Patent Application
20110081611
The present U.S. patent application claims a priority under the Paris Convention of Japanese patent application No. 2009-230103 filed on Oct. 2, 2009, which shall be a basis of correction of an incorrect translation.
1. Field of the Invention
The present invention relates to a toner manufacturing method.
2. Description of the Related Art
Energy saving is given as a problem of a printer or the like adopting an electrophotographic printing system, and a demand for a toner capable of being fixed at a low temperature, i.e., a toner having the so-called low temperature fixing performance, has increased.
In order to enable low temperature fixation, it has heretofore been known, as one of an effective method, to use a binding resin having a higher sharp melt performance as a toner. A polyester resin is superior as a binding resin having such a characteristic.
When a polyester resin is used as a binding resin for a toner, it is general to give an elastic modulus at a high temperature by advancing cross-linkage by using a cross-linker. Thereby hot offsets in fixation are prevented to control the toner not to have an excessive luster.
It is general to use a polycarboxylic acid of being trivalent or more as a cross-linker of the polyester resin (see, for example, Japanese Patent Application Laid-Open Publication No. H5-289401). Besides, a case of using hexamethylene tetramine or a polyvalent metal compound was disclosed (see, for example, Japanese Patent Application Laid-Open Publication No. H5-027478), but both of the disclosed materials have the problems of strong hydrophilicity at a cross-linkage point and the excessive humidity dependency of charging.
On the other hand, a technique of a hybrid resin aiming to have a heat characteristic close to that of a cross-linked resin was disclosed, which hybrid resin was produced by adding a radically polymerizable monomer, such as styrene, and a radical polymerization initiator to a polyester resin having a double bond, such as a fumaric acid unit, to make the polyester resin react with a part of a styrene resin.
For example, Japanese Patent Application Laid-Open Publication No. H7-120976 disclosed the technique of dropping a monomer of a vinyl resin and a polymerization initiator for one hour through a dropping funnel while warming and agitating a monomer, including a fumaric acid, for a polyester in a reactor up to 135° C. to advance a radical polymerization reaction during this period, and, after that, heating the monomer to 230° C. to complete the polyester condensation reaction.
Furthermore, Japanese Patent Application Laid-Open Publication No. 2000-56511 disclosed the technique of manufacturing a polyester resin of a low degree of cross-linkage by causing a condensation polymerization reaction while heating a polyester monomer to 210° C., successively adding xylene, a polyester resin, and a styrene monomer to the polyester monomer, and, after that, dropping t-butyl hydroperoxide, which is a radical polymerization initiator. The technique holds the polyester resin for another 10 hours at that temperature and, after that, completes the radical polymerization reaction to manufacture the hybrid resin.
However, the efficiency of the reaction of a double bond in a polyester resin and a radically polymerizable monomer, such as styrene, as described above, is low, and it is required to use a conventional polyester cross-linker in conjunction with the polyester resin practically in order to obtain an aimed elastic modulus characteristic, which fact remains as a problem.
The present invention was made in view of the aforesaid situation, and aims to provide a toner manufacturing method capable of advancing the hybridization of a polyester resin and a radically polymerizable monomer efficiently in a short time, securing a sufficient elastic modulus at a high temperature without using any conventional cross-linkers for polyesters, settling the problems of offsets and excessive luster, and obtaining a toner causing no toner exfoliation at a folded part, namely, having no fixation strength poverty.
To achieve at least one of the abovementioned objects, a toner manufacturing method reflecting one aspect of the present invention comprises:
dispersing a polyester resin prepared by condensing a polyol and an unsaturated polycarboxylic acid into an aqueous medium and preparing a polyester resin particle dispersion liquid;
adding a vinyl polymerizable monomer and a radical polymerization initiator to the polyester resin particle dispersion liquid to cause a radical polymerization reaction, followed by preparing a dispersion liquid of resin particles made of a resin in which vinyl polymerizable monomers react with the polyester resin; and
mixing at least the resin particles made of the resin in which the vinyl polymerizable monomers react with the polyester resin, and a dispersion liquid of coloring agent particles, and forming toner particles by making the resin particles and the coloring agent particles cohere.
