Patent Application
20240117192
The present invention relates to a surface-treated gas-phase-process silica particle, a manufacturing method therefor, and a toner external additive for electrostatic charge image development used for developing an electrostatic charge image in an electrophotographing method, an electrostatic recording method, etc.
Dry developers used in an electrophotographing method, etc. can be classified into: a single-component developer using a toner itself in which a colorant is dispersed in a binder resin; and a two-component developer in which a carrier is mixed with the toner. When copying is performed by using these developers, the developer needs to have excellent flowability, caking resistance, fixability, charging property, cleanability, etc. in order to have process compatibility. In particular, to improve the flowability, the caking resistance, the fixability, and the cleanability, an inorganic fine particle is often used as a toner external additive.
However, dispersibility of the inorganic fine particle significantly affects the toner characteristics. Ununiform dispersibility may fail to yield desired characteristics of flowability, caking resistance, and fixability, or may cause insufficient cleanability and generate toner adhesion, etc. on a photoreceptor, which may be a cause of generation of a black-spot-like image defect. For a purpose of improving these points, various inorganic fine particles having a hydrophobized surface are proposed.
Among the inorganic fine particles used for such uses, gas-phase-process silica is known to have excellent functions as the toner external additive because of its small primary particle diameter and control of its charging property by a surface treatment (Patent Documents 1, 2, and 3).
However, although having the small primary particle diameter, the gas-phase-process silica easily aggregates, and a diameter of the aggregated particle may be typically from 10 μm to 200 μm or even larger. Such an aggregated particle is loosened with receiving strong frictional force to be dispersed in the toner in a dispersing step into the toner, but silica forming a large aggregate has poor dispersibility in the toner. Such aggregated particles present in the toner may degrade flowability or cause falling from the toner, which causes problems of generating a white spot in a printed image, etc.
From such a viewpoint, proposed is a method for crushing and classifying the aggregated particles generated after the hydrophobizing treatment and using only the fine particles thereof (Patent Document 4). However, this method is not favorable because the crushing and classifying as above have poor manufacturing efficiency and is costly.
The present invention has been made in view of the aforementioned circumstances. An object of the present invention is to provide: a surface-treated gas-phase-process silica particle that contains few coarsely aggregated particles and that can impart good flowability when added into a toner; a manufacturing method therefor; and an external additive for a toner containing the surface-treated gas-phase-process silica particle.
To solve the above problem, the present invention provides a method for manufacturing a surface-treated gas-phase-process silica particle, the method comprising steps of:
Such a method for manufacturing a surface-treated gas-phase-process silica particle can manufacture the surface-treated gas-phase-process silica particle that contains few coarsely aggregated particles and that can impart good flowability when added into a toner.
A BET specific surface area of the raw material gas-phase-process silica particle is preferably 40 to 400 m2/g.
Such a raw material gas-phase-process silica particle has excellent dispersibility and hardly aggregates during the surface treatment with the silazane compound.
In the step (A1), an amount (g) of the added 1,3-divinyl-1,1,3,3-tetramethyldisilazane is preferably an amount represented by
{an amount(g) of the raw material gas-phase-process silica particle used in the step(A1)×a BET specific surface area(m2/g) of the raw material gas-phase-process silica particle}/B(B represents a number of 5,000to100,000).
Such a range of the amount of added 1,3-divinyl-1,1,3,3-tetramethyldisilazane is preferable in terms of the cost, and can improve efficiency of the hydrophobizing treatment with hexamethyldisilazane in the step (A2).
In the step (A2), an amount (g) of the added hexamethyldisilazane is preferably an amount represented by
{an amount(g) of the preliminarily treated silica particle used in the step(A2)×a BET specific surface area(m2/g) of the raw material gas-phase-process silica particle}/C(C represents a number of 150to3,000),
Such a range of the amount of added hexamethyldisilazane can inhibit generation of aggregates during the reaction, and can further increase the hydrophobicity degree of the silica particle.
The present invention also provides a surface-treated gas-phase-process silica particle, comprising a gas-phase-process silica particle having a surface treated with 1,3-divinyl-1,1,3,3-tetramethyldisilazane and hexamethyldisilazane, wherein
The present invention can achieve the surface-treated gas-phase-process silica particle having such characteristics.
