts by mass relative to 100 parts by mass of toner base particles.
The ion-conductive oxide semiconductor fine particles are composed of a material selected from cerium oxide and stabilized zirconia each having an average particle size of 50 to 400 nm.
Examples of cerium oxide include Type S having a primary particle size of 50 to 100 nm (Anan Kasei Co., Ltd.), AU having a primary particle size of 50 to 100 nm (Shin-Etsu Chemical Co., Ltd.), and UU having a primary particle size of 20 to 50 nm and a particle size of sintered aggregates of 200 to 400 nm (Shin-Etsu Chemical Co., Ltd.).
An example of stabilized zirconia is yttria stabilized zirconia (YSZ) that is excellent in ion conductivity and has a primary particle size of 400 nm.
The electron-conductive oxide semiconductor fine particles and the ion-conductive oxide semiconductor fine particles may be hydrophobized with an organic silane compound such as alkylalkoxysilane, siloxane, silane, or silicone oil. In particular, alkylalkoxysilane is preferably used. Examples of the alkylalkoxysilane include vinyltrimethoxysilane, vinyltriethoxysilane, γ-methacryloxypropyltrimethoxysilane, vinyltriacetoxysilane, methyltrimethoxysilane, methyltriethoxysilane, isobutyltrimethoxysilane, dimethyldimethoxysilane, dimethyldiethoxysilane, trimethylmethoxysilane, hydroxypropyltrimethoxysilane, phenyltrimethoxysilane, n-hexadecyltrimethoxysilane, and n-octadecyltrimethoxysilane.
The external additive may be added to toner base particles using a Henschel mixer (available from MITSUI MIIKE MACHINERY Co., Ltd.), a Q-type mixer (available from MITSUI MINING COMPANY, Limited), a Mechanofusion system (available from Hosokawa Micron Corporation), or a Mechanomill (available from OKADA SEIKO Co., Ltd.). When multistage processing is performed using a Henschel mixer, the operation conditions at each stage are selected from a peripheral speed of 30 to 50 m/s and a processing time of 2 to 15 minutes.
The multistage processing may be constituted by two stages of the additions of the external additives. At a first stage, the external additives having a large particle size are processed to the toner base particles. At a second stage, the external additives having a small particle size are processed and attached to the toner base particles. Thus, the flowability achieved by the small particle size silica and the functions of the small and the large particle size aluminas and cerium oxide having a large particle size are ensured even if printing is performed for a long time. One of the reasons for this can be considered as follows, but is not limited to the mechanism. That is, it is believed that a structure in which small silica particles as charged sites are present together with electron-conductive oxide semiconductor fine particles as charged paths that connect the charged sites is formed while ion-conductive oxide semiconductor fine particles and larger silica particles are attached to toner base particles without being buried between the toner base particles, whereby the function as charged paths between toner particles and a spacer effect are easily achieved.
In the invention, other hydrophobized external additives may be added as long as the purpose of the addition of the external-additive particles is not defeated. Examples of the other hydrophobized external additives include hydrophobic medium silica particles (fumed silica RX50 available from NIPPON AEROSIL Co., Ltd., absolute specific gravity: 2.2, volume-average particle size D50: 40 nm (standard deviation=20 nm)); magnesium stearate, calcium stearate, zinc stearate, aluminum monostearate, and aluminum tristearate that are each a metal salt of a higher fatty acid which is a metallic soap particle, the metal being selected from magnesium, calcium, and aluminum; fine particles of metal oxides such as strontium oxide, magnesium oxide, and indium oxide; fine particles of nitrides such as silicon nitride; fine particles of carbides such as silicon carbide; resin particles; fine particles of metal salts such as calcium sulfate, barium sulfate, calcium carbonate, and strontium titanate; and inorganic fine particles such as a complex of the foregoing.
