Patent Grant
10082742
This application is based on and claims priority under 35 USC 119 from Japanese Patent Application No. 2016-166100 filed Aug. 26, 2016.
The present invention relates to an electrostatic charge image developing toner, an electrostatic charge image developer, and a toner cartridge.
In the electrophotographic image forming, toners are used as image forming materials, and, for example, a toner including toner particles including a binder resin and a colorant, and an external additive that is externally added to the toner particles is widely used.
According to an aspect of the invention, there is provided an electrostatic charge image developing toner including:
toner particles including an amorphous resin and a crystalline resin,
wherein, when the toner particles are subjected to a measurement by differential scanning calorimetry before and after being heated at a temperature of 50° C. and a humidity of 50% RH for a week, a relationship between an endothermic amount S1 (J/g) derived from the crystalline resin in a first heating process with respect to the toner particles before being heated and an endothermic amount Sh (J/g) derived from the crystalline resin in a first heating process with respect to the toner particles after being heated satisfies Expression (1): 0.50≤S1/Sh≤0.90.
Exemplary embodiments of the present invention will be described in detail based on the following figures, wherein:
Hereinafter, the exemplary embodiments which are an example of the invention will be described in detail.
Electrostatic Charge Image Developing Toner
An electrostatic charge image developing toner (hereinafter, also simply referred to as a “toner”) according to the exemplary embodiment includes toner particles including an amorphous resin and a crystalline resin. When the toner particles are subjected to a measurement by differential scanning calorimetry before and after being heated at a temperature of 50° C. and a humidity of 50% RH for a week, a relationship between an endothermic amount S1 (J/g) derived from the crystalline resin in a first heating process with respect to the toner particles before being heated and an endothermic amount Sh (J/g) derived from the crystalline resin in a first heating process with respect to the toner particles after being heated satisfies Expression (1): 0.50≤S1/Sh≤0.90.
With the configuration described above, the toner according to the exemplary embodiment prevents color irregularity which may be generated when an image is formed in a high temperature and high humidity environment (for example, in an environment of a temperature of 30° C. and humidity of 80% RH) and a low temperature and low humidity environment (for example, in an environment of a temperature of 10° C. and humidity of 20% RH). A reason thereof is assumed as follows.
In recent years, in regards to a demand for energy saving, a technology of improving low temperature fixing properties of a toner, in order to reduce power consumption when fixing a toner image has been known. As one technology, a toner including an amorphous resin and a crystalline resin in toner particles has been known. Meanwhile, from a viewpoint of ensuring heat resistance, a technology of forming a structure (sea-island structure) in which an amorphous resin and a crystalline resin are suitably phase-separated in toner particles has been known.
However, in a degree of “phase separation between an amorphous resin and a crystalline resin” of the related art, the amount of the crystalline resin compatible with the amorphous resin is large, and accordingly, when an image is formed in a high temperature and high humidity environment (for example, in an environment of a temperature of 30° C. and humidity of 80% RH), color irregularity may be generated.
Specifically, when the amount of the crystalline resin compatible with the amorphous resin is large, tendency of exhibiting characteristics derived from the crystalline resin in which electric resistance is low, as characteristics of the toner increases. Particularly, in the toner having low electric resistance, charging injection occurs in a high temperature and high humidity environment, and transfer properties with respect to a hydrous recording medium (water-containing paper or the like) are deteriorated due to low charging of the toner. Accordingly, color irregularity of a primary color may be generated.
Meanwhile, when the amount of the crystalline resin compatible with the amorphous resin becomes excessively small (that is, when phase separation between the amorphous resin and the crystalline resin is excessively performed), a tendency of excessively increasing electric resistance of the toner increases. Accordingly, partial transfer failure of a monochrome toner image on an uppermost layer occurs in combination color transfer (transfer of a combination color toner image obtained by superimposing monochrome toner images with primary colors different from each other) in a low temperature and low humidity environment (for example, in an environment of a temperature of 10° C. and humidity of 20% RH), and color irregularity is generated. The tendency more significantly occurs with a toner having a small diameter in which charging quantity of the toner per unit weight is increased.
Therefore, in the toner according to the exemplary embodiment, the ranges of the phase-separated amount of the crystalline resin from the amorphous resin and the amount of the crystalline resin compatible with the amorphous resin in the toner particles are suitably controlled. That is, when the toner particles are heated at a temperature of 50° C. and humidity of 50% RH for a week, a relationship between an endothermic amount S1 (J/g) derived from the crystalline resin of the toner particles before being heated, in a first heating process, which is measured by differential scanning calorimeter (DSC) and an endothermic amount Sh (J/g) derived from the crystalline resin of the toner particles after being heated, in the first heating process, which is measured by differential scanning calorimeter (DSC) satisfies Expression (1): 0.50≤S1/Sh≤0.90.
Here, the endothermic amount derived from the crystalline resin of the toner particles, in the first heating process, measured by differential scanning calorimeter (DSC) is an endothermic amount based on an endothermic peak of the crystalline resin phase-separated from the amorphous resin. That is, a small endothermic amount derived from the crystalline resin means that the amount (compatible portion) of the crystalline resin compatible with the amorphous resin is large and the phase-separated amount of the crystalline resin is small. The large endothermic amount derived from the crystalline resin means that the amount (compatible portion) of the crystalline resin compatible with the amorphous resin is small and the phase-separated amount of the crystalline resin is large.
Meanwhile, when the toner particles are heated at a temperature of 50° C. and humidity of 50% RH for a week, phase separation between the amorphous resin and the crystalline resin proceeds in the toner particles, and the amount of the crystalline resin compatible with the amorphous resin becomes close to zero.
That is, satisfying Expression (1): 0.50≤S1/Sh≤0.90 with a relationship in which an endothermic amount S1 (J/g) derived from the crystalline resin of the toner particles before being heated, in a first heating process, which is measured by differential scanning calorimeter (DSC) and an endothermic amount Sh (J/g) derived from the crystalline resin of the toner particles after being heated, in the first heating process, which is measured by differential scanning calorimeter (DSC) means that the phase-separated amount of the crystalline resin from the amorphous resin is larger than the amount (compatible portion) of the crystalline resin compatible therewith in a suitable range in the toner particles.
When a value of “S1/Sh” in Expression (1) is set to be equal to or greater than 0.50 to decrease the amount (compatible portion) of the crystalline resin compatible with the amorphous resin (that is, to prevent an excessive compatible state between the amorphous resin and the crystalline resin), an excessive deterioration in electric resistance of the toner is prevented, and accordingly, generation of color irregularity of a primary color when an image is formed in the high temperature and high humidity environment is prevented.
Meanwhile, when a value of “S1/Sh” in Expression (1) is set to be equal to or smaller than 0.90 to prevent an excessive decrease in the amount (compatible portion) of the crystalline resin compatible with the amorphous resin (that is, to prevent excessive phase separation between the amorphous resin and the crystalline resin), an excessive increase in electric resistance of the toner is prevented, and accordingly, generation of color irregularity when an image is formed in the low temperature and low humidity environment is prevented.
As described above, in the toner according to the exemplary embodiment, it is assumed that generation of color irregularity which is generated when an image is formed in the high temperature and high humidity environment and the low temperature and low humidity environment, is prevented.
In the toner according to the exemplary embodiment, Expression (1): 0.50≤S1/Sh≤0.90 is satisfied, but, from a viewpoint of preventing generation of color irregularity, Expression (12): 0.55≤S1/Sh≤0.85 is preferably satisfied and Expression (13) (corresponding to Expression (2)): 0.58≤S1/Sh≤0.82 is more preferably satisfied.
The value of “S1/Sh” may be adjusted, for example, depending on a cooling speed after forming the toner particles conditions of an annealing process, and the like.
Here, the heating of the toner particles is performed by heating the toner particles to a temperature of 50° C. and humidity of 50% RH from the environment of a temperature of 25° C. and humidity of 50% RH and keeping the temperature for a week.
Meanwhile, the measurement of the endothermic amount derived from the crystalline resin of the toner particles measured by differential scanning calorimeter and the measurement of the melting temperature are performed based on ASTMD 3418-8.
Specifically, 10 mg of the toner particles (or toner particles to which the external additive is externally added) which is a measurement target is set in a differential scanning calorimeter (manufactured by Shimadzu Corporation: DSC-60A) including an automatic connection processing system, heated from room temperature (25° C.) to 150° C. at a rate of temperature rise of 10° C./min, and kept at 150° C. for 5 minutes, and first heating spectra (DSC curve) in the heating process are obtained. Next, the temperature is decreased to 0° C. at a rate of temperature decrease of −10° C./min by using liquid nitrogen and the temperature is kept at 0° C. for 5 minutes. After that, the temperature is increased to 150° C. at a rate of temperature rise of 10° C./min and second heating spectra (DSC curve) in the heating process are obtained.
An endothermic peak derived from the crystalline resin is specified from the obtained heating spectra (DSC curves). The specification of the endothermic peak derived from the crystalline resin is performed by specifying an endothermic peak which is not measured as the endothermic peak in the second DSC curve among the endothermic peaks measured in the first DSC curve, as the endothermic peak derived from the crystalline resin. Here, the endothermic peak indicates that a half value width is within 15° C.
The area of the endothermic peak derived from the crystalline resin is calculated as the endothermic amount. The area of the endothermic peak is calculated as the endothermic amount derived from the crystalline resin by determining the endothermic amount per weight of the sample from a peak area surrounded by a base line and the endothermic peak from the endothermic peak derived from the crystalline resin, based on Article 9 of JIS-K7122. A temperature of a peak portion of the endothermic peak derived from the crystalline resin is calculated as a melting temperature.
In a case of the toner particles to which an external additive is externally added, the toner particles to which an external additive is externally added are set as a heating target and a measurement target of the endothermic amount of the crystalline resin.
Hereinafter, the toner according to the exemplary embodiment will be described in detail.
The toner according to the exemplary embodiment, for example, includes toner particles and an external additive.
Toner Particles
The toner particles include a binder resin. The toner particles may further include a colorant, a release agent, and other additives, if necessary.
Binder Resin
Examples of the binder resin include an amorphous resin and a crystalline resin.
A weight ratio between the crystalline resin and the amorphous resin (crystalline resin/amorphous resin) is preferably 1/100 to 50/100 and more preferably 5/100 to 30/100.
The content of the entire binder resin is preferably 40% by weight to 95% by weight, more preferably 50% by weight to 90% by weight, and even more preferably 60% by weight to 85% by weight with respect to the content of the toner particles.
Here, “crystallinity” of the resin indicates that not a stepwise change in the endothermic amount but a clear endothermic peak is provided in the differential scanning calorimetry (DSC) based on ASTMD 3418-8, and specifically indicates that a half value width of the endothermic peak measured at a rate of temperature rise of 10 (° C./min) is within 10° C.
Meanwhile, “non-crystallinity” of the resin indicates that a half value width exceeds 10° C., a stepwise change in the endothermic amount is shown, or a clear endothermic peak is not recognized.
The amorphous resin will be described.
As the amorphous resin, well-known amorphous resins such as an amorphous polyester resin, an amorphous vinyl resin (for example, a styrene acrylic resin or the like), an epoxy resin, a polycarbonate resin, and a polyurethane resin are used, for example. Among these, an amorphous polyester resin and an amorphous vinyl resin (particularly, a styrene acrylic resin) are preferable and an amorphous polyester resin is more preferable, from the viewpoints of low temperature fixing properties and chargeability of the toner.