The present invention also provides a toner external additive for electrostatic charge image development comprising the above surface-treated gas-phase-process silica particle.
The inventive surface-treated gas-phase-process silica particle can impart good flowability and printing characteristics to a toner when used as the toner external additive.
As described above, the present invention can provide: a surface-treated gas-phase-process silica particle that can improve defects in a printed image and low toner flowability that are caused by using a conventional fumed silica with a small particle diameter as an external additive; a toner for electrostatic development using the same; and a toner external additive for electrostatic development using the same.
As noted above, there have been demands for the developments of an external additive for a toner containing a surface-treated gas-phase-process silica particle that contains few aggregated particles and that can impart good flowability when added into a toner.
The present inventors have made earnest study to achieve the above object, and consequently found that a surface-treated gas-phase-process silica particle that contains few aggregates, that has excellent dispersibility even when added into a toner, and that causes no defect in a printed image can be obtained by surface-treating a gas-phase-process silica particle with vinyltetramethyldisilazane and hexamethyldisilazane.
Specifically, the present invention is a method for manufacturing a surface-treated gas-phase-process silica particle, the method comprising steps of:
Hereinafter, the present invention will be described in detail, but the present invention is not limited thereto.
The gas-phase-process silica particle (gas-phase-process silica fine particle) used as a raw material in the present invention is also called “dry-method silica”, and is not particularly limited as long as it is manufactured by flame hydrolysis of a silicon compound, oxidation with a combustion-in-flame method, or a combination of these reactions. In particular, a gas-phase-process silica particle manufactured by a flame hydrolysis method is preferably used. Examples or commercially available products thereof include “AEROSIL”, manufactured by NIPPON AEROSIL CO., LTD. or Evonik Degussa GmnbH; “CAB-O-SIL”, manufactured by Cabot Corporation; “HDK”, manufactured by Wacker Asahikasei. Silicone Co., Ltd.; and “REOLOSIL”, manufactured by Tokuyama Corporation.
A method for manufacturing a gas-phase-process silica particle by the flame hydrolysis is a method of, for example, introducing a gas of a raw material silicon compound such as silicon tetrachloride together with an inert gas into a mixing chamber of a combustion burner, mixing the gasses with hydrogen and air to form a mixed gas at a predetermined ratio, burning this mixed gas in a reaction chamber at a temperature of 1,000 to 3,000° C. to generate silica, and after cooling, collecting the generated silica with a filter.
Examples of the silicon compound used as the raw material of the gas-phase-process silica particle include various inorganic silicon compounds and organic silicon compounds. Examples thereof include: inorganic silicon compounds, such as silicon tetrachloride, silicon trichloride, and silicon dichloride; and organic silicon compounds, such as siloxanes such as hexamethylcyclotrisiloxane, octamethylcyclotetrasiloxane, decamethylcyclopentasiloxane, hexamethyldisiloxane, and octamethyltrisiloxane, alkoxysilanes such as methyltrimethoxysilane, tetramethoxysilane, ethyltrimethoxysilane, n-propyltrimethoxysilane, methyltributoxysilane, diethyldipropoxysilane, and trimethylbutoxysilane, tetramethylsilane, diethylsilane, hexamethyldisilazane, and an oligomer and polymer thereof.
The hydrolysis and combustion decomposition of such silicon compounds in flame can be performed, after purifying this silicon compound by distillation etc. as necessary, by introducing the silicon compound into flame such as oxyhydrogen flame to be reacted in this flame by: a stream-entraining method in which the silica compound is heated and evaporated to entrain a stream of an inert gas such as nitrogen gas; or a method in which the silicon compound is atomized to be supplied into flame. In this case, a combustible gas such as hydrogen gas and methane gas may be used as an auxiliary combustion gas. This auxiliary combustion gas may be any as long as it yields no residue, and is not particularly limited. The silica generated by the hydrolysis or combustion decomposition of these silicon compounds is collected by a known method such as a bag filter and a cyclone.
The raw material gas-phase-process silica particle in the present invention preferably has a BET specific surface area of 40 to 400 m2/g. Such a range yields excellent dispersibility, and hardly causes aggregation during a surface treatment with a silazane compound, described below.
