JP2013216537A - Method for producing ferrite particle - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing a ferrite particle having a low specific gravity, and no generation of a crack and chip.SOLUTION: A method for producing a ferrite particle includes: a step of obtaining slurry by throwing an Fe component raw material and an M component raw material which are adjusted in their components so as to form the ferrite particle expressed by MxFe-xOinto a dispersion medium; and a step of spraying and drying the slurry, and obtaining a granule, and a step of firing the granule and obtaining a fired product. And it is characterized in that the M component raw material includes at least a first metal carbonate having its decomposition temperature of 100°C-600°C under low oxygen atmosphere, and a second metal carbonate having its decomposition temperature of 650°C-1,200°C. The weight ratio between the first metal carbonate and the second metal carbonate is in a range of 10:1-100:1.

Description

  The present invention relates to a method for producing ferrite particles.

  For example, in an image forming apparatus such as a facsimile, a printer, or a copier using an electrophotographic system, a toner is attached to an electrostatic latent image formed on the surface of a photosensitive member to make a visible image, and the visible image is formed on a sheet. After being transferred to, etc., it is fixed by heating and pressing. A so-called two-component developer including a carrier and a toner is widely used as a developer from the viewpoint of high image quality and colorization.

  In the developing method using a two-component developer, the carrier and the toner are stirred and mixed in the developing device, and the toner is charged to a predetermined amount by friction. Then, a developer is supplied to the rotating developing roller, a magnetic brush is formed on the developing roller, and the toner is electrically moved to the photosensitive member via the magnetic brush, so that an electrostatic latent image on the photosensitive member can be formed. Visualize. The carrier after the toner movement remains on the developing roller and is mixed with the toner again in the developing device. For this reason, as the characteristics of the carrier, magnetic characteristics for forming a magnetic brush, charging characteristics for imparting a desired charge to the toner, and durability in repeated use are required.

  Therefore, a carrier in which the surface of magnetic particles such as magnetite and various ferrites is coated with a resin is generally used. However, since the carrier used so far has a high apparent density (specific gravity), the power required for stirring the developer. In addition, toner deterioration such as cracking of the toner and embedding of the toner external additive in the toner particles was likely to occur. Therefore, in combination with the recent increase in the speed of image forming apparatuses, a reduction in specific gravity of carriers has been strongly desired.

  Therefore, for example, Patent Document 1 proposes a technique for reducing the specific gravity of carrier core particles by forming pores of a predetermined size in the particles.

JP 2008-310104 A

  However, the proposed carrier core particles have large vacancies formed in the particles, and when used in an apparatus having a high image forming speed, there is a possibility that the carrier core particles may be cracked or chipped.

  The present invention has been made in view of such a conventional problem, and its object is to have a low specific gravity even when the image forming speed is increased when used as a carrier of an electrophotographic image forming apparatus. An object of the present invention is to provide a method for producing ferrite particles which does not cause cracks or chips.

Manufacturing method according to the present invention for achieving the above _{object, M X Fe 3-X O} 4 ( provided that M is at least one Mg, Mn, Ca, Ti, Cu, Zn, Sr, selected from the group consisting of Ni And adding a Fe component raw material and an M component raw material whose components are adjusted so that ferrite particles having a composition represented by 0 ≦ X ≦ 1) are formed into a dispersion medium, A method for producing ferrite particles comprising a step of spray-drying a slurry to obtain a granulated product, and a step of firing the granulated product to obtain a fired product, wherein the M component raw material is decomposed in a low oxygen atmosphere. At least a first metal carbonate having a temperature in the range of 100 ° C. to 600 ° C. and a second metal carbonate having a decomposition temperature in the range of 650 ° C. to 1200 ° C., wherein the first metal carbonate and the second metal carbonate The weight ratio of metal carbonate to 10: 1 It is characterized by being in the range of ˜100: 1.

  Here, in the step of obtaining the fired product by firing the granulated product, after maintaining a predetermined temperature in the range of 300 ° C. to 600 ° C. for 5 hours or longer, the predetermined temperature in the range of 800 ° C. to 1200 ° C. is maintained for 3 hours or longer. It is preferable to hold.

  Moreover, it is preferable that ratio of the average particle diameter of 1st metal carbonate and 2nd metal carbonate is the range of 1: 1-10: 1.