Examples of the amorphous polyester resin include condensation polymers of polyvalent carboxylic acids and polyols. A commercially available product or a synthesized product may be used as the amorphous polyester resin.
Examples of the polyvalent carboxylic acid include aliphatic dicarboxylic acids (for example, oxalic acid, malonic acid, maleic acid, fumaric acid, citraconic acid, itaconic acid, glutaconic acid, succinic acid, alkenyl succinic acid, adipic acid, and sebacic acid), alicyclic dicarboxylic acids (for example, cyclohexanedicarboxylic acid), aromatic dicarboxylic acids (for example, terephthalic acid, isophthalic acid, phthalic acid, and naphthalenedicarboxylic acid), anhydrides thereof, or lower alkyl esters (having, for example, from 1 to 5 carbon atoms) thereof. Among these substances, for example, aromatic dicarboxylic acids are preferably used as the polyvalent carboxylic acid.
As the polyvalent carboxylic acid, a tri- or higher-valent carboxylic acid employing a crosslinked structure or a branched structure may be used in combination with a dicarboxylic acid. Examples of the tri- or higher-valent carboxylic acid include trimellitic acid, pyromellitic acid, anhydrides thereof, or lower alkyl esters thereof (the alkyl group having from 1 to 5 carbon atoms, for example).
The polyvalent carboxylic acids may be used singly or in combination of two or more types thereof.
Examples of the polyol include aliphatic diols (for example, ethylene glycol, diethylene glycol, triethylene glycol, propylene glycol, butanediol, hexanediol, and neopentyl glycol), alicyclic diols (for example, cyclohexanediol, cyclohexanedimethanol, and hydrogenated bisphenol A), and aromatic diols (for example, ethylene oxide adduct of bisphenol A and propylene oxide adduct of bisphenol A). Among these, for example, aromatic diols and alicyclic diols are preferably used, and aromatic diols are more preferably used as the polyol.
As the polyol, a tri- or higher-valent polyol employing a crosslinked structure or a branched structure may be used in combination together with diol. Examples of the tri- or higher-valent polyol include glycerin, trimethylolpropane, and pentaerythritol.
The polyol may be used singly or in combination of two or more types thereof.
A well-known preparing method is applied to prepare the amorphous polyester resin. Examples thereof include a method of conducting a reaction at a polymerization temperature of 180° C. to 230° C., if necessary, under reduced pressure in the reaction system, while removing water or an alcohol generated during condensation.
In the case in which monomers of the raw materials are not dissolved or compatibilized at a reaction temperature, a high-boiling-point solvent may be added as a solubilizing agent to dissolve the monomers. In this case, a polycondensation reaction is conducted while distilling away the solubilizing agent. In the case in which a monomer having poor compatibility is used, the monomer having poor compatibility and an acid or an alcohol to be polycondensed with the monomer may be previously condensed and then polycondensed with the main component.
Here, as the amorphous polyester resin, a modified amorphous polyester resin is also used, in addition to the unmodified amorphous polyester resin described above. The modified amorphous polyester resin is an amorphous polyester resin in which a bonding group other than an ester bond is present, and an amorphous polyester resin in which a resin component other than the amorphous polyester resin is bonded by covalent bonding or ionic bonding. As the modified amorphous polyester resin, usable is, for example, a resin including a terminal modified by allowing a reaction between an amorphous polyester resin which a functional group such as an isocyanate group capable of reacting with an acid group or a hydroxyl group is introduced to a terminal thereof, and an active hydrogen compound is used.
As the modified amorphous polyester resin, a urea-modified amorphous polyester resin (hereinafter, also simply referred to as an “urea-modified polyester resin”) is preferable.
As the urea-modified polyester resin, a urea-modified polyester resin obtained by a reaction (at least one reaction of a crosslinking reaction and an extension reaction) between an amorphous polyester resin including an isocyanate group (amorphous polyester prepolymer) and an amine compound may be used. The urea-modified polyester resin may include a urea bond and a urethane bond.
As an amorphous polyester prepolymer including an isocyanate group, an amorphous polyester prepolymer obtained by allowing a reaction of a polyvalent isocyanate compound with respect to an amorphous polyester resin which is a polycondensate of polyvalent carboxylic acid and polyol and includes active hydrogen is used. Examples of a group including active hydrogen included in the amorphous polyester resin include a hydroxyl group (alcoholic hydroxyl group and phenolic hydroxyl group), an amino group, a carboxyl group, and a mercapto group, and an alcoholic hydroxyl group is preferable.
As polyvalent carboxylic acid and polyol of the amorphous polyester prepolymer including an isocyanate group, the compounds same as polyvalent carboxylic acid and polyol described in the section of the amorphous polyester resin are used.
Examples of a polyvalent isocyanate compound include aliphatic polyisocyanate (tetramethylene diisocyanate, hexamethylene diisocyanate, or 2,6-diisocyanato methyl caproate); alicyclic polyisocyanate (isophorone diisocyanate or cyclohexylmethane diisocyanate); aromatic diisocyanate (tolylene diisocyanate or diphenylmethane diisocyanate); aromatic aliphatic diisocyanate (α,α,α′,α′-tetramethylxylylene diisocyanate); isocyanurates; and a component obtained by blocking the polyisocyanate by a blocking agent such as a phenol derivative, oxime, or caprolactam.
The polyvalent isocyanate compounds may be used singly or in combination of two or more kinds thereof.
A ratio of the polyvalent isocyanate compound is preferably from 1/1 to 5/1, more preferably from 1.2/1 to 4/1, and even more preferably from 1.5/1 to 2.5/1, as an equivalent ratio [NCO]/[OH] of an isocyanate group [NCO] and a hydroxyl group of an amorphous polyester prepolymer including a hydroxyl group [OH].
In the amorphous polyester prepolymer including an isocyanate group, the content of a component derived from the polyvalent isocyanate compound is preferably from 0.5% by weight to 40% by weight, more preferably from 1% by weight to 30% by weight, and even more preferably from 2% by weight to 20% by weight, with respect to the content of the entire amorphous polyester prepolymer including an isocyanate group.
The number of isocyanate groups contained per 1 molecule of the amorphous polyester prepolymer including an isocyanate group is preferably averagely equal to or greater than 1, more preferably averagely from 1.5 to 3, and even more preferably averagely from 1.8 to 2.5.
Examples of the amine compound to be reacted with the amorphous polyester prepolymer including an isocyanate group include diamine, tri- or higher valent polyamine, amino alcohol, amino mercaptan, amino acid, and a compound obtained by blocking these amino groups.
Examples of diamine include aromatic diamine (phenylene diamine, diethyl toluene diamine, or 4,4′diaminodiphenylmethane); alicyclic diamine (4,4′-diamino-3,3′dimethyl dicyclohexyl methane, diamine cyclohexane, or isophorone diamine); and aliphatic diamine (ethylenediamine, tetramethylenediamine, or hexamethylenediamine).
Examples of tri- or higher valent polyamine include diethylenetriamine and triethylenetetramine.
Examples of amino alcohol include ethanolamine and hydroxyethyl aniline.
Examples of amino mercaptan include aminoethyl mercaptan and aminopropyl mercaptan.
Examples of amino acid include aminopropionic acid and aminocaproic acid.
Examples of a compound obtained by blocking these amino groups include a ketimine compound and an oxazoline compound obtained from an amine compound such as diamine, tri- or higher valent polyamine, amino alcohol, amino mercaptan, or amino acid and a ketone compound (acetone, methyl ethyl ketone, or methyl isobutyl ketone).
Among these amine compounds, a ketimine compound is preferable.
The amine compounds may be used singly or in combination of two or more kinds thereof.
The urea-modified polyester resin may be a resin in which the molecular weight after the reaction is adjusted by adjusting a reaction between the amorphous polyester resin including an isocyanate group (amorphous polyester prepolymer) and an amine compound (at least one reaction of the crosslinking reaction and the extension reaction), using a stopper which stops at least one reaction of the crosslinking reaction and the extension reaction (hereinafter, also referred to as a “crosslinking/extension reaction stopper”).
Examples of the crosslinking/extension reaction stopper include monoamine (diethylamine, dibutylamine, butylamine, or laurylamine) and a component obtained by blocking those (ketimine compound).
A ratio of the amine compound is preferably from 1/2 to 2/1, more preferably from 1/1.5 to 1.5/1, and even more preferably from 1/1.2 to 1.2/1, as an equivalent ratio [NCO]/[NHx] of an isocyanate group [NCO] of the amorphous polyester prepolymer including an isocyanate group and an amino group [NHx] of amines.
As the urea-modified polyester resin, a urea-modified polyester resin obtained by a reaction (at least one reaction of a crosslinking reaction and an extension reaction) between a polyester resin including an isocyanate group (hereinafter, referred to as a “polyester prepolymer”) and an amine compound may be used. The urea-modified polyester resin may include a urea bond and a urethane bond.
As a polyester prepolymer, a reactant between polyester including a group including active hydrogen and a polyvalent isocyanate compound is used. Examples of a group including active hydrogen include a hydroxyl group (alcoholic hydroxyl group and phenolic hydroxyl group), an amino group, a carboxyl group, and a mercapto group, and an alcoholic hydroxyl group is preferable. Examples of a polyvalent isocyanate compound include aliphatic polyisocyanate (tetramethylene diisocyanate, hexamethylene diisocyanate, or 2,6-diisocyanato methyl caproate); alicyclic polyisocyanate (isophorone diisocyanate or cyclohexylmethane diisocyanate); aromatic diisocyanate (tolylene diisocyanate or diphenylmethane diisocyanate); aromatic aliphatic diisocyanate (α,α,α′,α′-tetramethylxylylene diisocyanate); isocyanurates; and a compound obtained by blocking the polyisocyanate by a blocking agent such as a phenol derivative, oxime, or caprolactam. The polyvalent isocyanate compounds may be used singly or in combination of two or more kinds thereof.
The content of a component derived from the polyvalent isocyanate compound of the polyester prepolymer is preferably 0.5% by weight to 40% by weight, more preferably 1% by weight to 30% by weight, and even more preferably 2% by weight to 20% by weight, with respect to the content of the entire polyester prepolymer. The average number of isocyanate groups contained per 1 molecule of the polyester prepolymer is preferably equal to or greater than 1, more preferably 1.5 to 3, and even more preferably 1.8 to 2.5.
Examples of the amine compound to be reacted with the polyester prepolymer include diamine, tri- or higher valent polyamine, amino alcohol, amino mercaptan, amino acid, a compound obtained by blocking an amino group of these amino compounds.
Examples of diamine include aromatic diamine (phenylene diamine, diethyl toluene diamine, or 4,4′diaminodiphenylmethane); alicyclic diamine (4,4′-diamino-3,3′dimethyl dicyclohexyl methane, diamine cyclohexane, or isophorone diamine); and aliphatic diamine (ethylenediamine, tetramethylenediamine, or hexamethylenediamine). Examples of tri- or higher valent polyamine include diethylenetriamine and triethylenetetramine. Examples of amino alcohol include ethanolamine and hydroxyethyl aniline. Examples of amino mercaptan include aminoethyl mercaptan and aminopropyl mercaptan. Examples of amino acid include aminopropionic acid and aminocaproic acid.
Examples of a compound obtained by blocking the amino group of the amine compound include a ketimine compound and an oxazoline compound derived from the amine compound and ketone compound (acetone, methyl ethyl ketone, or methyl isobutyl ketone).
As the amine compound, a ketimine compound is preferable. The amine compounds may be used singly or in combination of two or more kinds thereof.