One kind of the raw material gas-phase-process silica particle may be used, or two or more kinds thereof may be used in mixture.
The inventive method for manufacturing a surface-treated gas-phase-process silica particle includes the following step (A1) and step (A2).
The step (A1) is a step of adding 1,3-divinyl-1,1,3,3-tetramethyldisilazane (hereinafter, described as “divinyltetramethyldisilazane”) to the raw material gas-phase-process silica particle and introducing the vinyldimethylsilyl group on the surface of the raw material gas-phase-process silica particle to obtain a preliminarily treated silica particle. This step allows the surface treatment in the following step (A2) to proceed more uniformly at high degree.
As the raw material gas-phase-process silica particle, the aforementioned gas-phase-process silica particle can be used.
For the surface treatment method for the raw material gas-phase-process silica particle with divinyltetramethyldisilazane in the step (A1), a dry method and a wet method, which are used for a surface treatment of a common powder, can be used. The dry method is preferably used in terms of productivity. As a method for adding divinyltetramethyldisilazane in the dry method, divinyltetramethyldisilazane can be dropped, sprayed with a spray, etc. with stirring the raw material gas-phase-process silica particle in a reaction container. Divinyltetramethyldisilazane may be used as it is, or may be diluted with a solvent such as toluene, xylene, and hexane to use.
When the raw material gas-phase-process silica particle is subjected to the surface treatment, water is preferably contained on the silica surface in advance because the efficiency of the surface treatment is improved in this manner. In this case, the silica is preferably stirred for approximately 0.5 hours to 2.0 hours after adding water.
Methods for adding water include a method of dropping or spraying water with stirring the raw material gas-phase-process silica particle in the reaction container, or alternatively, water may be added as steam.
An amount of the added water relative to the raw material gas-phase-process silica particle is preferably an amount calculated by the following formula.
The amount(g) of the added water={an amount(g) of the raw material gas-phase-process silica particle used in the step(A1)×a BET specific surface area(m2/g) of the raw material gas-phase-process silica particle}/A
In the calculation formula, A preferably represents a number of 300 to 200,000, and more preferably a number of 500 to 2,500. A of 300 or more is preferable because aggregation of the raw material gas-phase-process silica particle due to water can be inhibited. A of 200,000 or less is preferable because reactivity with the silazane compound can be more increased.
An amount of the added divinyltetramethyldisilazane relative to the raw material gas-phase-process silica particle is preferably an amount calculated by the following formula.
The amount(g) of the added divinyltetramethyldisilazane=fan amount(g) of the raw material gas-phase-process silica particle used in the step(A1)×a BET specific surface area(m2/g) of the raw material gas-phase-process silica particle)/B
In the calculation formula, B preferably represents a number of 5,000 to 100,000, and more preferably a number of 10,000 to 80,000. B of 5,000 or more is preferable in terms of the cost. B of 100,000 or less is preferable because efficiency of the hydrophobizing treatment with hexamethyldisilazane in the step (A2) can be increased.
For the reaction between the raw material gas-phase-process silica particle and divinyltetramethyldisilazane in the step (A1), common conditions for a surface treatment of silica with a silazane compound can be applied. Although the reaction also proceeds at room temperature, the mixture is preferably stirred at 50 to 70° C. for 0.5 hours to 3 hours to promote the reaction after divinyltetramethyldisilazane is added.
The step (A2) is a step of adding hexamethyldisilazane to the preliminarily treated silica particle obtained in the step (A1) and introducing the trimethylsilyl group on a surface of the preliminarily treated silica particle to obtain a hydrophobized surface-treated gas-phase-process silica particle.
For the surface treatment method for the preliminarily treated silica particle with hexamethyldisilazane in the step (A2), a dry method and a wet method, which are used for a surface treatment of a common powder, can be used. The dry method is preferably used in terms of productivity. As a method for adding hexamethyldisilazane in the dry method, hexamethyldisilazane can be dropped, sprayed with a spray, etc. with stirring the preliminarily treated silica particle in a reaction container. Hexamethyldisilazane may be used as it is, or may be diluted with a solvent such as toluene, xylene, hexane, etc. to use.
As in the step (A1), the silica surface preferably contains water in the step (A2) as well because in this manner, the efficiency of the surface treatment is increased. Although adding water in the step (A1) as above is sufficient, water may be additionally added in the step (A2).