  The first metal carbonate is preferably manganese carbonate or magnesium carbonate.

  Furthermore, the second metal carbonate is preferably any one of calcium carbonate, barium carbonate, and strontium carbonate.

  In the production method of the present invention, since two kinds of metal carbonates having different decomposition temperatures are used as the M component raw material at a specific weight ratio, pores can be formed almost uniformly inside the particles, and the strength of the particles can be reduced. Low specific gravity can be achieved while suppressing.

2 is a cross-sectional SEM photograph of the ferrite particles of Example 1. 3 is a cross-sectional SEM photograph of ferrite particles of Comparative Example 1.

  The method for producing ferrite particles according to the present invention will be described below in the order of steps. First, an Fe component raw material, an M component raw material, and, if necessary, an additive are weighed, put into a dispersion medium, and mixed to prepare a slurry. M is at least one metal element selected from divalent metal elements such as Mg, Mn, Ca, Ti, Cu, Zn, Sr, and Ni. What is important here is that, as the M component raw material, a first metal carbonate having a decomposition temperature in the range of 100 ° C. to 600 ° C. under a low oxygen atmosphere and a second metal carbonate having a decomposition temperature in the range of 650 ° C. to 1200 ° C. And at least the ratio of the first metal carbonate and the second metal carbonate in the range of 10: 1 to 100: 1 by weight ratio. By using these two types of metal carbonates having different decomposition temperatures at a predetermined weight ratio, pores are formed almost uniformly throughout the particles of the sintered product in the step of sintering the granulated product described later. The A more preferable range of the weight ratio is 20: 1 to 50: 1.

  By controlling the total amount of the first metal carbonate and the second metal carbonate with respect to the starting material, the total area of the particles in the particle cross-sectional area of the pores formed inside the particles can be controlled. % To 40 wt% is preferable, and more preferably 1 to 20 wt%. In addition, the average particle diameter of the first metal carbonate and the second metal carbonate is usually preferably in the range of 0.5 μm to 15 μm, and the ratio of the average particle diameter is 1: 1 to 10: 1. The range of is preferable.

The first metal carbonate used in the present invention is not particularly limited as long as the decomposition temperature in a low oxygen atmosphere is in the range of 100 ° C to 600 ° C. For example, manganese carbonate and magnesium carbonate are preferable. Used for. In addition, the second metal carbonate used in the present invention is not particularly limited as long as the decomposition temperature in a low oxygen atmosphere is in the range of 650 ° C. to 1200 ° C., for example, calcium carbonate or barium carbonate. Strontium carbonate and the like are preferably used. As the Fe component raw material used in the present invention, Fe ₂ O ₃ or the like is preferably used.

  Water is preferred as the dispersion medium used in the present invention. In addition to the Fe component raw material and M component raw material, a binder, a dispersant, and the like may be blended in the dispersion medium, if necessary. For example, polyvinyl alcohol can be suitably used as the binder. The blending amount of the binder is preferably about 0.5 to 2 wt% in the slurry. Moreover, as a dispersing agent, polycarboxylate ammonium etc. can be used conveniently, for example. As the blending amount of the dispersant, the concentration in the slurry is preferably about 0.5 to 2 wt%. In addition, you may mix | blend a lubricant, a sintering accelerator, etc. The solid content concentration of the slurry is desirably in the range of 50 to 90 wt%. Further, before introducing the Fe component raw material and the M component raw material into the dispersion medium, if necessary, pulverization and mixing may be performed.

  And the slurry produced as mentioned above is wet-ground if necessary. For example, wet grinding is performed for a predetermined time using a ball mill or a vibration mill. The average particle diameter of the raw material after pulverization is preferably 50 μm or less, more preferably 10 μm or less. The vibration mill or ball mill preferably contains a medium having a predetermined particle diameter. Examples of the material of the media include iron-based chromium steel and oxide-based zirconia, titania, and alumina. As a form of a grinding | pulverization process, any of a continuous type and a batch type may be sufficient. The particle size of the pulverized product is adjusted depending on the pulverization time and rotation speed, the material and particle size of the media used, and the like.