The urea-modified polyester resin may be a resin in which the molecular weight after the reaction is adjusted by adjusting a reaction between the polyester prepolymer and an amine compound using a stopper which stops at least one reaction of the crosslinking reaction and the extension reaction (hereinafter, also referred to as a “crosslinking/extension reaction stopper”). Examples of the crosslinking/extension reaction stopper include monoamine (diethylamine, dibutylamine, butylamine, or laurylamine) and a compound obtained by blocking the amino group of monoamine (ketimine compound).
The characteristics of the amorphous resin will be described.
The glass transition temperature (Tg) of the amorphous resin is preferably 50° C. to 80° C., and more preferably 50° C. to 65° C.
The glass transition temperature is obtained by a DSC curve which is obtained by a differential scanning calorimetry (DSC), and more specifically, is obtained by “Extrapolating Glass Transition Starting Temperature” disclosed in a method for obtaining the glass transition temperature of “Testing Methods for Transition Temperatures of Plastics” in JIS K-7121-1987.
The weight average molecular weight (Mw) of the amorphous resin is preferably 5,000 to 1,000,000 and more preferably 7,000 to 500,000.
The number average molecular weight (Mn) of the amorphous resin is preferably 2,000 to 100,000.
The molecular weight distribution Mw/Mn of the amorphous resin is preferably 1.5 to 100 and more preferably 2 to 60.
The weight average molecular weight and the number average molecular weight are measured by gel permeation chromatography (GPC). The molecular weight measurement by GPC is performed by using GPC.HLC-8120 GPC manufactured by Tosoh Corporation as a measuring device, TSKGEL SUPERHM-M (15 cm) manufactured by Tosoh Corporation, as a column, and a THF solvent. The weight average molecular weight and the number average molecular weight are calculated using a calibration curve of molecular weight obtained with a monodisperse polystyrene standard sample from the measurement results obtained from the measurement.
The crystalline resin will be described.
As the crystalline resin, well-known crystalline resins such as a crystalline polyester resin and a crystalline vinyl resin (for example, a polyalkylene resin or a long-chain alkyl (meth)acrylate resin) are used. Among these, a crystalline polyester resin is preferable from viewpoints of mechanical toughness and low temperature fixing properties of the toner.
Examples of the crystalline polyester resin include condensation polymers of polyvalent carboxylic acids and polyols. A commercially available product or a synthesized product may be used as the crystalline polyester resin.
Here, since a crystal structure is easily formed with the crystalline polyester resin, a condensation polymer using a polymerizable monomer including a straight aliphatic group is preferable than a polymerizable monomer including an aromatic group.
Examples of the polyvalent carboxylic acid include aliphatic dicarboxylic acids (e.g., oxalic acid, succinic acid, glutaric acid, adipic acid, suberic acid, azelaic acid, sebacic acid, 1,9-nonane dicarboxylic acid, 1,10-decane dicarboxylic acid, 1,12-dodecane dicarboxylic acid, 1,14-tetra decane dicarboxylic acid, and 1,18-octadecane dicarboxylic acid), aromatic dicarboxylic acids (e.g., phthalic acid, isophthalic acid, terephthalic acid, dibasic acid of naphthalene-2,6-dicarboxylic acid), anhydrides thereof, or lower alkyl esters (having, for example, from 1 to 5 carbon atoms) thereof.
As the polyvalent carboxylic acid, a tri- or higher-valent carboxylic acid employing a crosslinked structure or a branched structure may be used in combination with a dicarboxylic acid. Examples of the trivalent carboxylic acid include aromatic carboxylic acid (e.g., 1,2,3-benzenetricarboxylic acid, 1,2,4-benzenetricarboxylic acid, and 1,2,4-naphthalene tricarboxylic acid), anhydrides thereof, or lower alkyl esters (having, for example, from 1 to 5 carbon atoms) thereof.
As the polyvalent carboxylic acid, a dicarboxylic acid having a sulfonic acid group and a dicarboxylic acid having an ethylenic double bond may be used in combination with the dicarboxylic acids described above.
The polyvalent carboxylic acids may be used singly or in combination of two or more kinds thereof.
Examples of the polyol include aliphatic diols (e.g., linear aliphatic diol having 7 to 20 carbon atoms of main chain part). Examples of aliphatic diols include ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,7-heptane diol, 1,8-octanediol, 1,9-nonanediol, 1,10-decanediol, 1,11-undecanediol, 1,12-dodecane diol, 1,13-tri-decanediol, 1,14-tetradecanediol, 1,18-octadecanediol, and 1,14-eicosanedecanediol. Among these, 1,8-octanediol, 1,9-nonanediol, and 1,10-decanediol are preferable as aliphatic diols.
As the polyol, a tri- or higher-valent alcohol employing a crosslinked structure or a branched structure may be used in combination with a diol. Examples of the tri- or higher-valent polyol include glycerin, trimethylolethane, trimethylolpropane, and pentaerythritol.
The polyols may be used singly or in combination of two or more kinds thereof.
Here, in the polyol, the content of aliphatic diol may be suitably 80 mol % or more and is more preferably 90 mol % or more.
A well-known preparing method is applied to prepare the crystalline polyester resin, in the same manner as in the amorphous polyester resin.
The characteristics of the crystalline resin will be described.
A melting temperature of the crystalline resin is preferably 50° C. to 100° C., more preferably 55° C. to 90° C., and even more preferably 60° C. to 85° C.
The melting temperature is obtained from “melting peak temperature” described in the method of obtaining a melting temperature in JIS K7121-1987 “Testing Methods for Transition Temperatures of Plastics”, from a DSC curve obtained by differential scanning calorimetry (DSC).
A weight average molecular weight (Mw) of the crystalline resin is preferably 6,000 to 35,000.
Here, a suitable combination of the amorphous resin and the crystalline resin will be described.
A combination of the amorphous resin and the crystalline resin is selected by changing structures of the crystalline polyester resin and the amorphous resin and controlling a blending ratio between both resins or dispersion structures at the time of preparing, from viewpoints of satisfying Expression (1): 0.50≤S1/Sh≤0.90 and preventing generation of color irregularity.
The structure changing is performed, for example, by changing monomer units configuring both resins. In this case, a solubility parameter (SP value) is calculated by Fedors method (Polym. Eng. Sci., 14, 147(1974)). When the SP values of both resins are set to be close to each other, compatibility is increased and a value of ΔH2/ΔH1 may be decreased.
Specifically, for example, when bisphenol A ethylene oxide adduct as an alcohol component of polyester is changed to bisphenol A propylene oxide adduct, the SP value of the polyester resin obtained may be decreased. When dicarboxylic acid used as an acid component is changed from aliphatic dicarboxylic acid such as sebacic acid to aromatic dicarboxylic acid such as terephthalic acid, the SP value may be increased.
The SP value of the resin may also be measured by measuring solubility with respect to a solvent of which an SP value is known. However, the actual phenomenon that both resins are compatible with each other is also related to an interaction between both resins, and accordingly, the compatibility is not only determined with the SP value.
Here, a difference (ΔSP value) between the SP value of the crystalline resin and the SP value of the amorphous resin is preferably in a range of 0.2 to 1.3 and more preferably in a range of 0.5 to 1.1.
Colorant
Examples of the colorant include various pigments such as carbon black, chrome yellow, Hansa yellow, benzidine yellow, threne yellow, quinoline yellow, pigment yellow, permanent orange GTR, pyrazolone orange, vulcan orange, watchung red, permanent red, brilliant carmine 3B, brilliant carmine 6B, DuPont oil red, pyrazolone red, lithol red, Rhodamine B Lake, Lake Red C, pigment red, rose bengal, aniline blue, ultramarine blue, calco oil blue, methylene blue chloride, phthalocyanine blue, pigment blue, phthalocyanine green, and malachite green oxalate; and various dyes such as acridine dyes, xanthene dyes, azo dyes, benzoquinone dyes, azine dyes, anthraquinone dyes, thioindigo dyes, dioxadine dyes, thiazine dyes, azomethine dyes, indigo dyes, phthalocyanine dyes, aniline black dyes, polymethine dyes, triphenylmethane dyes, diphenylmethane dyes, and thiazole dyes.
The colorants may be used singly or in combination of two or more types thereof.
As the colorant, the surface-treated colorant may be used, if necessary. The colorant may be used in combination with a dispersing agent. Plural colorants may be used in combination.
The content of the colorant is, for example, preferably 1% by weight to 30% by weight, more preferably 3% by weight to 15% by weight with respect to a total amount of the toner particles.
Release Agent
Examples of the release agent include hydrocarbon waxes; natural waxes such as carnauba wax, rice wax, and candelilla wax; synthetic or mineral/petroleum waxes such as montan wax; and ester waxes such as fatty acid esters and montanic acid esters. The release agent is not limited thereto.
The melting temperature of the release agent is preferably 50° C. to 110° C. and more preferably 60° C. to 100° C.
The melting temperature is obtained from “melting peak temperature” described in the method of obtaining a melting temperature in JIS K 7121-1987 “Testing methods for transition temperatures of plastics”, from a DSC curve obtained by differential scanning calorimetry (DSC).
The content of the release agent is, for example, preferably 1% by weight to 20% by weight, and more preferably 5% by weight to 15% by weight with respect to the total amount of the toner particles.
Other Additives
Examples of other additives include well-known additives such as a magnetic material, a charge-controlling agent, and an inorganic particle. The toner particles include these additives as internal additives.
Characteristics of Toner Particles
The toner particles may be toner particles having a single-layer structure, or toner particles having a so-called core/shell structure composed of a core (core particle) and a coating layer (shell layer) coated on the core.
Here, the toner particles having a core/shell structure may be configured with, for example, a core including a binder resin, and if necessary, other additives such as a colorant and a release agent, and a coating layer including a binder resin.
The volume average particle diameter (D50v) of the toner particles is preferably 2 μm to 10 μm, and more preferably 4 μm to 8 μm.
Various average particle diameters and various particle size distribution indices of the toner particles are measured by using a COULTER MULTISIZER II (manufactured by Beckman Coulter, Inc.) and ISOTON-II (manufactured by Beckman Coulter, Inc.) as an electrolyte.
In the measurement, from 0.5 mg to 50 mg of a measurement sample is added to 2 ml of a 5% aqueous solution of surfactant (preferably sodium alkylbenzene sulfonate) as a dispersing agent. The obtained material is added to from 100 ml to 150 ml of the electrolyte.
The electrolyte in which the sample is suspended is subjected to a dispersion treatment using an ultrasonic disperser for 1 minute, and a particle size distribution of particles having a particle diameter of from 2 μm to 60 μm is measured by a COULTER MULTISIZER II using an aperture having an aperture diameter of 100 μm. 50,000 particles are sampled.
Cumulative distributions by volume and by number are drawn from the side of the smallest diameter with respect to particle size ranges (channels) separated based on the measured particle size distribution. The particle diameter when the cumulative percentage becomes 16% is defined as that corresponding to a volume average particle diameter D16v and a number average particle diameter D16p, while the particle diameter when the cumulative percentage becomes 50% is defined as that corresponding to a volume average particle diameter D50v and a number average particle diameter D50p. Furthermore, the particle diameter when the cumulative percentage becomes 84% is defined as that corresponding to a volume average particle diameter D84v and a number average particle diameter D84p.
Using these, a volume average particle size distribution index (GSDv) is calculated as (D84v/D16v)1/2, while a number average particle size distribution index (GSDp) is calculated as (D84p/D16p)1/2.
An average circularity of the toner particles is preferably 0.94 to 1.00 and more preferably 0.95 to 0.98.