In the toner of the invention, the flow softening temperature (Tf1/2) is in the range of 90 to 140° C. and the glass transition temperature (Tg) is in the range of 40 to 70° C. The flow softening temperature (Tf1/2) is determined with a flow tester (CFT-500 available from Shimadzu Corporation). The measurement is performed using a nozzle having a diameter of 1.0 mmΦ and a length of 1.0 mm at a heating rate of 6° C./min while a load of 10 kg per unit area (cm2) is applied. The glass transition temperature (Tg) is determined at a heating rate of 10° C./min by a second-run method using a differential scanning calorimeter (DSC-220C available from Seiko Instruments Inc.).
A method for forming an image and an image forming apparatus of the invention will now be described.
The photo-conductor 20 has a cylindrical conductive material and a photosensitive layer formed on the outer surface of the conductive material, and can rotate clockwise about the central axle as indicated by an arrow. The charging unit 30 is used for charging the photo-conductor 20. The exposure unit 40 is used for forming a latent image on the charged photo-conductor 20 by irradiation with laser beams. The exposure unit 40 irradiates the charged photo-conductor 20 with modulated laser beams in accordance with an image signal. By turning the laser beams on and off at a predetermined timing while rotating the photo-conductor 20 at a predetermined speed, dot latent images are formed on the photo-conductor 20 in regions partitioned in a grid pattern.
The developer container holder 50 is used for developing the latent image formed on the photo-conductor 20 using black (K) toner accommodated in a black developer container 51, magenta (M) toner accommodated in a magenta developer container 52, cyan (C) toner accommodated in a cyan developer container 53, and yellow (Y) toner accommodated in a yellow developer container 54. In the developer container holder 50, the positions of the developer containers 51, 52, 53, and 54 can be moved by rotating the developer container holder 50. For each time the photo-conductor 20 rotates 360 degrees, one of the developer containers 51, 52, 53, and 54 selectively faces the photo-conductor 20, and a latent image formed on the photo-conductor 20 is developed in sequence using the toner accommodated in one of the developer containers 51, 52, 53, and 54 that faces the photo-conductor 20.
The primary transfer unit 60 is used for transferring a single-color toner image formed on the photo-conductor 20 to the intermediate transfer belt 70. When four-color toners are transferred so as to overlap with each other, a full-color toner image is formed on the intermediate transfer belt 70. The intermediate transfer belt 70 is an endless belt and is rotated at substantially the same peripheral speed as that of the photo-conductor 20. The secondary transfer unit 80 is used for transferring the single-color toner image or the full-color toner image formed on the intermediate transfer belt 70 to a recording medium such as a sheet, a film, or a cloth.
The fixing unit 90 is used for fixing the single-color toner image or the full-color toner image transferred onto the recording medium such as a sheet by fusion to form a permanent image. The cleaning unit 75 is disposed between the primary transfer unit 60 and the charging unit 30, and includes a cleaning blade 76 made of rubber that is in contact with the surface of the photo-conductor 20. After the toner image is transferred onto the intermediate transfer belt 70 using the primary transfer unit 60, the cleaning unit 75 is used for removing toner T left on the photo-conductor 20 by scraping it using the cleaning blade 76.
The developer container holder 50 includes the black developer container 51 that accommodates black (K) toner, the magenta developer container 52 that accommodates magenta (M) toner, the cyan developer container 53 that accommodates cyan (C) toner, and the yellow developer container 54 that accommodates yellow (Y) toner. Since the structure of each of the developer containers is the same, only a structure of the cyan developer container 53 is described below.