The present invention will become more fully understood from the detailed description given hereinbelow and the appended drawings, and thus are not intended as a definition of the limits of the present invention, wherein;
In the following, a toner manufacturing method according to the present invention will be described.
The toner manufacturing method according to the present invention comprises:
dispersing a polyester resin prepared by condensing a polyol and an unsaturated polycarboxylic acid into an aqueous medium and preparing a polyester resin particle dispersion liquid;
adding a vinyl polymerizable monomer and a radical polymerization initiator to the polyester resin particle dispersion liquid to cause a radical polymerization reaction, followed by preparing a dispersion liquid of resin particles made of a resin in which vinyl polymerizable monomers react with the polyester resin; and
mixing at least the resin particles made of the resin in which the vinyl polymerizable monomers react with the polyester resin, and a dispersion liquid of coloring agent particles, and forming toner particles by making the resin particles and the coloring agent particles cohere.
A mold parting agent, an externally added agent, and the like are used, as the occasion demands, besides a binding resin and a coloring agent, for manufacturing a toner.
As the binding resins, polyester resins in each of which a vinyl polymerizable monomer reacts are used. The polyester resins to be used for the manufacturing method of the present invention are ones having noncrystalline among the ones obtained by polymerization reactions of publicly known bivalent or more alcohol components and publicly known bivalent or more unsaturated carboxylic acid components.
As the alcohol components, for example, a trivalent or more polyol, such as glycerin, pentaerythritol, trimethylolpropane, and sorbitol, are given besides aliphatic diols, such as 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,7-Heptanediol, 1,8-octanediol, neopentyl glycol, and 1,4-butenediol, and aromatic diols, such as an alkylene oxide adduct of bisphenol A. Two kinds or more of these alcohol components may be combined with each other to be used.
As the unsaturated polycarboxylic acid components, a fumaric acid, a maleic acid, and an itaconic acid are preferably used for obtaining hybridization.
As the polycarboxylic acid components that may be used in conjunction with the unsaturated polycarboxylic acid components, a carboxylic acid, a carboxylic acid anhydride, a carboxylic acid ester, and the like are used, and a benzenedicarboxylic acid and a saturated carboxylic acid are preferably used as the carboxylic acid components. For example, saturated aliphatic dicarboxylic acids, such as an oxalic acid, a malonic acid, a succinic acid, an adipic acid, a sebacic acid, an azelaic acid, and an n-dodecyl succinic acid; alicyclic dicarboxylic acids, such as a cyclohexanedicarboxylic acid; and aromatic dicarboxylic acids, such as a phthalic acid, an isophthalic acid, and a terephthalic acid may be used individually, or may be used in combination with other one or more of them.
Furthermore, hybridization may be accelerated by using an unsaturated hydroxy carboxylic acid monomer, such as a caffeic acid, as a monomer for polyesters.
A polyester resin can be manufactured by, for example, performing the condensation polymerization of one of the alcohol components mentioned above and one of the unsaturated polycarboxylic acid components mentioned above in an inert gas atmosphere at a temperature within a range of from 120° C. to 250° C. At the time of performing the condensation polymerization, a publicly known esterification catalyst may be used as the occasion demands.
In the present invention, the aforesaid unsaturated polyester resin and a radical polymerizable monomer are subjected to a radical polymerization reaction.
<Polymerizable Monomers>
As the polymerizable monomers, for example, methacrylic acid ester derivatives, such as styrene, methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, isopropyl methacrylate, isobutyl methacrylate, t-butyl methacrylate, n-octyl methacrylate, 2-ethylhexyl methacrylate, stearyl methacrylate, lauryl methacrylate, phenyl methacrylate, diethylaminoethyl methacrylate, and dimethylaminoethyl methacrylate; acrylic ester derivatives, such as methyl acrylate, ethyl acrylate, isopropyl acrylate, n-butyl acrylate, t-butyl acrylate, isobutyl acrylate, n-octyl acrylate, 2-ethylhexyl acrylate, stearyl acrylate, lauryl acrylate, and phenyl acrylate; monomers of an olefine group, such as ethylene, propylene, and isobutylene; vinyl monomers, such as acrylic acid or methacrylic acid derivatives, such as acrylonitrile, methacrylonitrile, and acrylamide are given. One of these vinyl monomers can independently be used, or two or more kinds of these vinyl monomers can be combined with one another to be used.