The average circularity of the toner particles is determined by an expression of (perimeter of equivalent circle diameter)/(perimeter) [(perimeter of a circle having the same projected area as that of a particle image)/(perimeter of particle projection image)]. Specifically, the average circularity thereof is a value measured using the following method.
First, the toner particles which is a measurement target are sucked and collected, a flat flow is formed, stroboscopic light emission is instantly performed to obtain a particle image as a still image, and the average circularity is determined using a flow-type particle image analysis device (FPIA-2100 manufactured by Sysmex Corporation) which performs image analysis of the particle image. 3,500 particles are sampled when determining the average circularity.
In a case where the toner includes an external additive, the toner (developer) which is a measurement target is dispersed in water including a surfactant, and then, the ultrasonic treatment is performed to obtain toner particles from which the external additive is removed.
External Additives
As the other external additives, inorganic particles are used, for example. Examples of the inorganic particles include SiO2, TiO2, Al2O3, CuO, ZnO, SnO2, CeO2, Fe2O3, MgO, BaO, CaO, K2O, Na2O, ZrO2, CaO.SiO2, K2O.(TiO2)n, Al2O3.2SiO2, CaCO3, MgCO3, BaSO4, and MgSO4.
The surfaces of the inorganic particles as the external additive may be treated with a hydrophobizing agent. The hydrophobizing treatment is performed by, for example, dipping the inorganic particles in a hydrophobizing agent. The hydrophobizing agent is not particularly limited and examples thereof include a silane coupling agent, silicone oil, a titanate coupling agent, and an aluminum coupling agent. These may be used singly or in combination of two or more kinds thereof.
Generally, the amount of the hydrophobizing agent is, for example, 1 part by weight to 10 parts by weight with respect to 100 parts by weight of the inorganic particles.
Examples of the external additives also include resin particles (resin particles such as polystyrene, polymethyl methacrylate (PMMA), and melamine resin) and a cleaning aid (for example, a metal salt of higher fatty acid represented by zinc stearate, and fluorine polymer particles).
The amount of the external additives externally added is, for example, preferably 0.01% by weight to 5% by weight, and more preferably 0.01% by weight to 2.0% by weight with respect to the amount of the toner particles.
Preparing Method of Toner
Next, a preparing method of the toner according to the exemplary embodiment will be described.
The toner according to the exemplary embodiment is obtained by externally adding an external additive to toner particles, after preparing the toner particles.
The toner particles may be prepared using any of a dry preparing method (e.g., kneading and pulverizing method) and a wet preparing method (e.g., aggregation and coalescence method, suspension and polymerization method, and dissolution and suspension method). The toner particle preparing method is not particularly limited to these preparing methods, and a known preparing method is employed.
First, a toner particle preparing method using an aggregation and coalescence method will be described.
The toner particles are prepared through the processes of: preparing a resin particle dispersion in which resin particles as a binder resin are dispersed (resin particle dispersion preparation process); aggregating the resin particles (if necessary, other particles) in the resin particle dispersion (if necessary, in the dispersion after mixing with other particle dispersions) to form aggregated particles (aggregated particle forming process); and heating the aggregated particle dispersion in which the aggregated particles are dispersed, to aggregate and coalesce the aggregated particles, thereby forming toner particles (aggregation and coalescence process).
Here, as the resin particle dispersion, an amorphous resin particle dispersion in which amorphous resin particles are dispersed, and a crystalline resin particle dispersion in which crystalline resin particles are dispersed are applied. As the resin particle dispersion, an amorphous resin particle dispersion in which resin particles including the amorphous resin and the crystalline resin are dispersed may also be applied.
Hereinafter, the processes will be described below in detail.
In the following description, a method of obtaining toner particles containing a colorant and a release agent will be described, but a colorant and a release agent is used, if necessary. Other additives may be used, in addition to a colorant and a release agent.
Resin Particle Dispersion Preparation Process
First, for example, a colorant particle dispersion in which colorant particles are dispersed and a release agent particle dispersion in which release agent particles are dispersed are prepared together with a resin particle dispersion in which resin particles as a binder resin are dispersed.
The resin particle dispersion is prepared by, for example, dispersing resin particles in a dispersion medium using a surfactant.
Examples of the dispersion medium used for the resin particle dispersion include aqueous mediums.
Examples of the aqueous mediums include water such as distilled water and ion exchange water, and alcohols. These may be used singly or in combination of two or more kinds thereof.
Examples of the surfactant include anionic surfactants such as a sulfuric ester salt, a sulfonate, a phosphate ester, and a soap; cationic surfactants such as an amine salt and a quaternary ammonium salt; and nonionic surfactants such as polyethylene glycol, an ethylene oxide adduct of alkyl phenol, and polyol. Among these, anionic surfactants and cationic surfactants are particularly preferably used. Nonionic surfactants may be used in combination with anionic surfactants or cationic surfactants.
The surfactants may be used singly or in combination of two or more kinds thereof.
Regarding the resin particle dispersion, as a method of dispersing the resin particles in the dispersion medium, a common dispersing method using, for example, a rotary shearing-type homogenizer, or a ball mill, a sand mill, or a DYNO mill having media is exemplified. Depending on the kind of the resin particles, resin particles may be dispersed in the resin particle dispersion according to, for example, a phase inversion emulsification method.
The phase inversion emulsification method includes: dissolving a resin to be dispersed in a hydrophobic organic solvent in which the resin is soluble; conducting neutralization by adding a base to an organic continuous phase (O phase); and converting the resin (so-called phase inversion) from W/O to O/W by putting an aqueous medium (W phase) to form a discontinuous phase, thereby dispersing the resin as particles in the aqueous medium.
A volume average particle diameter of the resin particles dispersed in the resin particle dispersion is, for example, preferably 0.01 μm to 1 μm, more preferably 0.08 μm to 0.8 μm, and even more preferably 0.1 μm to 0.6 μm.
Regarding the volume average particle diameter of the resin particles, a cumulative distribution by volume is drawn from the side of the smallest diameter with respect to particle size ranges (channels) separated using the particle size distribution obtained by the measurement with a laser diffraction-type particle size distribution measuring device (for example, LA-700 manufactured by Horiba, Ltd.), and a particle diameter when the cumulative percentage becomes 50% with respect to the entire particles is measured as a volume average particle diameter D50v. The volume average particle diameter of the particles in other dispersions is also measured in the same manner.
The content of the resin particles contained in the resin particle dispersion is, for example, preferably 5% by weight to 50% by weight, and more preferably 10% by weight to 40% by weight.
For example, the colorant particle dispersion and the release agent particle dispersion are also prepared in the same manner as in the case of the resin particle dispersion. That is, the particles in the resin particle dispersion are the same as the colorant particles dispersed in the colorant particle dispersion and the release agent particles dispersed in the release agent particle dispersion, in terms of the volume average particle diameter, the dispersion medium, the dispersing method, and the content of the particles.
Aggregated Particle Forming Process
Next, the colorant particle dispersion and the release agent dispersion are mixed together with the resin particle dispersion.
The resin particles, the colorant particles, and the release agent particles are heterogeneously aggregated in the mixed dispersion, thereby forming aggregated particles having a diameter near a target toner particle diameter and including the resin particles, the colorant particles, and the release agent particles.
Specifically, for example, an aggregating agent is added to the mixed dispersion and a pH of the mixed dispersion is adjusted to acidity (for example, the pH is 2 to 5). If necessary, a dispersion stabilizer is added. Then, the mixed dispersion is heated at a temperature of the glass transition temperature of the resin particles (specifically, for example, from a temperature 30° C. lower than the glass transition temperature of the resin particles to 10° C. lower than the glass transition temperature) to aggregate the particles dispersed in the mixed dispersion, thereby forming the aggregated particles.
In the aggregated particle forming process, for example, the aggregating agent may be added at room temperature (for example, 25° C.) under stirring of the mixed dispersion using a rotary shearing-type homogenizer, the pH of the mixed dispersion may be adjusted to be acidic (for example, the pH is 2 to 5), a dispersion stabilizer may be added if necessary, and then the heating may be performed.
Examples of the aggregating agent include a surfactant having an opposite polarity to the polarity of the surfactant used as the dispersing agent to be added to the mixed dispersion, an inorganic metal salt, and a bi- or higher-valent metal complex. Particularly, when a metal complex is used as the aggregating agent, the amount of the surfactant used is reduced and charging characteristics are improved.
If necessary, an additive may be used which forms a complex or a similar bond with the metal ions of the aggregating agent. A chelating agent is preferably used as the additive.
Examples of the inorganic metal salt include a metal salt such as calcium chloride, calcium nitrate, barium chloride, magnesium chloride, zinc chloride, aluminum chloride, and aluminum sulfate, and inorganic metal salt polymer such as polyaluminum chloride, polyaluminum hydroxide, and calcium polysulfide.
A water-soluble chelating agent may be used as the chelating agent. Examples of the chelating agent include oxycarboxylic acids such as tartaric acid, citric acid, and gluconic acid, iminodiacetic acid (IDA), nitrilotriacetic acid (NTA), and ethylenediaminetetraacetic acid (EDTA).
An addition amount of the chelating agent is, for example, preferably in a range of 0.01 parts by weight to 5.0 parts by weight, and more preferably in a range of 0.1 parts by weight to less than 3.0 parts by weight relative to 100 parts by weight of the resin particles.
Coalescence Process
Next, the aggregated particle dispersion in which the aggregated particles are dispersed is heated at, for example, a temperature that is equal to or higher than the glass transition temperature of the resin particles (for example, a temperature that is higher than the glass transition temperature of the resin particles by 10° C. to 30° C.) to coalesce the aggregated particles and form toner particles.
Toner particles are obtained through the foregoing processes.
After the aggregated particle dispersion in which the aggregated particles are dispersed is obtained, toner particles may be prepared through the processes of: further mixing the resin particle dispersion in which the resin particles are dispersed with the aggregated particle dispersion to conduct aggregation so that the resin particles further adhere to the surfaces of the aggregated particles, thereby forming second aggregated particles; and coalescing the second aggregated particles by heating the second aggregated particle dispersion in which the second aggregated particles are dispersed, thereby forming toner particles having a core/shell structure.
Here, the resin particles attached to the surface of the aggregated particles may be the amorphous resin particles.
After the coalescence process ends, the toner particles formed in the solution are subjected to a washing process, a solid-liquid separation process, and a drying process, that are well known, and thus dry toner particles are obtained.
In the washing process, preferably, displacement washing using ion exchange water is sufficiently performed from the viewpoint of charging properties. In addition, the solid-liquid separation process is not particularly limited, and suction filtration, pressure filtration, or the like may be performed from the viewpoint of productivity. The method for the drying process is also not particularly limited, and freeze drying, flush drying, fluidized drying, vibration-type fluidized drying, or the like may be performed from a viewpoint of productivity.
Next, a case of preparing the toner particles including the urea-modified polyester resin (urea-modified amorphous polyester resin) will be described.
The toner particles including the urea-modified polyester resin may be obtained by a dissolution and suspension method described below. A method of obtaining toner particles including the urea-modified polyester resin (urea-modified amorphous polyester resin) and an unmodified crystalline polyester resin as binder resins will be described, but toner particles may include an unmodified amorphous polyester resin as the binder resin. A method of obtaining toner particles including a colorant and a release agent will be described, but the colorant and the release agent are components included in the toner particles, if necessary.