An amount of the added hexamethyldisilazane relative to the preliminarily treated silica particle is preferably an amount calculated by the following formula.
The amount(g) of the added hexamethyldisilazane=(an amount(g) of the preliminarily treated silica particle used in the step(A2)×a BET specific surface area(m2/g) of the raw material gas-phase-process silica particle)/C
In the calculation formula, C preferably represents a number of 150 to 3,000, and more preferably a number of 200 to 1,000. C of 150 or more can inhibit generation of aggregates during the reaction. C of 3,000 or less can further increase the hydrophobicity degree of the silica particle.
For the reaction between the preliminarily treated silica particle and hexamethyldisilazane in the step (A2), common conditions for a surface treatment of silica with a silazane compound can be applied. Although the reaction also proceeds at room temperature, the mixture is preferably stirred at 50 to 100° C. for 0.5 hours to 3 hours to promote the reaction after hexamethyldisilazane is added.
In the inventive method for manufacturing a surface-treated gas-phase-process silica particle, the surface-treated gas-phase-process silica particle itself can be dried with air, allowed to be cooled, etc. after the step (A2), but the inventive method preferably further includes a step (A3): a step of drying the surface-treated gas-phase-process silica particle. The drying conditions are not particularly limited, but the silica particle is preferably dried at 140° C. to 250° C. for approximately 0.5 hours to 3 hours under a nitrogen flow.
The surface-treated gas-phase-process silica particle obtained by the inventive method for manufacturing a surface-treated gas-phase-process silica particle is a surface-treated gas-phase-process silica particle, containing a gas-phase-process silica particle having a surface treated with 1,3-divinyl-1,1,3,3-tetramethyldisilazane and hexamethyldisilazane, where
The combination of the above physical properties (1) to (4) imparts good flowability and printing characteristics to a toner when the silica particle is used as a toner external additive.
The BET specific surface area depends on a primary particle diameter, and specifically, is preferably 40 to 200 m2/g. If the BET specific surface area is less than 30 m2/g, the dispersibility in the toner is poor and the effect of improving the flowability is degraded when the silica particle is added into the toner as a toner external additive for electrostatic charge image development. If the BET specific surface area is 400 m2/g or more, the silica particles easily aggregate.
The particle size distribution on a volumetric basis by a laser diffraction method may be a particle size distribution of a 0.5 mass % dispersion of the surface-treated gas-phase-process silica particle in methanol (dispersed by ultrasonic irradiation with an output of 30 W/L for 10 minutes) on a volumetric basis by a laser diffraction method. A proportion of the particles with 1.5 μm or more of 10% or more, which means there are many large aggregated particles, causes poor dispersibility in the toner, and poor flowability of the toner and printed image quality when the silica particle is added into the toner as a toner external additive for electrostatic charge image development. This proportion is more preferably 8% or less, and particularly preferably 5% or less.
(3) Hydrophobicity Degree with Methanol
If the hydrophobicity degree with methanol of the surface-treated gas-phase-process silica particle is less than 68%, the silica particles easily aggregate due to remaining silanol groups on the silica surfaces, which causes poor dispersibility in the toner, and poor flowability of the toner and printed image quality when the silica particle is added into the toner as a toner external additive for electrostatic charge image development. If the hydrophobicity degree with methanol is more than 78%, a charge amount of the toner may be excessively high when the silica particle is added into the toner. The hydrophobicity degree with methanol in the present invention refers to a value measured under the following conditions.
<Method for Measuring Hydrophobicity Degree with Methanol>
Into 60 ml of an aqueous solution of methanol at a volume concentration of 50% (temperature: 25° C.), 0.2 g of the surface-treated gas-phase-process silica particle is added, and the mixture is stirred with a stirrer. Then, with dropping methanol into the liquid in which the silica particles float on the surface, the aqueous solution of methanol is irradiated with light at a wavelength of 780 nm to measure a transmittance. Specified as the hydrophobicity degree with methanol is a volume concentration (%) of methanol in an aqueous solution of methanol at a time where the spherical silica particles are suspended or precipitated and the transmittance is 80%.