Among the monomers mentioned above, as the polymerizable monomers, styrene, butyl acrylate, 2-ethylhexyl acrylate, methyl methacrylate, methacrylic acids, and acrylic acids are preferably used. Styrene, butyl acrylate, 2-ethylhexyl acrylate are hydrophobic monomers, and the combinations of them bring about advantages of making it easy to adjust an electrification characteristic and the glass transition point of a toner. Furthermore, as hydrophilic monomers, the methacrylic acids and the acrylic acids severally have an advantage of making it easy to control the cohesion diameters (the sizes of cohered particles) of the resin particles by improving the dispersion stability of a dispersion liquid of the resin particles including a polyester resin.
Each of the polymerizable monomers including the acrylic acids or the methacrylic acids has an electrically-charged dissociative functional group, such as a carboxyl group. It can be considered that, by making the polyester resin be subjected to the radical polymerization with such polymerizable monomers, the aforesaid dissociative functional groups are oriented on the surfaces of polyester resin particles, and repulsive charges are produced among the polyester resin particles to improve the dispersion stability of the particles. By the improvement of the dispersion stability, the agglomeration speed of the polyester resin particles becomes gentle, and it becomes easy to control the particle diameters and the shapes of cohering particles. As a result, even if the polyester resin is used for low temperature fixation, it is possible to make the particle size distribution a toner sharp and to form the shapes of the particles to be spheres. Thus, the defect of a transferred toner can be prevented.
As the coloring agents, publicly known coloring agents, such as a carbon black, a magnetic substance, a dye, and a pigment, can arbitrarily be used.
As black coloring agents, magnetic powders of magnetite, ferrite, and the like can be used besides carbon blacks, such as a furnace black and a channel black.
As the coloring agents of the other colors, pigments, such as C.I. pigment red 5, 48:1 of the same, 53:1 of the same, 57:1 of the same, 81:4 of the same, 122 of the same, 139 of the same, 144 of the same, 149 of the same, 166 of the same, 177 of the same, 178 of the same, 222 of the same, C.I. pigment yellow 14, 17 of the same, 74 of the same, 93 of the same, 94 of the same, 138 of the same, 155 of the same, 180 of the same, 185 of the same, C.I. pigment orange 31, 43 of the same, C.I. pigment blue 15:3, 60 of the same, and 76 of the same can be given. Furthermore, dyes, such as C.I. solvent red 1, 49 of the same, 52 of the same, 58 of the same, 68 of the same, 11 of the same, 122 of the same, C.I. solvent yellow 19, 44 of the same, 77 of the same, 79 of the same, 81 of the same, 82 of the same, 93 of the same, 98 of the same, 103 of the same, 104 of the same, 112 of the same, 162 of the same, C.I. solvent blue 25, 36 of the same, 69 of the same, 70 of the same, 93 of the same, and 95 of the same can be given. Furthermore, these pigments and dyes may be mixed with one another. As the mixtures, metal salts of acids, benzilic acid metallic complexes, or the like can be given.
As the externally added agents, a publicly known hydrophobic silica and a hydrophobic metal oxide can be given, and it is preferable from the point of view of a filming resistance property to add cerium oxide particles, titanate particles, a fatty acid having a carbon number within a range from 20 to 50, or higher alcohol particles to use the latter materials in conjunction with the former materials. In case of adding the cerium oxide particles or the titanate particles, it is preferable to use the particles of a number average particle diameter within a range of from 150 nm to 800 nm from the point of view of enhancing the filming resistance property.
In the following, concrete examples of the manufacturing method of the present invention are given.