The housing 540 is made by welding an upper housing portion 542 to a lower housing portion 544, each of which is composed of a resin and integrally formed. Inside the housing 540, a toner container 530 is formed for accommodating the toner T. The toner container 530 is divided into two toner containers, that is, a first toner container 530a and a second toner container 530b through a partition wall 545 that protrudes inward from the inner wall (in an up-down direction of
The upper portions of the first toner container 530a and the second toner container 530b communicate with each other. In the state shown in
The toner supplying roller 550 includes a roller portion 550a composed of, for example, urethane foam with elasticity and an axle body 550b about which the roller portion 550a rotates. The toner supplying roller 550 is supported by the housing 540 at both ends of the axle body 550b, whereby the toner supplying roller 550 is supported rotatably about the axle body 550b. The roller portion 550a is accommodated in the first toner container 530a of the housing 540 (in the housing 540) and supplies the toner T accommodated in the first toner container 530a to the developing roller 510. The toner supplying roller 550 is disposed under the first toner container 530a in a vertical direction. The toner T accommodated in the first toner container 530a is supplied to the developing roller 510 through the toner supplying roller 550 at the lower portion of the first toner container 530a. The toner supplying roller 550 also removes toner T excessively left on the developing roller 510 after development from the developing roller 510.
The toner supplying roller 550 and the developing roller 510 are attached to the housing 540 while both rollers are pressed against each other. Therefore, the roller portion 550a of the toner supplying roller 550 is in contact with the developing roller 510 while being elastically deformed. The toner supplying roller 550 rotates in a direction (in a clockwise direction in
The developing roller 510 carries the toner T and transfers it to a developing position that faces the photo-conductor 20. The developing roller 510 is composed of a metal such as an aluminum alloy including a 5056 aluminum alloy or a 6063 aluminum alloy or an iron alloy including carbon steel for machine structural purpose (STKM). If necessary, nickel plating or chromium plating may be performed on the developing roller 510. On the surface of the developing roller 510, a spiral groove is formed at the central portion in the axis direction of the developing roller 510. The surface profile of the developing roller 510 will be described later.
The developing roller 510 is supported at both ends in the longitudinal direction thereof, and thus can rotate about the central axle thereof. As shown in
As shown in
The regulating blade 560 provides a charge to the toner T carried by the developing roller 510 and regulates the layer thickness of the toner T. The regulating blade 560 includes a rubber portion 560a and a rubber supporting portion 560b. The rubber portion 560a is composed of silicon rubber, urethane rubber, or the like and the rubber supporting portion 560b is a thin plate composed of phosphor bronze, stainless steel, or the like and having a characteristic of spring. The rubber portion 560a is supported by the rubber supporting portion 560b at one end in the transverse direction of the rubber supporting portion 560b so as to extend in the longitudinal direction of the rubber supporting portion 560b. The rubber supporting portion 560b is attached to the housing 540 through a blade supporting metal sheet 562 while supported by the blade supporting metal sheet 562 at the other end thereof. Furthermore, a blade rear member 570 composed of moltopren is disposed on the side of the regulating blade 560 opposite the developing roller 510 side.
In the invention, a regulation bias for imparting a charge to the toner T is applied between the regulating blade 560 and the developing roller 510. A potential difference of 70 to 400 V, preferably 100 to 300 V, is provided as the regulation bias. When negatively charged toner is used, the layer thickness of the toner is regulated while the regulating blade 560 has a large negative potential with respect to the developing roller 510. If an alternating voltage is applied to the developing roller, an alternating voltage synchronized therewith may be applied to the regulating blade so that a predetermined potential difference is provided.
The rubber portion 560a is pressed against the developing roller 510 from the central portion to both end portions of the developing roller 510 by the elastic force exerted due to the bending of the rubber supporting portion 560b. The blade rear member 570 prevents the toner T from entering a space between the rubber supporting portion 560b and the housing 540 and stabilizes the elastic force exerted due to the bending of the rubber supporting portion 560b. Furthermore, the blade rear member 570 urges the rubber portion 560a in the direction from the back of the rubber portion 560a toward the developing roller 510, whereby the rubber portion 560a is pressed against the developing roller 510. Thus, the rubber portion 560a is brought into contact with the developing roller 510 more uniformly because of the blade rear member 570.