  Next, the pulverized slurry is spray-dried and granulated. Specifically, the slurry is introduced into a spray dryer such as a spray dryer, and granulated into a spherical shape by spraying into the atmosphere. The atmospheric temperature during spray drying is preferably in the range of 100 ° C to 300 ° C. Thereby, a spherical granulated product having a particle diameter of 10 μm to 200 μm is obtained. In addition, it is desirable that the obtained granulated product has a sharp particle size distribution by removing coarse particles and fine powder using a vibration sieve or the like.

  Next, the granulated product is put into a firing furnace and fired by a general method for synthesizing ferrite particles, thereby generating ferrite particles. The firing temperature condition is not particularly limited, but from the viewpoint of effectively thermally decomposing the first metal carbonate and the second metal carbonate, a predetermined temperature in the range of 300 ° C. to 600 ° C. is maintained for 5 hours or more. Thereafter, it is preferable to maintain a predetermined temperature in the range of 800 ° C. to 1200 ° C. for 3 hours or more. By holding at a predetermined temperature in the range of 300 ° C. to 600 ° C. for 5 hours or longer, first, the first metal carbonate having a low decomposition temperature is decomposed to generate a metal oxide and carbon dioxide gas. Usually, since the firing proceeds at a temperature of 800 ° C. or more, the generated carbon dioxide gas escapes from the granulated product that has not been sufficiently sintered, and pores are formed in the granulated product. Openings of pores are formed on the surface of the object.

  After that, when the temperature is raised to a predetermined temperature in the range of 800 ° C. to 1200 ° C. and held at that temperature for 3 hours or more, the sintering reaction starts, and the opening formed on the surface of the granulated product is once blocked by crystal growth. . And decomposition | disassembly of a 2nd metal carbonate begins, and a metal oxide and a carbon dioxide gas are produced | generated. The generated carbon dioxide gas forms new pores, is connected to the already formed pores, reopens the blocked opening, and escapes to the outside. As a result, pores are formed substantially uniformly throughout the particles of the sintered product, and the specific gravity can be reduced while suppressing a decrease in the strength of the particles.

  Next, the fired product thus obtained is pulverized as necessary. Specifically, for example, the fired product is pulverized by a hammer mill or the like. The form of the granulation step may be either a continuous type or a batch type. And if necessary, classification may be performed in order to make the particle size in a predetermined range. As a classification method, a conventionally known method such as air classification or sieve classification can be used. In addition, after primary classification with an air classifier, the particle size may be aligned within a predetermined range with a vibration sieve or an ultrasonic sieve. Furthermore, you may make it remove a nonmagnetic particle with a magnetic field separator after a classification process.

  Then, if necessary, the powder (baked product) after classification may be heated in an oxidizing atmosphere to form an oxide film on the particle surface to increase the resistance of the ferrite particles (high resistance treatment). ). The oxidizing atmosphere may be either an air atmosphere or a mixed atmosphere of oxygen and nitrogen. The heating temperature is preferably in the range of 200 ° C to 800 ° C, and more preferably in the range of 250 ° C to 600 ° C. The heating time is preferably in the range of 0.5 hours to 5 hours.

  The ferrite particles produced by the production method of the present invention as described above can be used in various applications, for example, electrophotographic developer carriers and electromagnetic wave absorbing materials, electromagnetic shielding material powders, rubbers, plastic fillers, It can be used as a reinforcing material, paint, matting material for paint / adhesive, filler, reinforcing material, and the like. Among these, it is particularly preferably used as a carrier for electrophotographic development.

  When the ferrite particles are used as a carrier for electrophotographic development, the ferrite particles can be used as they are as a carrier for electrophotographic development. However, from the viewpoint of chargeability, the surface of the ferrite particles is used by coating with a resin. preferable.

  As the resin for covering the surface of the ferrite particles, conventionally known resins can be used, for example, polyethylene, polypropylene, polyvinyl chloride, poly-4-methylpentene-1, polyvinylidene chloride, ABS (acrylonitrile-butadiene-styrene). Examples thereof include resins, polystyrene, (meth) acrylic resins, polyvinyl alcohol resins, polyvinyl chloride-based, polyurethane-based, polyester-based, polyamide-based, polybutadiene-based thermoplastic elastomers, fluorine silicone-based resins, and the like.