(1) Process of Dispersing a Polyester Resin Produced by Condensing a Polyol and an Unsaturated Polycarboxylic Acid to Prepare the Polyester Resin Particle Dispersion Liquid
After dissolving a polyester resin into a solvent, such as ethyl acetate, and performing the emulsification dispersion of the polyester resin into an aqueous medium with a disperser, desolvation processing may be performed. Alternatively, the polyester resin may be dispersed at a temperature of 120° C. or more without using any solvents. Alternatively, as disclosed in Japanese Patent Application Laid-Open Publication No. 2006-337995, a polyester resin dispersion liquid may be produced by condensing droplets of a polyol and an unsaturated polycarboxylic acid after the droplets have been formed in an aqueous medium together with a strong acid, such as a dodecyl benzenesulfonic acid.
(2) Process of Preparing the Dispersion Liquid of Resin Particles Made of a Resin Produced by Adding a Vinyl Polymerizable Monomer and a Radical Polymerization Initiator to the Polyester Resin Particle Dispersion Liquid, and after that, by Performing the Radical Polymerization of the Vinyl Polymerizable Monomer to React with the Polyester Resin
A radical polymerizable monomer and a polymerization initiator are added to the polyester resin particle dispersion liquid of the aforesaid item (1), and a dispersion liquid of resin particles made of a resin produced by the reaction of a vinyl polymerizable monomer with the polyester resin is prepared. At this time, a chain transfer agent may be added in order to adjust the molecular weight of the polymer. The polymerizable monomer is preferably added to be 5% to 95% of the polyester resin by a mass ratio, and especially preferably added to be 10% to 50% . Furthermore, each of the resin particles in the dispersion liquid prepared by this process preferably has a volumetric basis median diameter to be within a range of from 50 nm to 300 nm.
As the polymerization initiators, any water soluble polymerization initiator can suitably be used. For example, water soluble radical polymerization initiators, such as persulfates of potassium persulfate, ammonium persulfate, and the like, are preferably used in order to obtain the effects of the present invention.
As the chain transfer agents, generally used chain transfer agents can be used. For example, 2-chloroethanol; mercaptans, such as octyl mercaptan, dodecyl mercaptan, and t-dodecyl mercaptan; a styrene dimer, and the like are given.
(3) Process of Obtaining a Dispersion Liquid of Coloring Agent Particles Obtained by Dispersing a Coloring Agent into an Aqueous Medium
Oil droplet dispersion is performed by means of mechanical energy, and the disperser thereof is not particularly limited. Clearmix (manufactured by M Technique Co, Ltd.), which is an agitator equipped with a rotor capable of high speed rotation, an ultrasonic disperser, a mechanical homogenizer, Cavitron, Manton Golin, pressure type homogenizer, and the like can be used.
Each of the coloring agent particles in a dispersion liquid prepared in this process preferably has a volumetric basis median diameter within a range of from 10 nm to 300 nm, and more preferably within a range of from 100 nm to 200 nm, and furthermore preferably within a range of from 100 nm to 150 nm. For example, by adjusting the magnitude of the aforesaid mechanical energy, the volumetric basis median diameter can be controlled within the aforesaid ranges.
(4) Process of Performing the Cohesion and the Fusion of Resin Particles and the Coloring Agent Particles to Form Toner Particles by Adding a Coagulant to an Aqueous Medium in Which the Dispersion Liquid of the Resin Particles of the Resin Prepared by the Reactions of the Vinyl Polymerizable Monomers with the Polyester Resin and the Dispersion Liquid of the Coloring Agent Particles are Mixed, and by Adjusting the Temperature of the Aqueous Medium
As the coagulants, for example, alkali metal salts and alkaline earth metal salts are given. As the alkaline metals of these salts, lithium, potassium, sodium, and the like are given. Furthermore, as the alkaline earth metals of these salts, magnesium, calcium, strontium, barium, and the like are given. Among them, potassium, sodium, magnesium, calcium, and barium are particularly preferable. As the counterions (anions constituting the salts) of the alkaline metals or the alkaline earth metals, chloride ions, bromide ions, iodide ions, carbonate ions, sulfate ion, and the like are given.