The end of the regulating blade 560 on the side opposite the side on which the regulating blade 560 is supported by the blade supporting metal sheet 562, that is, the free end is not in contact with the developing roller 510. Only a portion having a certain width and that is spaced apart from the free end by a certain distance is in contact with the developing roller 510. In other words, the edge of the regulating blade 560 is not in contact with the developing roller 510, and the flat surface of the rubber portion 560a is in contact with the developing roller 510. The regulating blade 560 is disposed such that the free end is oriented in the upstream direction of the rotation of the developing roller 510, that is, the regulating blade 560 is in so-called counter contact with the developing roller 510. The regulating blade 560 is in contact with the developing roller 510 at a position lower than that of the central axle of the developing roller 510 and also lower than that of the central axle of the toner supplying roller 550.
The rubber supporting portion 560b is disposed so as to be longer than the rubber portion 560a in the axis direction of the developing roller 510, and extends outward from both ends of the rubber portion 560a. In the extending region of the rubber supporting portion 560b, the end seal 527 having a thickness larger than that of the rubber portion 560a and composed of a nonwoven fabric or the like is attached to the surface on the same side as the rubber portion 560a. Herein, the end face of the rubber portion 560a in the axis direction of the developing roller 510 is in contact with the side face of the end seal 527.
The end seal 527 is disposed so as to be in contact with both end portions of the developing roller 510 when the developing roller 510 is mounted. Both the end portions are portions of the surface where a groove is not formed. The end seal 527 has a width that protrudes outward from the end portions of the developing roller 510. The end seal 527 extends from the free end of the rubber portion 560a of the regulating blade 560 by a sufficiently long distance. When the regulating blade 560 is attached to the housing 540, the end seal 527 is disposed along the portion of the housing 540 formed so as to face the outer surface of the developing roller 510, to seal the gap between the housing 540 and the developing roller 510.
The upper seal 520 prevents the toner T accommodated in the cyan developer container 53 from leaking to the outside of the cyan developer container 53, and collects the toner T, on the developing roller 510, that has passed through the developing position into the developer container without scraping it. The upper seal 520 is composed of a polyethylene film or the like. The upper seal 520 is supported by a seal supporting metal sheet 522, and attached to the housing 540 through the seal supporting metal sheet 522. Furthermore, a seal urging member 524 composed of moltopren or the like is disposed on the side of the upper seal 520 opposite the developing roller 510 side. The upper seal 520 is pressed against the developing roller 510 by the elastic force of the seal urging member 524. The upper seal 520 is in contact with the developing roller 510 at a position higher than that of the central axle of the developing roller 510.
In the cyan developer container 53 having such a structure, the toner supplying roller 550 supplies the toner T accommodated in the toner container 530 to the developing roller 510. The toner T supplied to the developing roller 510 reaches a contact position with the regulating blade 560 as the developing roller 510 rotates. When the toner T passes through the contact position, a charge is provided to the toner T and the layer thickness of the toner T is regulated.
The charged toner T on the developing roller 510 reaches a developing position that faces the photo-conductor 20 as the developing roller 510 further rotates, and is used for development of the latent image formed on the photo-conductor 20 under an alternating electric field at the developing position. The toner T, on the developing roller 510, that has passed through the developing position due to the further rotation of the developing roller 510 passes through the upper seal 520 and is collected into the developer container without being scraped by the upper seal 520. The toner T still left on the developing roller 510 is removed by the toner supplying roller 550.
The developing roller 510 has projections and depressions for carrying toner particles at the central portion 510a in the axis direction and also has smooth surfaces at both end portions 510b such that the end seals 527 are brought into close contact with the end portions 510b.
As shown in
That is, the first groove 511a is formed in a spiral shape so as to be inclined clockwise by 45° with respect to the axle of the developing roller 510. The second groove 511b is formed in a spiral shape so as to be inclined counterclockwise by 45° with respect to the axle of the developing roller 510. Therefore, the first groove 511a and the second groove 511b intersect each other at 90°. Since the pitches of the first and second grooves 511a and 511b in the axis direction of the developing roller 510 are equally formed, the top face 512a of the projection 512 surrounded by the first and second grooves 511a and 511b has a substantially square shape.