Oil-Phase Solution Preparation Process
An oil-phase solution obtained by dissolving or dispersing a toner particle material including an unmodified crystalline polyester resin (hereinafter, also simply referred to as a “crystalline polyester resin”), an amorphous polyester prepolymer including an isocyanate group, an amine compound, a colorant, and a release agent in an organic solvent is prepared (oil-phase solution preparation process). The oil-phase solution preparation process is a process of dissolving or dispersing the toner particle material in an organic solvent to obtain a mixed solution of the toner material.
The oil-phase solution is prepared by methods such as 1) a method of preparing an oil-phase solution by collectively dissolving or dispersing the toner material in an organic solvent, 2) a method of preparing an oil-phase solution by kneading the toner material in advance and dissolving or dispersing the kneaded material in an organic solvent, 3) a method of preparing an oil-phase solution by dissolving the crystalline polyester resin, the amorphous polyester prepolymer including an isocyanate group, and the amine compound in an organic solvent and dispersing a colorant and the release agent in the organic solvent, 4) a method of preparing an oil-phase solution by dispersing a colorant and the release agent in the organic solvent and dissolving the crystalline polyester resin, the amorphous polyester prepolymer including an isocyanate group, and the amine compound in the organic solvent, 5) a method of preparing an oil-phase solution by dissolving or dispersing toner particle materials other than the amorphous polyester prepolymer including an isocyanate group and the amine compound (the crystalline polyester resin, a colorant, and a release agent) in an organic solvent and dissolving the amorphous polyester prepolymer including an isocyanate group and the amine compound in the organic solvent, or 6) a method of preparing an oil-phase solution by dissolving or dispersing toner particle materials other than the amorphous polyester prepolymer including an isocyanate group or the amine compound (the crystalline polyester resin, a colorant, and a release agent) in an organic solvent and dissolving the amorphous polyester prepolymer including an isocyanate group or the amine compound in the organic solvent. The method of preparing the oil-phase solution is not limited thereto.
Examples of the organic solvent of the oil-phase solution include an ester solvent such as methyl acetate or ethyl acetate; a ketone solvent such as methyl ethyl ketone or methyl isopropyl ketone; an aliphatic hydrocarbon solvent such as hexane or cyclohexane; a halogenated hydrocarbon solvent such as dichloromethane, chloroform or trichloroethylene. It is preferable that these organic solvents dissolve the binder resin, a rate of the organic solvent dissolving in water is from approximately 0% by weight to 30% by weight, and a boiling point is equal to or lower than 100° C. Among the organic solvents, ethyl acetate is preferable.
Suspension Preparation Process
Next, a suspension is prepared by dispersing the obtained oil-phase solution in a water-phase solution (suspension preparation process).
A reaction between the amorphous polyester prepolymer including an isocyanate group and the amine compound is performed together with the preparation of the suspension. The urea-modified polyester resin is prepared by the reaction. The reaction is performed with at least one reaction of the crosslinking reaction and the extension reaction of molecular chains. The reaction between the amorphous polyester prepolymer including an isocyanate group and the amine compound may be performed with the following organic solvent removing process.
Here, the reaction conditions are selected according to reactivity between the structure of isocyanate group included in the amorphous polyester prepolymer and the amine compound. As an example, a reaction time is preferably 10 minutes to 40 hours and more preferably 2 hours to 24 hours. A reaction temperature is preferably 0° C. to 150° C. and more preferably 40° C. to 98° C. In addition, a well-known catalyst (dibutyltin laurate or di-octyltin laurate) may be used if necessary, in the formation of the urea-modified polyester resin. That is, a catalyst may be added to the oil-phase solution or the suspension.
As the water-phase solution, a water-phase solution obtained by dispersing a particle dispersing agent such as an organic particle dispersing agent or an inorganic particle dispersing agent in an aqueous solvent is used. In addition, as the water-phase solution, a water-phase solution obtained by dispersing a particle dispersing agent in an aqueous solvent and dissolving a polymer dispersing agent in an aqueous solvent is also used. Further, a well-known additive such as a surfactant may be added to the water-phase solution.
As the aqueous solvent, water (for example, generally ion exchange water, distilled water, or pure water) is used. The aqueous solvent may be a solvent containing water and an organic solvent such as alcohol (methanol, isopropyl alcohol, or ethylene glycol), dimethylformamide, tetrahydrofuran, cellosolves (methyl cellosolve), or lower ketones (acetone or methyl ethyl ketone).
As the organic particle dispersing agent, a hydrophilic organic particle dispersing agent is used. As the organic particle dispersing agent, particles of poly (meth)acrylic acid alkyl ester resin (for example, a polymethyl methacrylate resin), a polystyrene resin, or a poly(styrene-acrylonitrile) resin are used. As the organic particle dispersing agent, particles of a styrene acrylic resin are also used.
As the inorganic particle dispersing agent, a hydrophilic inorganic particle dispersing agent is used. Specific examples of the inorganic particle dispersing agent include particles of silica, alumina, titania, calcium carbonate, magnesium carbonate, tricalcium phosphate, clay, diatomaceous earth, or bentonite, and particles of calcium carbonate are preferable. The inorganic particle dispersing agent may be used singly or in combination of two or more kinds thereof.
The surface of the particle dispersing agent may be subjected to surface treatment by a polymer including a carboxyl group.
As the polymer including a carboxyl group, a copolymer of at least one kind selected from salts (alkali metal salt, alkaline earth metal salt, ammonium salt, amine salt) in which α,β-monoethylenically unsaturated carboxylic acid or a carboxyl group of α,β-monoethylenically unsaturated carboxylic acid is neutralized by alkali metal, alkaline earth metal, ammonium, or amine, and α,β-monoethylenically unsaturated carboxylic acid ester is used. As the polymer including a carboxyl group, salt (alkali metal salt, alkaline earth metal salt, ammonium salt, amine salt) in which a carboxyl group of a copolymer of α,β-monoethylenically unsaturated carboxylic acid and α,β-monoethylenically unsaturated carboxylic acid ester is neutralized by alkali metal, alkaline earth metal, ammonium, or amine is also used. The polymer including a carboxyl group may be used singly or in combination with two or more kinds thereof.
Representative examples of α,β-monoethylenically unsaturated carboxylic acid include α,β-unsaturated monocarboxylic acid (acrylic acid, methacrylic acid, or crotonic acid), and α,β-unsaturated dicarboxylic acids (maleic acid, fumaric acid, or itaconic acid). Representative examples of α,β-monoethylenically unsaturated carboxylic acid ester include alkyl esters of (meth)acrylate, (meth)acrylate including an alkoxy group, (meth)acrylate including a cyclohexyl group, (meth)acrylate including a hydroxy group, and polyalkylene glycol mono(meth)acrylate.
As the polymer dispersing agent, a hydrophilic polymer dispersing agent is used. As the polymer dispersing agent, specifically a polymer dispersing agent which includes a carboxyl group and does not include lipophilic group (hydroxypropoxy group or a methoxy group) (for example, water-soluble cellulose ether such as carboxymethyl cellulose or carboxyethyl cellulose) is used.
Solvent Removing Process
Next, a toner particle dispersion is obtained by removing an organic solvent from the obtained suspension (solvent removing process). The solvent removing process is a process of forming toner particles by removing the organic solvent contained in liquid droplets of the water-phase solution dispersed in the suspension. The method of removing the organic solvent from the suspension may be performed immediately after the suspension preparation process or may be performed after 1 minute or longer, after the suspension preparation process.
In the solvent removing process, the organic solvent may be removed from the suspension by cooling or heating the obtained suspension to have a temperature in a range of 0° C. to 100° C., for example.
As a specific method of the organic solvent removing method, the following method is used.
(1) A method of allowing airflow to blow to the suspension to forcibly update a gas phase on the surface of the suspension. In this case, gas may flow into the suspension.
(2) A method of reducing pressure. In this case, a gas phase on the surface of the suspension may be forcibly updated due to filling of gas or gas may further blow into the suspension.
The toner particles are obtained through the above-mentioned processes.
Here, after the organic solvent removing process ends, the toner particles formed in the toner particle dispersion are subjected to a well-known washing process, a well-known solid-liquid separation process, a well-known drying process, and thereby dried toner particles are obtained.
Regarding the washing process, replacing washing using ion exchanged water may preferably be sufficiently performed for charging properties.
The solid-liquid separation process is not particularly limited, but suction filtration, pressure filtration, or the like may preferably be performed for productivity. The drying process is not particularly limited, but freeze drying, flush drying, fluidized drying, vibrating fluidized drying, and the like may preferably be performed for productivity.
Next, the annealing process will be described.
In the preparing process of the toner particles, for example, an annealing process (heating process) may be performed with respect to the toner particles obtained through the processes described above.
Specifically, for example, the obtained toner particles are heated to a temperature of 40° C. to 70° C. and kept at that temperature for the time in a range of 0.5 hours to 10 hours. By performing the process, the phase separation between the crystalline resin and the amorphous resin proceeds in the obtained toner particles. Accordingly, in the toner, Expression (1): 0.50≤S1/Sh≤0.90 is easily satisfied.
The performing time of the annealing process is not limited as described above, as long as the process of extremely changing the “state in which the amorphous resin and the crystalline resin are compatible with each other” of the toner particles (process of setting the Expression (1): 0.50≤S1/Sh≤0.90 not to be satisfied in the toner) is not performed after the annealing process, and, for example, the annealing process may be performed with a dispersion formed as the toner particles or in a slurry state in which the amount of the solvent of the dispersion is decreased.
In addition, the following process may be performed, for example. First, a dispersion obtained by re-dispersing the obtained toner particles in a dispersion medium (for example, water or the like) is obtained. In the toner particle dispersion, after increasing the temperature to a temperature equal to or higher than the glass transition temperature of the amorphous polyester resin (specifically, preferably equal to or higher than the glass transition temperature of the amorphous polyester resin by 5° C. and more preferably equal to or higher than the glass transition temperature of the amorphous polyester resin by 10° C.), the temperature is kept for 0.5 hours to 10 hours (preferably 2 hours to 8 hours). After that, the toner particles are rapidly cooled (for example, rapidly cooled preferably at 5° C./min to 30° C./min and more preferably at 10° C./min to 20° C./min). By performing the process, toner particles in which compatibilizing between the amorphous resin and the crystalline resin has been excessively proceeded are temporarily obtained. After that, when the annealing process is performed under the conditions described above, the phase separation between the crystalline resin and the amorphous resin easily proceeds in the obtained toner particles, in a desired range (range of satisfying Expression (1): 0.50≤S1/Sh≤0.90).
In a case of preparing the toner particles by an aggregation and coalescence method, in the aggregation and coalescence process, when the temperature is kept at a temperature at which the aggregation and coalescence method is performed, for 0.5 hours to 20 hours (preferably 5 hours to 15 hours) and rapid cooling is performed under the conditions described above, toner particles in which compatibilizing between the amorphous resin and the crystalline resin has been excessively proceeded may be temporarily obtained. After that, when the annealing process is performed under the conditions described above, the phase separation between the crystalline resin and the amorphous resin easily proceeds in a desired range (range of satisfying Expression (1): 0.50≤S1/Sh≤0.90) in the obtained toner particles.
The toner according to the exemplary embodiment is, for example, prepared by adding an external additive to the obtained dry toner particles and mixing the materials. The mixing may be performed in a V blender, a HENSCHEL MIXER, a LÖDIGE mixer, and the like. Further, if necessary, coarse toner particles may be removed with a vibration classifier, a wind classifier, and the like.
Electrostatic Charge Image Developer
An electrostatic charge image developer according to the exemplary embodiment includes at least the toner according to the exemplary embodiment.