In case of adding a mold parting agent, it is only necessary to add the dispersion liquid (wax emulsion) of the mold parting agent particles into the aforesaid aqueous medium in this process, and to perform the salting-out and the cohesion of the resin particles, the coloring agent particles, and the mold parting agent particles. Alternatively, it may be performed to add the dispersion liquid of the mold parting agent particles to prepare a dispersion liquid of the resin particles and the mold parting agent particles in advance in the process of the item (2), and then to perform the cohesion at the process of the item (4).
(5) Process of Filtering out Toner Particles from the Aqueous Medium and Removing Undesired Substances, such as a Surface Active Agent from the Toner Particles by Washing Processing
(6) Process of Performing the Drying Processing of the Toner Particles Subjected to the Washing Processing
(7) Process of Adding an Externally Added Agent to the Toner Particles Subjected to the Drying Processing
In the following, concrete examples of the present invention will be described, but the present invention is not limited to those examples.
1. Making Noncrystalline Polyester Resins (A-1) to (A-5)
The polycarboxylic acid monomer and the polyol component were stocked in a reaction container equipped with an agitator, a nitrogen introducing pipe, a temperature sensor, and a rectifying column, and one hour was spent to raise the temperatures of the polycarboxylic acid monomer and the polyol component to 190° C. After ascertaining that the inside of the reaction system was agitated to be uniform, a catalyst Ti(OBu)4 was projected (0.003 percents by mass of the whole polycarboxylic acid monomer).
Furthermore, it was needed for six hours to raise the temperature to 240° C. from the aforesaid temperature while distilling away produced water, and the dehydration condensation reaction was continued for further six hours at 240° C. to perform polymerization. Thereby, a noncrystalline polyester resin (A-1) was obtained. By the measurement of the molecular weight of the resin of the obtained noncrystalline polyester resin (A-1) with a gel permeation chromatography (GPC) (HLC-8 120 GPC manufactured by Tosoh Corporation), it was found that the number average molecular weight was 3100 (converted by the styrene reference material). Furthermore, as the result of the measurement of the heat characteristic of the obtained resin with a differential scanning calorimeter (DSC) (Diamond DSC manufactured by PerkinElmer, Inc.) (the speed of temperature rise: 10° C./min), it was found that the glass transition temperature (Tg) thereof was 63° C.
A noncrystalline polyester resin (A-2) was made by a similar method to that of the noncrystalline polyester resin (A-1) except that the part of the polycarboxylic acid monomer was changed to the followings. The number average molecular weight was 2900, and the Tg was 66° C.
A noncrystalline polyester resin (A-3) was made by a similar method to that of the noncrystalline polyester resin (A-1) except that the part of the polycarboxylic acid monomer was changed to the followings. The number average molecular weight was 3200, and the Tg was 65° C.
A noncrystalline polyester resin (A-4) was made by a similar method to that of the noncrystalline polyester resin (A-1) except that the part of the polycarboxylic acid monomer was changed to the followings. The number average molecular weight was 3500, and the Tg was 61° C.
A noncrystalline polyester resin (A-5) was made by a similar method to that of the noncrystalline polyester resin (A-1) except that the part of the polycarboxylic acid monomer was changed to the followings. The number average molecular weight was 4400, and the Tg was 58° C.
The obtained noncrystalline polyester resin (A-1) was transferred to Cavitron CD1010 (manufactured by Eurotec, Ltd.) at a speed of 100 parts by mass per minute in its molten state. Dilute aqueous ammonia of the concentration of 0.37 percents by mass prepared by diluting regent aqueous ammonia with an ion-exchange water was put into a separately prepared aqueous medium tank, and the dilute aqueous ammonia was transferred to Cavitron CD100 (manufactured by Eurotec, Ltd.) at the speed of 0.1 liter per minute while being heated to 160° C. with a heat exchanger at the same time as the transfer of the noncrystalline polyester resin (A-1) in its molten state. Cavitron CD1010 was driven under the conditions that the rotation speed of the rotor thereof was 60 Hz and the pressure thereof was 5 kg/cm2, and the noncrystalline polyester resin (A-1) dispersion liquid having a volumetric basis median diameter of 223 nm and 30 parts by mass of solid content quantity was obtained.