As shown in
The two types of the groove 511 are each formed such that the depth of the groove 511, that is, the distance from the top face 512a of the projection 512 to the bottom face 511c of the groove 511 is constant, specifically about 7 μm. When the volume-average particle size of the toner is 3 μm, the depth of the groove 511 is set to 2 times or less the volume-average particle size of the toner.
Such a developing roller 510 is formed by rolling.
The developing roller 510 is formed of a cylindrical hollow material. First, the cylindrical material is cut into cylindrical members 515 each having a sufficient length such that the central portion 510a for carrying toner and the end portions 510b brought into contact with the end seal 527 can be formed (S001). In the cylindrical member 515, a step 510c (
Next, the flange 513 having the shaft 513b is inserted into the cylindrical member 515 in which the step 510c has been formed on the inner surface of each of the end portions such that the shaft 513b protrudes outward from the cylindrical member 515 (S003).
Subsequently, the cylindrical member 515 into which the flange 513 is inserted rotates about an axle formed by supporting the shafts 513b of both end portions of the cylindrical member 515, whereby the entire outer surface of the cylindrical member 515 is cut by a small amount. Consequently, the surface of the cylindrical member 515 is ground such that the entire region on the surface is made concentric with the axle, that is, the distance L from the axle is made constant, to form a non-rolled developing roller 509 (S004).
In the cylindrical member 515 whose surface has been ground, two types of grooves 511a and 511b are formed on the surface by rolling using an apparatus including dies 900 as processing tools shown in
Toner is supplied from the toner supplying roller 550 to a region between the end seals 527 brought into contact with the end portions 510b of the developing roller 510. The layer thickness of the toner layer is regulated at a pressing position of the regulating blade 560. In this case, the regulating blade 560 presses the developing roller 510 over the end portions 510b and the central portion 510a. However, since the end portions 510b of the developing roller 510 and the top face 512a of the projection 512 are at the same distance L from the axle C, the regulating blade 560 presses the developing roller 510 while remains substantially flat without being significantly bended. Therefore, an excessively large gap is not formed between the surface 510d of the developing roller 510 and the regulating blade 560, for example, even at the boundary between the end portions 510b and the central portion 510a.
Furthermore, since the depth of the groove 511 is two times or less the volume-average particle size of the toner particles T, more than two toner particles are never stacked in the depth direction at any position in the groove 511. In other words, a large amount of toner particles does not enter the groove 511. When the regulating blade 560 presses the developing roller 510, most of the toner particles are brought into contact with at least one of the surface 510d of the developing roller 510 and the surface of the regulating blade 560. Therefore, the toner particles T are easily rolled, and can be charged appropriately because the toner particles T do not easily remain in the groove 511. Thus, the toner particles are carried by the developing roller 510 with certainty and used for development. In addition, since an excessively large gap is not formed between the surface 510d of the developing roller 510 and the regulating blade 560, the toner particles T can be prevented from leaking to the outside of the developer containers 51, 52, 53, and 54.
If depressions and projections having a nonuniform size, depth, shape, and the like are formed on the surface 510d of the developing roller 510, the carried toner particles T that have entered deep depressions are not easily rolled and charged. If the groove is formed in the circumferential direction at a certain pitch in the axis direction, the relative position of the photo-conductor 20 that faces the groove is not changed in the axis direction of the photo-conductor 20 even when the photo-conductor 20 rotates. Therefore, the developed toner image may have a high concentration only at a portion that has faced the groove. On the other hand, if the groove is formed in the axis direction, the direction of the groove is substantially orthogonal to the rotational direction of the toner particle carrying roller. Thus, the carried toner particles are not easily rolled and charged.