The electrostatic charge image developer according to the exemplary embodiment may be a single-component developer including only the toner according to the exemplary embodiment or may be a two-component developer obtained by mixing the toner and a carrier.
The carrier is not particularly limited and known carriers are exemplified. Examples of the carrier include a coating carrier in which surfaces of cores formed of magnetic particles are coated with a coating resin; magnetic particles dispersion-type carrier in which magnetic particles is dispersed and blended in a matrix resin; and a resin impregnation-type carrier in which porous magnetic particles are impregnated with a resin.
The magnetic particle dispersion-type carrier and the resin impregnation-type carrier may be carriers in which constituent particles of the carrier are cores and coated with a coating resin.
Examples of the magnetic particles include magnetic metals such as iron, nickel, and cobalt, and magnetic oxides such as ferrite and magnetite.
Examples of the resin for coating and matrix resin include polyethylene, polypropylene, polystyrene, polyvinyl acetate, polyvinyl alcohol, polyvinyl butyral, polyvinyl chloride, polyvinyl ether, polyvinyl ketone, a vinyl chloride-vinyl acetate copolymer, a styrene-acrylic acid ester copolymer, a straight silicone resin configured to include an organosiloxane bond or a modified product thereof, a fluorine resin, polyester, polycarbonate, a phenol resin, and an epoxy resin.
The coating resin and the matrix resin may contain other additives such as conductive materials.
Examples of the conductive particles include particles of metals such as gold, silver, and copper, carbon black particles, titanium oxide particles, zinc oxide particles, tin oxide particles, barium sulfate particles, aluminum borate particles, and potassium titanate particles.
Here, a coating method using a coating layer forming solution in which a coating resin, and if necessary, various additives are dissolved in an appropriate solvent is used to coat the surface of a core with the coating resin. The solvent is not particularly limited, and may be selected in consideration of the coating resin to be used, coating suitability, and the like.
Specific examples of the resin coating method include a dipping method of dipping cores in a coating layer forming solution, a spraying method of spraying a coating layer forming solution to surfaces of cores, a fluid bed method of spraying a coating layer forming solution in a state in which cores are allowed to float by flowing air, and a kneader-coater method in which cores of a carrier and a coating layer forming solution are mixed with each other in a kneader-coater and the solvent is removed.
The mixing ratio (weight ratio) between the toner and the carrier in the two-component developer is preferably 1:100 to 30:100, and more preferably 3:100 to 20:100 (toner:carrier).
Image Forming Apparatus and Image Forming Method
An image forming apparatus and an image forming method according to the exemplary embodiment will be described.
The image forming apparatus according to the exemplary embodiment is provided with an image holding member, a charging unit that charges a surface of the image holding member, an electrostatic charge image forming unit that forms an electrostatic charge image on the charged surface of the image holding member, a developing unit that contains a container that contains an electrostatic charge image developer and develops the electrostatic charge image formed on the surface of the image holding member with the electrostatic charge image developer as a toner image, a transfer unit that transfers the toner image formed onto the surface of the image holding member to a surface of a recording medium, and a fixing unit that fixes the toner image transferred onto the surface of the recording medium. As the electrostatic charge image developer, the electrostatic charge image developer according to the exemplary embodiment is applied.
In the image forming apparatus according to the exemplary embodiment, an image forming method (image forming method according to the exemplary embodiment) including the processes of: charging a surface of an image holding member; forming an electrostatic charge image on the charged surface of the image holding member; developing the electrostatic charge image formed on the surface of the image holding member with the electrostatic charge image developer according to the exemplary embodiment as a toner image; transferring the toner image formed onto the surface of the image holding member to a surface of a recording medium; and fixing the toner image transferred onto the surface of the recording medium is performed.
As the image forming apparatus according to the exemplary embodiment, a known image forming apparatus is applied, such as a direct transfer type apparatus that directly transfers a toner image formed on a surface of an image holding member onto a recording medium; an intermediate transfer type apparatus that primarily transfers a toner image formed on a surface of an image holding member onto a surface of an intermediate transfer member, and secondarily transfers the toner image transferred to the surface of the intermediate transfer member onto a surface of a recording medium; an apparatus that is provided with a cleaning unit that cleans a surface of an image holding member before charging after transfer of a toner image; or an apparatus that is provided with an erasing unit that irradiates, after transfer of a toner image, a surface of an image holding member with erase light before charging for erasing.
In the case of an intermediate transfer type apparatus, a transfer unit is configured to have, for example, an intermediate transfer member having a surface to which a toner image is to be transferred, a primary transfer unit that primarily transfers a toner image formed on a surface of an image holding member onto the surface of the intermediate transfer member, and a secondary transfer unit that secondarily transfers the toner image transferred onto the surface of the intermediate transfer member onto a surface of a recording medium.
In the image forming apparatus according to the exemplary embodiment, for example, a part including the developing unit may have a cartridge structure (process cartridge) that is detachable from the image forming apparatus. As the process cartridge, for example, a process cartridge that includes a container that contains the electrostatic charge image developer according to the exemplary embodiment and is provided with a developing unit is suitably used.
Hereinafter, an example of the image forming apparatus according to the exemplary embodiment will be shown. However, the image forming apparatus is not limited thereto. Main portions shown in the drawing will be described, but descriptions of other portions will be omitted.
The image forming apparatus shown in
An intermediate transfer belt 20 as an intermediate transfer member is installed above the units 10Y, 10M, 10C, and 10K in the drawing to extend through the units. The intermediate transfer belt 20 is wound on a driving roll 22 and a support roll 24 contacting the inner surface of the intermediate transfer belt 20, which are disposed to be separated from each other on the left and right sides in the drawing, and travels in a direction toward the fourth unit 10K from the first unit 10Y. The support roll 24 is pressed in a direction in which it departs from the driving roll 22 by a spring or the like (not shown), and a tension is given to the intermediate transfer belt 20 wound on both of the rolls. In addition, an intermediate transfer member cleaning device 30 opposed to the driving roll 22 is provided on a surface of the intermediate transfer belt 20 on the image holding member side.
Developing devices (developing units) 4Y, 4M, 4C, and 4K of the units 10Y, 10M, 10C, and 10K are supplied with toner including four color toner, that is, a yellow toner, a magenta toner, a cyan toner, and a black toner accommodated in toner cartridges 8Y, 8M, 8C, and 8K, respectively.
The first to fourth units 10Y, 10M, 10C, and 10K have the same configuration, and accordingly, only the first unit 10Y that is disposed on the upstream side in a traveling direction of the intermediate transfer belt to form a yellow image will be representatively described here. The same parts as in the first unit 10Y will be denoted by the reference numerals with magenta (M), cyan (C), and black (K) added instead of yellow (Y), and descriptions of the second to fourth units 10M, 10C, and 10K will be omitted.
The first unit 10Y has a photoreceptor 1Y acting as an image holding member. Around the photoreceptor 1Y, a charging roll (an example of the charging unit) 2Y that charges a surface of the photoreceptor 1Y to a predetermined potential, an exposure device (an example of the electrostatic charge image forming unit) 3 that exposes the charged surface with laser beams 3Y based on a color-separated image signal to form an electrostatic charge image, a developing device (an example of the developing unit) 4Y that supplies a charged toner to the electrostatic charge image to develop the electrostatic charge image, a primary transfer roll (an example of the primary transfer unit) 5Y that transfers the developed toner image onto the intermediate transfer belt 20, and a photoreceptor cleaning device (an example of the cleaning unit) 6Y that removes the toner remaining on the surface of the photoreceptor 1Y after primary transfer, are arranged in sequence.
The primary transfer roll 5Y is disposed inside the intermediate transfer belt 20 to be provided at a position opposed to the photoreceptor 1Y. Furthermore, bias supplies (not shown) that apply a primary transfer bias are connected to the primary transfer rolls 5Y, 5M, 5C, and 5K, respectively. Each bias supply changes a transfer bias that is applied to each primary transfer roll under the control of a controller (not shown).
Hereinafter, an operation of forming a yellow image in the first unit 10Y will be described.
First, before the operation, the surface of the photoreceptor 1Y is charged to a potential of −600 V to −800 V by the charging roll 2Y.
The photoreceptor 1Y is formed by laminating a photosensitive layer on a conductive substrate (for example, volume resistivity at 20° C.: 1×10−6 Ωcm or less). The photosensitive layer typically has high resistance (that is about the same as the resistance of a general resin), but has properties in which when laser beams 3Y are applied, the specific resistance of a part irradiated with the laser beams changes. Accordingly, the laser beams 3Y are output to the charged surface of the photoreceptor 1Y via the exposure device 3 in accordance with image data for yellow sent from the controller (not shown). The laser beams 3Y are applied to the photosensitive layer on the surface of the photoreceptor 1Y, whereby an electrostatic charge image of a yellow image pattern is formed on the surface of the photoreceptor 1Y.
The electrostatic charge image is an image that is formed on the surface of the photoreceptor 1Y by charging, and is a so-called negative latent image, that is formed by irradiating the photosensitive layer with laser beams 3Y so that the specific resistance of the irradiated part is lowered to cause charges to flow on the surface of the photoreceptor 1Y, while charges stay on a part which is not irradiated with the laser beams 3Y.
The electrostatic charge image formed on the photoreceptor 1Y is rotated up to a predetermined developing position with the travelling of the photoreceptor 1Y. The electrostatic charge image on the photoreceptor 1Y is visualized (developed) as a toner image at the developing position by the developing device 4Y.
The developing device 4Y accommodates, for example, an electrostatic charge image developer including at least a yellow toner and a carrier. The yellow toner is frictionally charged by being stirred in the developing device 4Y to have a charge with the same polarity (negative polarity) as the charge that is on the photoreceptor 1Y, and is thus held on the developer roll (an example of the developer holding member). By allowing the surface of the photoreceptor 1Y to pass through the developing device 4Y, the yellow toner electrostatically adheres to the erased latent image part on the surface of the photoreceptor 1Y, whereby the latent image is developed with the yellow toner. Next, the photoreceptor 1Y having the yellow toner image formed thereon continuously travels at a predetermined rate and the toner image developed on the photoreceptor 1Y is transported to a predetermined primary transfer position.
When the yellow toner image on the photoreceptor 1Y is transported to the primary transfer position, a primary transfer bias is applied to the primary transfer roll 5Y and an electrostatic force toward the primary transfer roll 5Y from the photoreceptor 1Y acts on the toner image, whereby the toner image on the photoreceptor 1Y is transferred onto the intermediate transfer belt 20. The transfer bias applied at this time has the opposite polarity (+) to the toner polarity (−), and, for example, is controlled to +10 μA in the first unit 10Y by the controller (not shown).
On the other hand, the toner remaining on the photoreceptor 1Y is removed and collected by the photoreceptor cleaning device 6Y.
The primary transfer biases that are applied to the primary transfer rolls 5M, 5C, and 5K of the second unit 10M and the subsequent units are also controlled in the same manner as in the case of the first unit.
In this manner, the intermediate transfer belt 20 onto which the yellow toner image is transferred in the first unit 10Y is sequentially transported through the second to fourth units 10M, 10C, and 10K, and the toner images of respective colors are multiply-transferred in a superimposed manner.