As for also the noncrystalline polyester resin (A-2), a noncrystalline polyester resin (A-2) dispersion liquid was obtained by a similar method to that of the <Preparation of a Dispersion Liquid of the Noncrystalline Polyester Resin (A-1)>. The volumetric basis median diameter thereof was 237 nm.
As for also the noncrystalline polyester resin (A-3), a noncrystalline polyester resin (A-3) dispersion liquid was obtained by a similar method to that of the <Preparation of a Dispersion Liquid of the Noncrystalline Polyester Resin (A-1)>. The volumetric basis median diameter thereof was 230 nm.
As for also the noncrystalline polyester resin (A-4), a noncrystalline polyester resin (A-4) dispersion liquid was obtained by a similar method to that of the <Preparation of a Dispersion Liquid of the Noncrystalline Polyester Resin (A-1)>. The volumetric basis median diameter thereof was 210 nm.
<Preparation of a Dispersion Liquid of the Noncrystalline Polyester Resin (A-5)>
As for also the noncrystalline polyester resin (A-5), a noncrystalline polyester resin (A-5) dispersion liquid was obtained by a similar method to that of the <Preparation of a Dispersion Liquid of the Noncrystalline Polyester Resin (A-1)>. The volumetric basis median diameter thereof was 200 nm.
A solution containing the mixed aforesaid components was heated to 95° C., and the solution was sufficiently dispersed with ULTRA-TURRAX T50 manufactured by IKA Company. After that, the dispersed solution was subjected to dispersion processing with a pressure discharging type Golin homogenizer to obtain the mold parting agent dispersion liquid 1 having a volume mean diameter of 240 nm and a solid content quantity of 20 percents by mass.
A polymerization initiator solution obtained by dissolving 10.3 parts by mass of potassium persulfate into 210 parts by mass of ion-exchange water was added to 1450 parts by weight of “noncrystalline polyester resin (A-1) dispersion liquid,” obtained by the aforesaid method, 650 parts by weight of “mold parting agent dispersion liquid 1,” and 1250 parts by weight of ion-exchange water, and a monomer mixture liquid containing the following compounds was dropped for two hours under the temperature condition of 80° C.
After the completion of the dropping, polymerization was performed by agitating the liquid while heating it for two hours. After the completion of the polymerization, the liquid was cooled to 28° C. to make a “resin particle dispersion liquid 1.” The weight-average molecular weight of the “resin particle dispersion liquid 1” was 19500.
The resin particle dispersion liquids 2 and 3 were made by similar methods to that of the resin particle dispersion liquid 1 except that the “noncrystalline polyester resin (A-1) dispersion liquid” in the preparation of the resin particle dispersion liquid 1 was changed to the “noncrystalline polyester resin (A-2) dispersion liquid” and the “noncrystalline polyester resin (A-3) dispersion liquid,” respectively. The molecular weights of the resin particle dispersion liquids 2 and 3 were 19000 and 19200, respectively.
The resin particle dispersion liquids 4 and 5 were made by similar methods to that of the resin particle dispersion liquid 1 except that the “noncrystalline polyester resin (A-1) dispersion liquid” in the preparation of the resin particle dispersion liquid 1 was changed to the “noncrystalline polyester resin (A-4) dispersion liquid” and the “noncrystalline polyester resin (A-5) dispersion liquid,” respectively. The molecular weights of the resin particle dispersion liquids 4 and 5 were 16400 and 17600, respectively.
11.5 parts by mass of n-sodium dodecyl sulfate was agitated and dissolved into 160 parts by mass of ion-exchange water, and 25 parts by mass of C.I. pigment blue 15:3 was gradually added thereto. Next, the C.I. pigment blue 15:3 was dispersed with “Clearmix W-Motion CLM-0.8” (manufactured by M Technique Co., Ltd.) to obtain the coloring agent fine particle dispersion liquid 1 containing coloring agent fine particles 1 having a volumetric basis median diameter of 158 nm.
In addition, the volumetric basis median diameter was measured under the following measurement conditions with “MICROTRAC UPA 150” (manufactured by Honeywell International Inc.).