The aggregation degree of the mixture of the polyester resin particle and the surface-treated gas-phase-process silica particle represents aggregation in a toner when the silica particles are dispersed in the toner. A smaller value of the aggregation degree means a smaller amount of aggregates in the toner, which can be evaluated to be good.
If the aggregation degree of the mixture of 100 parts by mass of the polyester resin particle having a volumetric median diameter of 5 to 8 μm and 0.1 part by mass of the surface-treated gas-phase-process silica particle is more than 20%, many aggregates are generated due to the toner bonding to each other and the toner flowability is degraded when the surface-treated gas-phase-process silica particle is added into the toner as the toner external additive for electrostatic charge image development. The aggregation degree is preferably 10% or less. The aggregation degree in the present invention refers to a value measured under the following condition,
By using 2 g of a mixture of 1 part by mass of the surface-treated gas-phase-process silica particle relative to 100 parts by mass of the polyester resin particle having a volumetric median diameter by a laser diffraction/scattering method of 5 to 8 μm mixed with a mixer, the mixture is vibrated using sieves having an aperture of 150 μm, 75 μm, and 45 μm from the upper side with a vibration width of 1 mm and a vibration frequency of 1 Hz for 60 seconds. After the vibration, amounts of the mixture remaining on the sieves are measured to calculate the aggregation degree with the following formula.
Aggregation Degree (%)=(W1+0.6×W2+0.2×W3)/2×100
The present invention also provides a toner external additive for electrostatic charge image development containing the above surface-treated gas-phase-process silica particle. The inventive surface-treated gas-phase-process silica particle can impart good flowability and printing characteristics to the toner when used as the toner external additive.
Hereinafter, the present invention will be specifically described by using Examples and Comparative Examples, but the present invention is not limited thereto.
Into a 5-L reaction apparatus equipped with a stirrer, a spraying apparatus, and a thermometer, 240 g of a gas-phase-process silica particle having a BET specific surface area of 50 m2/g was fed. After air in the reaction apparatus was substituted with dry nitrogen, 18 g of water was sprayed with the spraying apparatus with stirring. After the mixture was stirred at 25° C. for 1 hour, 0.6 g of divinyltetramethyldisilazane was sprayed, and the mixture was stirred at 60° C. for 1 hour. The mixture was once cooled to 25° C., and then 60 g of hexamethyldisilazane was sprayed. The mixture was stirred at 60° C. for 1 hour, and then further dried at 150° C. for 3 hours with stirring under a nitrogen flow. This mixture was cooled to obtain 243 g of a white powder of a surface-treated gas-phase-process silica particle (T).
In the same manner as in Example 1-1 except that the amount: of the added divinyltetramethyldisilazane was 1.2 g, 244 g of a white powder of a surface-treated gas-phase-process silica particle (II) was obtained.
In the same manner as in Example 1-1 except that a gas-phase-process silica particle having a BET specific surface area of 90 m2/g was used instead of the gas-phase-process silica particle having a BET specific surface area of 50 m2/g, 242 g of a white powder of a surface-treated gas-phase-process silica particle (III) was obtained.
Into a 5-L reaction apparatus equipped with a stirrer, a spraying apparatus, and a thermometer, 148 g of a gas-phase-process silica fine particle having a BET specific surface area of 130 m2/g was fed. After air in the reaction apparatus was substituted with dry nitrogen, 13 g of water was sprayed with the spraying apparatus with stirring. After the mixture was stirred at 25° C. for 1 hour, 0.4 g of divinyltetramethyldisilazane was sprayed, and the mixture was stirred at 60° C. for 1 hour. The mixture was once cooled to 25° C., and then 60 g of hexamethyldisilazane was sprayed. The mixture was stirred at 60° C. for 1 hour, and then further dried at 150° C. for 3 hours with stirring under a nitrogen flow. This mixture was cooled to obtain 51 g of a white powder of a surface-treated gas-phase-process silica particle (IV).
In the same manner as in Example 1-4 except that a gas-phase-process silica fine particle having a BET specific surface area of 200 m2/g was used instead of the gas-phase-process silica fine particle having a BET specific surface area of 130 m2/g, 153 g of a white powder of a surface-treated gas-phase-process silica particle (V) was obtained.