The intermediate transfer belt 20 onto which the four color toner images have been multiply-transferred through the first to fourth units reaches a secondary transfer part that is composed of the intermediate transfer belt 20, the support roll 24 contacting the inner surface of the intermediate transfer belt, and a secondary transfer roll (an example of the secondary transfer unit) 26 disposed on the image holding surface side of the intermediate transfer belt 20. Meanwhile, a recording sheet (an example of the recording medium) P is supplied to a gap between the secondary transfer roll 26 and the intermediate transfer belt 20, that are brought into contact with each other, via a supply mechanism at a predetermined timing, and a secondary transfer bias is applied to the support roll 24. The transfer bias applied at this time has the same polarity (−) as the toner polarity (−), and an electrostatic force toward the recording sheet P from the intermediate transfer belt 20 acts on the toner image, whereby the toner image on the intermediate transfer belt 20 is transferred onto the recording sheet P. In this case, the secondary transfer bias is determined depending on the resistance detected by a resistance detector (not shown) that detects the resistance of the secondary transfer part, and is voltage-controlled.
Thereafter, the recording sheet P is fed to a pressure-contacting part (nip part) between a pair of fixing rolls in a fixing device (an example of the fixing unit) 28 so that the toner image is fixed to the recording sheet P, whereby a fixed image is formed.
Examples of the recording sheet P onto which a toner image is transferred include plain paper that is used in electrophotographic copying machines, printers, and the like. As a recording medium, an OHP sheet is also exemplified other than the recording sheet P.
The surface of the recording sheet P is preferably smooth in order to further improve smoothness of the image surface after fixing. For example, coated paper obtained by coating a surface of plain paper with a resin or the like, art paper for printing, and the like are preferably used.
The recording sheet P on which the fixing of the color image is completed is discharged toward a discharge part, and a series of the color image forming operations end.
Process Cartridge/Toner Cartridge
A process cartridge according to the exemplary embodiment will be described.
The process cartridge according to the exemplary embodiment includes a developing unit that includes a container that contains the electrostatic charge image developer according to the exemplary embodiment and develops an electrostatic charge image formed on a surface of an image holding member with the electrostatic charge image developer as a toner image, and is detachable from an image forming apparatus.
The process cartridge according to the exemplary embodiment is not limited to the above-described configuration, and may be configured to include a developing device, and if necessary, at least one selected from other units such as an image holding member, a charging unit, an electrostatic charge image forming unit, and a transfer unit.
Hereinafter, an example of the process cartridge according to the exemplary embodiment will be shown. However, the process cartridge is not limited thereto. Major parts shown in the drawing will be described, but descriptions of other parts will be omitted.
A process cartridge 200 shown in
In
Next, a toner cartridge according to the exemplary embodiment will be described.
The toner cartridge according to the exemplary embodiment includes a container that contains the toner according to the exemplary embodiment and is detachable from an image forming apparatus. The toner cartridge includes a container that contains a toner for replenishment for being supplied to the developing unit provided in the image forming apparatus.
The image forming apparatus shown in
Hereinafter, the exemplary embodiment of the invention will be described in detail using examples and comparative examples, but the exemplary embodiment of the invention is not limited to the examples. Unless specifically noted, “parts” and “%” represent “parts by weight” and “% by weight”.
Preparation of Toner Particles (A1)
Preparation of amorphous polyester resin particle dispersion (A1)
The above materials are put in a 5-liter flask equipped with a stirrer, a nitrogen gas introducing tube, a temperature sensor, and a rectifying column, the temperature is increased to 220° C. over 1 hour, and 1 part of titanium tetraethoxide with respect to 100 parts of the materials described above is put therein. The temperature is increased to 230° C. over 0.5 hours while distilling away generated water, a dehydration condensation reaction is continued at the temperature for 1 hour, and then the reactant is cooled. Thus, the amorphous polyester resin (A1) having a weight average molecular weight of 19,000, an acid value of 14 mgKOH/g, and a glass transition temperature of 58° C. is synthesized.
Then, 40 parts of ethyl acetate and 25 parts of 2-butanol are put into a container equipped with a temperature adjusting unit and a nitrogen substituting unit to prepare a mixed solution, 100 parts of the amorphous polyester resin (A1) is slowly put therein and dissolved, and 10 weight % ammonia aqueous solution is put therein in an amount equivalent to three times amount of the acid value of the resin in terms of mol and stirred for 30 minutes.
Then, the atmosphere in the container is substituted with dry nitrogen, the temperature is held at 40° C., and 400 parts of ion exchange water is added dropwise at a rate of 2 parts/min while stirring the mixed solution to perform emulsification. After finishing the adding dropwise, the temperature of the emulsified solution is returned to room temperature (20° C. to 25° C.), bubbling is performed with dry nitrogen for 48 hours while stirring the solution, the content of ethyl acetate and 2-butanol is decreased to 1,000 ppm or smaller, and a resin particle dispersion in which resin particles having a volume average particle diameter of 200 nm are dispersed is obtained. Ion exchange water is added to the resin particle dispersion to adjust the solid content to 20% by weight, and thus, an amorphous polyester resin particle dispersion (A1) is obtained.
Preparation of crystalline polyester resin particle dispersion (A1)
The monomer components are put into a reaction vessel equipped with a stirrer, a thermometer, a condenser, and a nitrogen gas introducing tube, the inside of the reaction vessel is substituted with dry nitrogen gas, and 0.25 parts of titanium tetrabutoxide (reagent) with respect to 100 parts of the monomer components described above is put therein. After stirring and allowing a reaction under the nitrogen gas atmosphere at 170° C. for 3 hours, the temperature is further increased to 210° C. over 1 hour, the pressure in the reaction vessel is reduced to 3 kPa, the reaction is performed under reduced pressure for 13 hours, and thus, a crystalline polyester resin (A1) is obtained.
With respect to the obtained crystalline polyester resin (A1), the melting temperature provided by DSC measurement is 73.6° C., the weight average molecular weight Mw measured by GPC is 25,000, the number average molecular weight Mn measured by GPC is 10,500, and the acid value AV is 10.1 mgKOH/g.
Then, 300 parts of the crystalline polyester resin (1), 160 parts of methyl ethyl ketone (solvent), and 100 parts of isopropyl alcohol (solvent) are put in a 3-liter reaction vessel with a jacket (BJ-30N, manufactured by Tokyo Rikakikai Co, Ltd.) which is provided with a condenser, a thermometer, a water dropping device, and an anchor blade, stirred and mixed at 100 rpm to dissolve the resin, while maintaining the temperature at 70° C. in a water circulation type thermostatic bath (dissolved solution preparing method).
After that, the stirring rotation rate is set as 150 rpm, the temperature of the water circulation type thermostatic bath is set as 66° C., 17 parts of 10% ammonia aqueous solution (reagent) is put therein over 10 minutes, and 900 parts in total of ion exchange water warmed at 66° C. is added dropwise at a rate of 7 parts/min to cause the phase transition, thereby obtaining an emulsified solution.
Immediately, 800 parts of the obtained emulsified solution and 700 parts of ion exchange water are put in a 2-liter eggplant flask and the resultant is set in an evaporator (Tokyo Rikakikai Co., Ltd.) with a vacuum control unit through a trap ball. While rotating the eggplant flask, heating is performed with hot water at 60° C., and the pressure is reduced to 7 kPa while paying attention to bumping, so that the solvent is removed. At the time when the amount of the solvent collected becomes 1,100 parts, the pressure is returned to normal pressure and the eggplant flask is cooled, thereby obtaining a dispersion. The obtained dispersion has no smell of the solvent. A volume average particle diameter D50v of the resin particles of the dispersion is 130 nm. After that, the solid content concentration is adjusted to 20% by adding ion exchange water, and the resultant is designated as a crystalline polyester resin particle dispersion (A1).
Preparation of Colorant Particle Dispersion (A1)
The above components are mixed with each other, and dispersed with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.) for 10 minutes. Ion exchange water is added so that the solid content in the dispersion becomes 20% by weight, and a colorant particle dispersion (A1) in which colorant particles having a volume average particle diameter of 140 nm are dispersed is obtained.
Preparation of Release Agent Particle Dispersion (A1)
The above materials are mixed with each other, heated to 100° C., and dispersed with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.). After that, the mixture is subject to dispersion treatment with MANTON-GAULIN HIGH PRESSURE HOMOGENIZER (manufactured by Gaulin Co., Ltd.), and thus, a release agent particle dispersion (A1) (solid content of 20% by weight) in which release agent particles having a volume average particle diameter of 200 nm are dispersed is obtained.
Preparation of Toner Particles
The above materials are put into a round stainless steel flask, 0.1 N of nitric acid is added thereto to adjust the pH to 3.5, and then, and 30 parts of a nitric acid aqueous solution having polyaluminum chloride concentration of 10% by weight is added thereto. Then, the resultant material is dispersed at 30° C. with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.), heated to 40° C. in a heating oil bath, and kept for 30 minutes. After that, 100 parts of the amorphous polyester resin particle dispersion (A1) is gently added and maintained for 1 hour, 0.1 N of sodium hydroxide aqueous solution is added to adjust the pH to 8.5, and the mixture is heated to 105° C. with stirring and then maintained for 10 hours. After that, the mixture is cooled to 20° C. at a rate of 20° C./min, heated to 45° C. again, the annealing process is performed for 5 hours, and cooling is performed to 20° C. at a rate of 20° C./min. Then, the mixture is filtered, sufficiently washed with ion exchange water, and dried, and thus, toner particles having a volume average particle diameter of 4.0 μm are obtained.
Preparation of Toner Particles (A2)
Toner particles (A2) are obtained in the same manner as in the preparation of the toner particles (A1) except that the temperature is 45° C. and the keeping time is 3 hours in the conditions of the annealing process.
Preparation of Toner Particles (A3)
Toner particles (A3) are obtained in the same manner as in the preparation of the toner particles (A1) except that the temperature is 45° C. and the keeping time is 7 hours in the conditions of the annealing process.
Preparation of Toner Particles (A4)
Toner particles (A4) are obtained in the same manner as in the preparation of the toner particles (A1) except that the temperature is 45° C. and the keeping time is 4 hours in the conditions of the annealing process.
Preparation of Toner Particles (A5)
Toner particles (A5) are obtained in the same manner as in the preparation of the toner particles (A1) except that the temperature is 45° C. and the keeping time is 6 hours in the conditions of the annealing process.
Preparation of Toner Particles (A6)
Toner particles (A6) are obtained in the same manner as in the preparation of the toner particles (A1), except for using an amorphous polyester resin particle dispersion (A2) described below instead of the amorphous polyester resin particle dispersion (A1), and using a crystalline polyester resin particle dispersion (A2) described below instead of the crystalline polyester resin particle dispersion (A1).
Preparation of Amorphous Polyester Resin Particle Dispersion (A2)
An amorphous polyester resin particle dispersion (A2) is obtained in the same manner as in the preparation of the amorphous polyester resin particle dispersion (A1), except for changing the amount of ethylene glycol to 1 part by mol and the amount of bisphenol A propylene oxide adduct to 94 parts by mol.
A glass transition temperature Tg of the amorphous polyester resin (A2) is 60° C.
Preparation of Crystalline Polyester Resin Particle Dispersion (A2)
A crystalline polyester resin particle dispersion (A2) is obtained in the same manner as in the preparation of the crystalline polyester resin particle dispersion (A1), except for changing 1,9-nonanediol to 1,4-butanediol.
A melting temperature of the crystalline polyester resin (A2) measured by DSC is 59.0° C.
Preparation of Toner Particles (A7)
Toner particles (A7) are obtained in the same manner as in the preparation of the toner particles (A1), except for using an amorphous polyester resin particle dispersion (A3) described below instead of the amorphous polyester resin particle dispersion (A1), and using a crystalline polyester resin particle dispersion (A3) described below instead of the crystalline polyester resin particle dispersion (A1).