In the developer containers 51, 52, 53, and 54 and the developing roller 510 according to this embodiment, the spiral groove 511 is formed on the surface 510d of the developing roller 510 with a constant pitch so as to be inclined with respect to the axis direction and the circumferential direction. Since the toner particles T are moved by rolling as the developing roller 510 rotates, the toner particles T can be charged appropriately. Furthermore, since the positions of the photo-conductor 20 and the groove 511 facing each other are relatively changed in the axis direction and the circumferential direction as the developing roller 510 rotates, the occurrence of the concentration unevenness on the developed toner image can be suppressed.
In the developing roller 510 according to this embodiment, since two types of grooves 511a and 511b each having a different angle of inclination are formed, toner particles T are moved in two directions along the grooves 511a and 511b. Therefore, the toner particles T can be prevented from being moved only in a certain single direction in an unbalanced manner. Furthermore, since the two grooves 511a and 511b intersect each other to form a grid, toner particles T that have started to roll along the first groove 511a (second groove 511b) can then roll along the second groove 511b (first groove 511a). Thus, the movement direction of the toner particles T can be effectively prevented from being unbalanced.
Since the top face 512a of the projection 512 surrounded by the two types of groove 511 has a square shape and one of two diagonal lines of the square shape extends in the circumferential direction, the projection 512 has two vertical angles located in the circumferential direction and two vertical angles located in the axis direction, all of the vertical angles being right angles. Therefore, the two grooves 511a and 511b have the same angle of inclination with respect to the circumferential direction and the axis direction. Consequently, the toner particles T are easily moved in the circumferential direction as well as the axis direction. Thus, the toner particles can be rolled more uniformly and uniformly charged.
For the toner particles T carried on the surface of the developing roller 510, since the layer thickness is regulated with the flat surface of the rubber portion 560a equipped with the regulating blade 560, the toner particles T carried on the surface of the developing roller 510, in particular on the projection 512, are not scraped by the regulating blade 560 completely. In other words, the layer thickness of the toner particles T can be regulated while the toner particles T are carried on both the groove 511 and the projection 512 of the developing roller 510.
Furthermore, since the toner particles T carried on the surface 510d are pressed by the flat surface of the regulating blade 560, the toner particles T can be charged appropriately by friction between the toner particles T and the surface of the developing roller 510, between the toner particles T and the regulating blade 560, and between the toner particles T.
When a developing apparatus can be resupplied with toner, mixed toner of residual toner and newly supplied toner is used. When a developing apparatus cannot be resupplied with toner, mixed toner of residual toner and newly loaded toner is used.
The invention will now be described in detail with Examples.
After 2 kg of toner base particles obtained by phase inversion emulsification were placed in a Henschel mixer (20 L), 2.0 g of small particle size silica (RX200 available from NIPPON AEROSIL Co., Ltd. having a primary particle size of 12 nm and processed with hexamethyldisilazane (HMDS)) and 0.5 g of large particle size silica (KEP10S available from NIPPON SHOKUBAI Co., Ltd. having a primary particle size of 100 nm and processed with silicone oil) were placed in the Henschel mixer as an addition amount per 100 g of toner base particles (volume-average particle size: 2.9 μm) (the same shall apply hereinafter). In addition, the electron-conductive oxide semiconductor fine particles shown in the first raw of Table 6 and the ion-conductive oxide semiconductor fine particles shown in the first column of Table 6 were placed in the Henschel mixer at the amounts shown in the first raw and in the first column of Table 6, respectively, to perform processing at a peripheral speed of 40 m/s for 2 minutes. After the treatment, coarse particles were removed using a sonic sifter with a metal mesh having an opening of 63 μm to prepare 21 types of toner.