Into a 5-L, reaction apparatus equipped with a stirrer, a spraying apparatus, and a thermometer, 240 g of a gas-phase-process silica particle having a BET specific surface area of 50 m2/g was fed. After air in the reaction apparatus was substituted with dry nitrogen, 18 g of water was sprayed with the spraying apparatus with stirring. After the mixture was stirred at 25° C. for 1 hour, 60 q of hexamethyldisilazane was sprayed. The mixture was stirred at 60° C. for 1 hour, and then further dried at 150° C. for 3 hours with stirring under a nitrogen flow. This mixture was cooled to obtain 243 g of a white powder of a surface-treated gas-phase-process silica particle (VI).
Into a 5-L reaction apparatus equipped with a stirrer, a spraying apparatus, and a thermometer, 148 g of a gas-phase-process silica fine particle having a BET specific surface area of 130 m2/g was fed. After air in the reaction apparatus was substituted with dry nitrogen, 13 g of water was sprayed with the spraying apparatus with stirring. After the mixture was stirred at 25° C. for 1 hour, 60 g of hexamethyldisilazane was sprayed. The mixture was stirred at 60° C. for 1 hour, and then further dried at 150° C. for 3 hours with stirring under a nitrogen flow. This mixture was cooled to obtain 51 g of a white powder of a surface-treated gas-phase-process silica particle (VII).
Into a 5-L reaction apparatus equipped with a stirrer, a spraying apparatus, and a thermometer, 240 g of a gas-phase-process silica particle having a BET specific surface area of 50 m2/g was fed. After air in the reaction apparatus was substituted with dry nitrogen, 18 g of water was sprayed with the spraying apparatus with stirring. After the mixture was stirred at 25° C. for 1 hour, 60 g of divinyltetramethyldisilazane was sprayed. The mixture was stirred at 60° C. for 1 hour, and then further dried at 150° C. for 3 hours with stirring under a nitrogen flow. This mixture was cooled to obtain 247 g of a white powder of a surface-treated gas-phase-process silica particle (VIII).
The surface-treated gas-phase-process silica particles (I) to (VIII) obtained in the above steps were measured in accordance with the following measurement methods (1) to (4). Table 1 shows the measurement results.
By using a fully automatic BET specific surface area measuring apparatus (Macsorb HM model-1201, manufactured by MOUNTECH Co., Ltd.), the BET specific surface area was measured by a BET 1-point method using nitrogen.
Into a vial, 0.1 g of the surface-treated gas-phase-process silica particle and 19.9 g of methanol were added, the vial was placed in an ultrasonic-wave washing apparatus and irradiated with ultrasonic wave with an output of 30 W/L for 10 minutes to disperse the silica particles in methanol. A particle size distribution on a volumetric basis of the particles in the dispersion was measured by using a laser diffraction/scattering-type particle size distribution measuring apparatus (LA-950V2, manufactured by HORIBA, Ltd.), and based on the particle size distribution, the proportion of the aggregated particles having a particle diameter of 1.5 μm or more was calculated.
(3) Hydrophobicity Degree with Methanol
By using a powder wettability tester (WET101P, manufactured by RHESCA Co., LTD.), 0.2 g of the surface-treated gas-phase-process silica particle was added into 60 ml of an aqueous solution of methanol at a volume concentration of 50% (temperature: 25° C.), and the mixture was stirred with a stirrer. Then, with dropping methanol into the liquid in which the silica particles floated on the surface, the aqueous solution of methanol was irradiated with light at a wavelength of 780 nm to measure a transmittance. Specified as the hydrophobicity degree with methanol was a volume concentration (%) of methanol in an aqueous solution of methanol at a time where the spherical silica particles were suspended or precipitated and the transmittance was 80%.
1 part by mass of the surface-treated gas-phase-process silica particle to 100 parts by mass of the polyester resin particle having a volumetric median diameter by a laser diffraction/scattering method of 5 to 8 μm was mixed with a mixer. By using a powder characteristic evaluating apparatus (Powder Tester PT-X, manufactured by HOSOKAWA MICRON CORPORATION), 2 g of the mixture was vibrated using sieves having an aperture of 150 μm, 75 μm, and 45 μm from the upper side with a vibration width of 1 mm and a vibration frequency of 1 Hz for 60 seconds. After the vibration, amounts of the mixture remaining on the sieves were measured to calculate the aggregation degree with the following formula.