Preparation of Amorphous Polyester Resin Particle Dispersion (A3)
An amorphous polyester resin particle dispersion (A3) is obtained in the same manner as in the preparation of the amorphous polyester resin particle dispersion (A1), except for changing the amount of ethylene glycol to 5 parts by mol and the amount of bisphenol A propylene oxide adduct to 90 parts by mol.
A glass transition temperature Tg of the amorphous polyester resin (A3) is 56° C.
Preparation of Crystalline Polyester Resin Particle Dispersion (A3)
A crystalline polyester resin particle dispersion (A3) is obtained in the same manner as in the preparation of the crystalline polyester resin particle dispersion (A1), except for changing 1,9-nonanediol to 1,12-dodecanediol.
A melting temperature of the crystalline polyester resin (A3) measured by DSC is 81.0° C.
Preparation of Toner Particles (P1)
Synthesis of Crystalline Polyester Resin (P1)
80.9 parts of fumaric acid, 46.3 parts of 1,10-decanediol, and 1 part of titanium tetraethoxide with respect to 100 parts of the materials (fumaric acid and 1,10-decanediol) are put in a 5-liter flask equipped with a stirrer, a nitrogen gas introducing tube, a temperature sensor, and a rectifying column. The reaction is performed at 150° C. for 4 hours while removing generated water, the temperature is increased to 18° C. for 6 hours under the nitrogen atmosphere, and the reaction is performed at 180° C. over 6 hours. After that, the reaction is performed under the reduced pressure for 1 hour, and then cooling is performed, thereby obtaining an unmodified crystalline polyester resin (P1).
Synthesis of Amorphous Polyester Resin (P1)
30 parts of isophthalic acid, 70 parts of fumaric acid, 5 parts by mol of bisphenol A ethylene oxide adduct, and 95 parts of bisphenol A propylene oxide adduct are put in a 5-liter flask equipped with a stirrer, a nitrogen gas introducing tube, a temperature sensor, and a rectifying column, the temperature is increased to 220° C. over 1 hour, 1 part of titanium tetraethoxide with respect to 100 parts of the materials (isophthalic acid, fumaric acid, bisphenol A ethylene oxide adduct, and bisphenol A propylene oxide adduct) is put therein. The temperature is increased to 230° C. over 0.5 hours while distilling away generated water, a dehydration condensation reaction is continued at the temperature for 1 hour, and then the reactant is cooled. After that, isophorone diisocyanate is added so that the content thereof is 2 parts with respect to 1 part of the resin, 5 parts of ethyl acetate is added and dissolved, the reaction is performed at 200° C. for 3 hours, and then the materials are cooled, and thus, an amorphous polyester resin (P1) including an isocyanate group at a terminal is obtained. The glass transition temperature Tg of the amorphous polyester resin (P1) is 60° C.
Preparation of Release Agent Particle Dispersion
100 parts of Paraffin Wax (HNP-9 manufactured by Nippon Seiro Co., Ltd.), 1 part of an anionic surfactant (NEOGEN RK manufactured by DKS Co., Ltd.), and 350 parts of ion exchange water are mixed with each other, heated at 100° C., dispersed with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.). After that, the mixture is subject to dispersion treatment with MANTON-GAULIN HIGH PRESSURE HOMOGENIZER (manufactured by Gaulin Co., Ltd.), and thus, a release agent particle dispersion (solid content of 20% by weight) in which release agent particles having a volume average particle diameter of 200 nm are dispersed is obtained.
Preparation of Masterbatch
150 parts of the amorphous polyester resin (P1), 80 parts of a cyan pigment (pigment 15:3, manufactured by Dainichiseika Color & Chemicals Mfg. Co., Ltd.), and 20 parts of ion exchange water are mixed with each other using a HENSCHEL MIXER. The obtained mixture is pulverized to thereby prepare a masterbatch.
Preparation of Oil Phase (A)/Water Phase
107 parts of the amorphous polyester resin (P1), 75 parts of the release agent particle dispersion, 18 parts of the masterbatch, and 73 parts of ethyl acetate are put together, and the resultant is stirred with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.), and dissolved and dispersed, thereby obtaining an oil phase (A). 990 parts of ion exchange water, 100 parts of an anionic surfactant, and 100 parts of ethyl acetate are mixed and stirred in another flask and thus, a water phase is obtained.
Emulsification Dispersion
500 parts of a solution (solid content concentration of 4%) obtained by dissolving the crystalline polyester resin (P1) in ethyl acetate and 3 parts of isophoronediamine are added to 300 parts of the oil phase (A), stirred with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.), dissolved and dispersed at 50° C., and thus, an oil phase (B) is obtained. Next, 400 parts of the water phase is put in another container and stirred at 50° C. with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.) 50 parts of the oil phase (B) is added to the water phase and stirred with a homogenizer (ULTRA TURRAX T50 manufactured by IKA Works, Inc.) at 50° C. for 5 minutes, and an emulsified slurry is obtained. By performing desolvation of the emulsified slurry at 50° C. for 15 hours, a toner slurry is obtained. The toner slurry is filtered under the reduced pressure and subjected to a cleaning treatment, thereby obtaining toner particles.
Then, after the cleaning, a dispersion obtained by adding 50 parts of the toner particles and 500 parts of ion exchange water is stirred in a 5-liter flask equipped with a stirrer, a nitrogen gas introducing tube, a temperature sensor, and a rectifying column and is heated to 85° C. After heating, the dispersion is stirred for 24 hours while keeping the heating temperature. Accordingly, the toner particles are heated at 85° C. for 24 hours. Then, liquid nitrogen is introduced into the dispersion such that the toner particles are cooled to room temperature (25° C.) at 20° C./min (rapidly cooled). The toner particles are heated again to 45° C., the annealing process is performed for 5 hours, and cooling is performed to 20° C. at a rate of 20° C./min.
Drying and Sieving
By drying and sieving the obtained toner particles, toner particles having a volume average particle diameter of 7 μm are prepared.
The toner particles (P1) are obtained through the processes described above.
Preparation of Toner Particles (C1)
Toner particles (C1) are obtained in the same manner as in the preparation of the toner particles (A1), except that the temperature is 45° C. and the keeping time is 2.5 hours in the conditions of the annealing process.
Preparation of Toner Particles (C2)
Toner particles (C2) are obtained in the same manner as in the preparation of the toner particles (A1), except that the temperature is 45° C. and the keeping time is 7.5 hours in the conditions of the annealing process.
100 parts of each of the obtained toner particles and 0.7 parts of dimethyl silicone oil-treated silica particles (RY200 manufactured by Nippon Aerosil Co., Ltd.) are mixed with each other in a HENSCHEL MIXER to obtain a toner of each example.
8 parts of each of the obtained toners and 100 parts of a carrier described below are mixed with each other to obtain a developer of each example (cyan developer).
A magenta developer is also prepared in the same manner as in the preparation of the cyan developer, except for changing the type of pigment.
Preparation of Carrier
The above components other than the ferrite particles are dispersed in a sand mill to prepare a dispersion, the dispersion and the ferrite particles are put into a vacuum degassing type kneader, and dried while stirring under reduced pressure, and thus, a carrier is obtained.
Measurement
With respect to the toner of the developer of each example, an endothermic amount S1 (J/g) derived from the crystalline resin of the toner particles before being heated, in a first heating process, which is measured by differential scanning calorimeter (DSC) [in the table, shown as “endothermic amount S1 derived from the crystalline resin before being heated” ], and an endothermic amount Sh (J/g) derived from the crystalline resin of the toner particles after being heated, in the first heating process, which is measured by differential scanning calorimeter (DSC)) [in the table, shown as “endothermic amount Sh derived from the crystalline resin after being heated” ] are obtained by the method described above.
The results thereof are shown in Table 1.
Evaluation
The following evaluation is performed using the obtained developer.
Evaluation of Color Irregularity in High Temperature and High Humidity Environment
The following operation and image forming are performed in the environment of a temperature of 30° C. and humidity of 80%.
ApeosPort IV C4470 manufactured by Fuji Xerox Co., Ltd. is prepared as an image forming apparatus which forms images for evaluation, the developer is put in the developing device, and supply toner (toner which is the same as the toner contained in the developer) is put in a toner cartridge. Then, solid images having a size of 5 cm×5 cm and an image area ratio of a cyan color of 100% are formed and continuously printed on 100 sheets of pure paper (P PAPER manufactured by Fuji Xerox Co., Ltd., product name P, basis weight 64 g/m2, paper thickness: 88 m, kept in the environment of a temperature of 30° C. and a humidity of 80% for a week). An L* value, a* value, and b* value of an image are randomly measured regarding 30 points of the 100-th image using a reflection spectral densitometer (XRite-939 manufactured by Xrite Inc.). A color difference ΔE value of two points at which measured values are most separated from each other among the measured values is obtained and set as an index of color irregularity. The color difference ΔE is calculated by the following expression.
ΔE=((L*1−L*2)2+(a*1−a*2)2+(b*1−b*2)2)0.5
When the ΔE value is equal to or smaller than 2, it is in an acceptable range, and the ΔE value is more preferably equal to or smaller than 1.
Evaluation of Color Irregularity in Low Temperature and Low Humidity Environment
The following operation and image forming are performed in the environment of a temperature of 10° C. and humidity of 20%.
ApeosPort IV C4470 manufactured by Fuji Xerox Co., Ltd. is prepared as an image forming apparatus which forms images for evaluation, the developer is put in a developing device, and supply toner (toner which is the same as the toner contained in the developer) is put in a toner cartridge. Then, secondary color images having a size of 5 cm×5 cm and an image area ratio of a cyan toner of 100% and an image area ratio of a magenta toner of 100% are formed and continuously printed on 100 sheets of coated paper (OS coated paper W, manufactured by Fuji Xerox Co., Ltd., bases weight 127 g/m2). An L* value, a* value, and b* value of an image (an L* value, an a* value, and a b* value in the CIE 1976 L*a*b* color system) are randomly measured regarding 30 points of the 100-th image using a reflection spectral densitometer (Xrite-939 manufactured by X-Rite Inc.). A color difference ΔE of two points at which measured values are most separated from each other among the measured values is obtained and set as an index of color irregularity. The color difference ΔE is calculated by the following expression.
ΔE=((L*1−L*2)2+(a*1−a*2)2+(b*1−b*2)2)0.5
When the ΔE value is equal to or smaller than 2, it is in an acceptable range, and the ΔE value is more preferably equal to or smaller than 1.
From the results described above, it is found that, in Examples, generation of color irregularity is prevented, even when an image is formed in the high temperature and high humidity environment and the low temperature and low humidity environment, compared to a case of Comparative Examples.
The foregoing description of the exemplary embodiments of the present invention has been provided for the purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise forms disclosed. Obviously, many modifications and variations will be apparent to practitioners skilled in the art. The embodiments were chosen and described in order to best explain the principles of the invention and its practical applications, thereby enabling others skilled in the art to understand the invention for various embodiments and with the various modifications as are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the following claims and their equivalents.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2016-166100 | Aug 2016 | JP | national |
| Number | Name | Date | Kind |
|---|---|---|---|
| 20150177630 | Umeda | Jun 2015 | A1 |
| Number | Date | Country |
|---|---|---|
| 2007-072333 | Mar 2007 | JP |
| 2010-152102 | Jul 2010 | JP |
| 2014-164064 | Sep 2014 | JP |
| Entry |
|---|
| Translation of JP 2010-152102 published Jul. 2010. |
| Number | Date | Country | |
|---|---|---|---|
| 20180059560 A1 | Mar 2018 | US |