Each of the obtained toners was loaded into the image forming apparatus (LP9000C available from SEIKO EPSON CORPORATION) shown in
A developing roller was formed by rolling. The surface of a hollow open pipe made of iron and having a diameter of 18 mm and a length of 370 mm had a shape shown in
A layer thickness regulating member had a thickness of 2 mm. The layer thickness regulating member was composed of silicon rubber or urethane rubber having a rubber hardness of 65 degrees (JIS-A standard) and supported by a layer thickness regulating member supporting member. The layer thickness regulating member supporting member included a thin plate and a thin plate supporting member and supported the layer thickness regulating member at one end in the transverse direction thereof. The thin plate composed of phosphor bronze, stainless steel, or the like had a thickness of 0.15 mm and a characteristic of spring. The thin plate directly supported the layer thickness regulating member and pressed the layer thickness regulating member against the developing roller using an urging force. The regulation form of the layer thickness regulating member used herein was a regulation form (so-called edge regulation) in which the edge in the transverse and thickness directions of the layer thickness regulating member is located within a contact nip having a certain width. A regulation bias of 150 V was applied to the layer thickness regulating member. A supplying roller composed of an urethane sponge having an outer diameter of φ19 and an Asker F hardness of 70° was brought into contact with the developing roller with pressure at a contact depth of 1 mm.
A color image was formed by AC jumping development under the following conditions:
processing speed (peripheral speed of photo-conductor): 210 mm/s
dark potential of photo-conductor: −50 V
light potential of photo-conductor: −550 V
transfer bias: 440 V
peripheral speed of developing roller: 336 mm/s
peripheral speed of supplying roller: 504 mm/s
peripheral speed ratio of photo-conductor to developing roller: 1.6
peripheral speed ratio of developing roller to supplying roller: 1.5
photo-conductor/developing roller gap: 100 μm
photo-conductor/developing roller AC bias component Vpp: 1100 V
Vavg: −200 V
photo-conductor/developing roller AC frequency (f): 6 kHz
photo-conductor/developing roller AC duty (ratio of applied time on the removing side): 60%
A toner amount adjusting patch sensor was not allowed to operate. The test environment was 10° C. and 15% RH.
An image was formed in the same manner as in Example 1, except that the regulation bias was changed to 300V.
In the image formation of Example 1 and Example 2, the transfer efficiency from an actual image forming apparatus (photo-conductor) to J paper (available from Fuji Xerox Co., Ltd.) was investigated. The evaluation criteria obtained from the weights of toner before and after the transference are as follows.
Excellent: transfer efficiency is more than 95%
Good: transfer efficiency is more than 90% and 95% or less
Fair: transfer efficiency is more than 85% and 90% or less
Poor: transfer efficiency is 85% or less
Tables 6 and 7 show the evaluation results of Example 1 and Example 2, respectively.
1) UU having a primary particle size of 20 to 50 nm and a particle size of sintered aggregates of 200 to 400 nm (available from Shin-Etsu Chemical Co., Ltd.)
2) HT1701 having a primary particle size of 100 to 300 nm (available from Toho Titanium Co., Ltd.)
3) STT30S having a primary particle size of 15 nm (available from Titan Kogyo, Ltd.)
4) FINEX-50S-LP2 having a primary particle size of 20 nm (available from Sakai Chemical Industry Co., Ltd.)
5) TAIMICRON TM-100 having a primary particle size of 14 nm (available from TAIMEI CHEMICALS Co., Ltd.)
1) UU having a primary particle size of 20 to 50 nm and a particle size of sintered aggregates of 200 to 400 nm (available from Shin-Etsu Chemical Co., Ltd.)
2) HT1701 having a primary particle size of 100 to 300 nm (available from Toho Titanium Co., Ltd.)
3) STT30S having a primary particle size of 15 nm (available from Titan Kogyo, Ltd.)
4) FINEX-50S-LP2 having a primary particle size of 20 nm (available from Sakai Chemical Industry Co., Ltd.)
5) TAIMICRON TM-100 having a primary particle size of 14 nm (available from TAIMEI CHEMICALS Co., Ltd.)
As is clear from Tables 6 and 7, the invention can provide a method for forming an image and an image forming apparatus that are excellent in uniform electrification and a transfer efficiency even if the particle size of toner is small.
The entire disclosure of Japanese Patent Application No. 2009-097944, filed Apr. 14, 2009 is expressly incorporated by reference herein.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2009-097944 | Apr 2009 | JP | national |