Aggregation Degree (%)=(W1+0.6×W2+0.2×W3)/2×100
As shown in Table 1, the surface-treated gas-phase-process silica particles obtained in Examples 1-1 to 1-5 had a small proportion of the aggregated silica particles, sufficient hydrophobicity degree with methanol, and in addition, a small toner aggregation degree. Meanwhile, the surface-treated gas-phase-process silica particles obtained in Comparative Examples 1-1 and 1-2, where the surface treatment with divinyltetramethyldisilazane was not performed, and in Comparative Example 1-3, where the surface treatment with hexamethyldisilazane was not performed, exhibited much aggregation of the silica particles with each other, low hydrophobicity degree with methanol, and high aggregation degree when added into the toner.
Melt-kneading 96 parts by weight of a polyester resin having Tg of 60° C. and a softening point of 110° C. and 4 parts by weight of CARMNINE 6BC (manufactured by SUMIKA COLOR CO., LTD.) as a colorant was performed, and the mixture was crushed and classified to obtain a toner having a volumetric median diameter of 7 μm. Mixing 10 g of this toner and 0.2 g of one of the surface-treated gas-phase-process silica particles obtained in Examples 1-1 to 1-5 and Comparative Examples 1-1 to 1-3 was performed with a sample mill to obtain an external additive-mixed toner.
Mixing 3 parts by mass of the external additive-mixed toner and 97 parts by mass of Standard Ferrite L (The Imaging Society of Japan) being a carrier was performed to prepare a two-component developer. The two-component developer obtained in the above steps was measured in accordance with the following methods (5) to (9). Table 2 show the results.
The two-component developer was exposed for one day to each condition of high-temperature and high-humidity (30° C., 90% RH), medium-temperature and medium-humidity (25° C., 55% RH), and low-temperature and low-humidity (10° C., 15% RH). Then, each of the samples was frictionally charged under the same conditions, and a charge amount in this time was measured by using a blow-off powder charge amount measuring apparatus (TB-200, manufactured by Toshiba Chemical Corp.).
The two-component developer was added into a developing apparatus equipped with an organic photoreceptor, and a printing test with 30,000 sheets was performed under an environment at 25° C. and 50% RH. In this time, adhesion of the toner to the photoreceptor can be detected as a void in a full solid image. Here, a degree of the voids was evaluated as follows: 10 or more voids per cm2 was evaluated as “many”, 1 to 9 voids was evaluated as “few”, and 0 voids was evaluated as “none”.
In the printing test in the above (6), photoreceptor wearing detected as disorder of the image was evaluated with the following criteria.
The two-component developer was exposed for one day to an environment at 30° C. and 90% RH, then 5,000 sheets were continuously printed with solid printing (image density: 100%) with 20 cm square, and thereafter, the two-component developer was left to stand again under the environment at 30° C. and 90% RH. This was repeated 60 times to print a total of 300,000 sheets. The 10th print in the first day was specified as a print 1, and the last print in the last day was specified as a print 2.
Presence or absence of an image defect (white spot) in the print 2 obtained above was evaluated with image observation by the following criteria.
A change in density of the print 2 relative to the print 1 was evaluated under the following criteria by measuring a color difference (ΔE) in a color space CIE1976 (L*a*b*) by using a reflective densitometer X-rite938 (manufactured by X-Rite, Incorporated.) in accordance with JIS Z 8781-5.
0%
%
%
)
0
4
4
2
indicates data missing or illegible when filed
As shown in Table 2, the two-component developers in which the surface-treated gas-phase-process silica particles obtained in Examples 1-1 to 1-5 were used as the toner external additive exhibited no defect in the printed image. Meanwhile, those using the surface-treated gas-phase-process silica particles obtained in Comparative Examples 1-1 to 1-3 had large variation of the toner charge amount due to the environment, and had poor printing characteristics.
It should be noted that the present invention is not limited to the above-described embodiments. The embodiments are just examples, and any examples that substantially have the same feature and demonstrate the same functions and effects as those in the technical concept disclosed in claims of the present invention are included in the technical scope of the present invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2021-024701 | Feb 2021 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2021/047691 | 12/22/2021 | WO |