Next, an aqueous solution in which 54.3 parts by mass of magnesium chloride.6 hydrate was dissolved in 54.3 parts by mass of an ion-exchange water was added, and after that, the temperature in the system was raised to 60° C. to start the agglutination reactions of the resin particles and the coloring agent particles.
After the start of the agglutination reactions, sampling was periodically performed, and the volumetric basis median diameter (D50) of the sample particles was measured with a particle size distribution measuring device “Coulter Multisizer 3” (manufactured by Beckman Coulter, Inc.). When the measured median diameter became 5.8 μm, an aqueous solution in which 2 parts by mass of magnesium chloride.6 hydrate was dissolved in 2 parts by mass of ion-exchange water was added for 10 minutes. Agitation was continued until the volumetric basis median diameter (D50) of the particles became 6 μm.
The agitation was further continued for one hour with the temperature kept at 60° C., and then 20.1 parts by mass of iminocarboxylic acid compound (9-2) was added.
When the degrees of circularity of toner particles were measured with a flow type particle image analyzing device “FPIA-2100” (manufactured by Sysmex Corporation), it was found that the degree of circularity of the toner particles at this time point was 0.951. The agitation was continued for four hours with the temperature kept at 65° C., and the toner particle dispersion liquid was cooled to 30° C. under the condition of 6° C. per minute when the degree of circularity of the toner particles reached 0.976 to complete the reactions.
Next, the solid-liquid separation of the produced toner particle dispersion liquid was performed with a basket type centrifugal separator “MARK III type” (model number 60×40) (manufactured by Matsumoto Kikai MFG. Co. , Ltd.) to form a wet cake of the toner. After that, the washing and the solid-liquid separation of the toner were repeated until the value of the electric conductivity of the filtrate became 15 μS/cm or less.
Next, the wet cake was moved to an airflow type dryer “Flash Jet Dryer” (manufactured by Seishin Enterprise Co., Ltd.), and the drying processing of the wet cake was performed until the water quantity thereof became 0.5 percents by mass. In addition, the drying processing was performed by blowing an airflow of 40° C. and 20% RH against the water cake. The dried toner was slowly cooled to 24° C., and 1.0 part by mass of hydrophobic silica was mixed to 100 parts by mass of toner with a Henschel mixer. After setting the peripheral speed of the rotor blade to 24 m/s and mixing the mixture for 20 minutes, the mixture was made to pass through a sieve of 400 meshes. The thus obtained toner is referred to the “toner 1.”
As described in Table 1 which is shown in
Ferrite carriers coated by a silicone resin and having a volume average diameter of 60 nm were mixed to each of the made toners 1-5 to prepare the developing agent of each of the toners 1-5. The developing agent was mixed to each toner so that the concentration of the toner in each developing agent became 6 percents by mass.
The developing agent of each of the toners 1-5 was mounted on a commercially available multifunction peripheral (manufactured by Konica Minolta Business Technologies, Inc.). Then, evaluation tests of the following respective items were performed, and the results are described in Table 2 shown in
As for fold fixing performances (strength), the fixation ratios of toner images at folds of sheets of paper at the time of setting the surface temperature of the heating roller to 170° C. were evaluated. To put it concretely, when a fixation image of a toner was bent toward the inner surface of the image, the degree of the exfoliation of the toner at the bent part was evaluated as a fixation ratio.
The measurement method was performed as follows: folding a solid image part (image concentration: 0.8) so that the image surface became inside, rubbing the folded part with a finger three times, then opening the image to wipe the image three times with “JK wiper (manufactured by Nippon Paper Crecia Co. , Ltd.)”, and calculating the value of the fixation ratio on the basis of the image concentrations at the folding position of the image before and after the folding in conformity with the following formula.
Fixation Ratio (%)=(image concentration after folding)/(image concentration before folding)×100
The fold fixation strength was evaluated from the obtained fixation ratios as follows, and the fold fixation strength of 80% or more was evaluated to be acceptant.
19 g of a carrier and 1 g of a toner were put in a container made of a glass and having a capacity of 20 ml, and the container was shaken for 20 minutes in the following two environments (low temperature and low humidity environment, and high temperature and high humidity environment) under the conditions of: the shaking frequency of 200 times per minute, the shaking angle of 45 degrees, the arm length of 50 cm. After that, the charge quantities were measured by a blowoff method.
The ranks of the toners 1-5 were evaluated on the basis of the differences between the charge quantities in the low temperature and low humidity environments and the charge quantities in the high temperature and high humidity environments.
After 100,000 sheets of continuous running of an image having a C/W ratio of 20% were performed in the L/L environment (10° C., 15% RH) and the H/H environment (30° C., 85% RH), the fogging on the white ground parts of the image and the fogging on a photosensitive body were visually observed. As the sheets of transfer paper, sheets of glossy paper, each having brightness of 92 and a thickness of 80 g/m2, were used. Good “⊙”: no falls of image concentration and no fogging were generated
The evaluation machine was remodeled to be able to change the temperature of its fixation roller by the 5° C., and hot offset generating temperatures were examined. Sheets of glossy paper, each having a thickness of 80 g/m2, were used. If no hot offsets were produced at 210° C., the toner was judged to be acceptant.
From the results described in Table 2 shown in
According to a preferred embodiment of the present invention, there is provided a toner manufacturing method, comprising:
dispersing a polyester resin prepared by condensing a polyol and an unsaturated polycarboxylic acid into an aqueous medium and preparing a polyester resin particle dispersion liquid;
adding a vinyl polymerizable monomer and a radical polymerization initiator to the polyester resin particle dispersion liquid to cause a radical polymerization reaction, followed by preparing a dispersion liquid of resin particles made of a resin in which vinyl polymerizable monomers react with the polyester resin; and
Preferably, the vinyl polymerizable monomer includes a (meta)acrylic acid.
Preferably, the unsaturated polycarboxylic acid is a fumaric acid.
Preferably, the unsaturated polycarboxylic acid is an itaconic acid.
Preferably, the radical polymerization initiator is a water soluble radical polymerization initiator.
Preferably, the water soluble radical polymerization initiator is potassium persulfate.
Preferably, a volumetric basis median diameter of the resin particles made of the resin in which the vinyl polymerizable monomers react with the polyester resin, is within a range of 50 to 300 nm.
Preferably, a volumetric basis median diameter of the coloring agent particles is within a range of 10 to 300 nm.
According to the present invention, hybridization efficiency advances in a short time. Even if no conventional cross-linkers for polyesters are used, it is possible to secure a sufficient elastic modulus at a high temperature, and to settle the problems of offsets and excessive luster. Furthermore, it is possible to obtain a toner causing no toner exfoliation at a folded part, namely, having no fixation strength poverty.
The mechanism of the present invention can be guessed as follows here.
The present invention is provided with a step of dispersing a polyester resin into an aqueous medium, and preparing the polyester resin particle dispersion liquid. In this step, the (specific) surface area of the polyester resin expands.
When a vinyl polymerizable monomer and a radical polymerization initiator are added to the polyester resin particle dispersion liquid, the vinyl polymerizable monomer and the radical polymerization initiator can comparatively freely move in the aqueous medium, and consequently the frequency (probability) of radical's attacks on the surface of the polyester resin particles rises. By the prior art, the frequency, probability, of the attacks of the radicals in a high viscous polyester resin and a polyester monomer in a reactor was limited from the point of view of the agitation mechanism thereof, and it was not able to cause hybridization as efficiently as that of the present invention.
Furthermore, because the efficiency of the hybridization rises, it becomes unnecessary to add any cross-linkers for accelerating hydration to the polyester resin itself. Consequently, the humidity dependency of charging reduces, and the variations of development and transfer characteristics caused by the variations of humidity are improved to stabilize images and image qualities.
Furthermore, it can be considered that the rise of the efficiency of hybridization causes a rise of the density of the branch points of molecular chains in the resin to accelerate the entanglements of the molecular chains, thereby, even if a toner image exists at a fold, the toner is not fractured to show a high fixation strength.
Although various exemplary embodiments have been shown and described, the invention is not limited to the embodiments shown. Therefore, the scope of the invention is intended to be limited solely by the scope of the claims that follow.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2009230103 | Oct 2009 | JP | national |