  In order to coat the surface of the ferrite particles with a resin, a resin solution or dispersion may be applied to the ferrite particles. Solvents for the coating solution include aromatic hydrocarbon solvents such as toluene and xylene; ketone solvents such as acetone, methyl ethyl ketone, methyl isobutyl ketone, and cyclohexanone; cyclic ether solvents such as tetrahydrofuran and dioxane; ethanol, propanol, and butanol Alcohol solvents such as ethyl cellosolve, cellosolve solvents such as butyl cellosolve; ester solvents such as ethyl acetate and butyl acetate; amide solvents such as dimethylformamide and dimethylacetamide, etc. . The concentration of the resin component in the coating solution is generally in the range of 0.001 to 30 wt%, particularly 0.001 to 2 wt%.

  As a method for coating the resin on the ferrite particles, for example, a spray drying method, a fluidized bed method, a spray drying method using a fluidized bed, an immersion method, or the like can be used. Among these, the fluidized bed method is particularly preferable in that it can be efficiently applied with a small amount of resin. For example, in the case of the fluidized bed method, the resin coating amount can be adjusted by the amount of resin solution sprayed and the spraying time.

When ferrite particles are used as a carrier core material for electrophotographic development, the particle diameter is generally in the range of 10 to 200 μm, particularly in the range of 10 to 50 μm in terms of volume average particle diameter. Moreover, the preferable electrical resistance of the ferrite particles is in the range of 1.0 × 10 ⁵ Ω · cm to 1.0 × 10 ¹⁰ Ω · cm at an applied voltage of 1000V. If the electrical resistance is less than 1.0 × 10 ⁵ Ω · cm, charge leakage may occur. On the other hand, if the electrical resistance exceeds 1.0 × 10 ¹⁰ Ω · cm, the edge effect increases and the image density increases. There is a risk of lowering. A more preferable electric resistance of the ferrite particles is in the range of 1.0 × 10 ⁷ Ω · cm to 1.0 × 10 ⁹ Ω · cm.

Further, the apparent density (specific gravity) of the ferrite particles is preferably 1.50 g / cm ³ or less. This is because if the apparent density is higher than 1.50 g / cm ³ , the power required for stirring cannot be sufficiently reduced. A more preferable apparent density is 1.45 g / cm ³ or less.

  The carrier produced as described above is mixed with toner to form a two-component developer. The mixing ratio of the carrier and the toner is not particularly limited, and may be determined as appropriate based on the developing conditions of the developing device to be used. In general, the toner concentration in the developer is preferably in the range of 1 wt% to 15 wt%. When the toner density is less than 1 wt%, the image density becomes too thin, and when the toner density exceeds 15 wt%, the toner scatters in the developing device, and the toner adheres to the background portion such as in-machine dirt or transfer paper. This is because there is a risk of occurrence. A more preferable toner concentration is in the range of 3 to 10 wt%.

  As the toner, toner produced by a conventionally known method such as a polymerization method, a pulverization classification method, a melt granulation method, or a spray granulation method can be used. Specifically, a binder resin containing a thermoplastic resin as a main component and containing a colorant, a release agent, a charge control agent and the like can be suitably used.

  In general, the particle diameter of the toner is preferably in the range of 4 μm to 12 μm, more preferably in the range of 5 μm to 8 μm, as a volume average particle diameter measured by a Coulter counter.

  If necessary, a modifier may be added to the toner surface. Examples of the modifier include silica, alumina, zinc oxide, titanium oxide, magnesium oxide, polymethyl methacrylate and the like. These 1 type (s) or 2 or more types can be used in combination.

  A known mixing device can be used for mixing the carrier and the toner. For example, a Henschel mixer, a V-type mixer, a tumbler mixer, a hybridizer, or the like can be used.

  EXAMPLES Hereinafter, although an Example demonstrates this invention further in detail, this invention is not limited to these Examples at all.

Example 1
Mn ferrite particles were produced by the following method. As starting materials, Fe ₂ O ₃ (average particle size: 0.6 μm) 7.0 kg, MnCO ₃ (average particle size: 5.0 μm) 1.9 kg, Mn ₃ O ₄ (average particle size: 0.9 μm) ) 1.3 kg and CaCO ₃ (average particle size: 1 μm) 60 g were dispersed in 3.0 kg of pure water, and 60 g of an ammonium polycarboxylate dispersant was added as a dispersant to obtain a mixture. This mixture was pulverized by a wet ball mill (media diameter 2 mm) to obtain a mixed slurry.

  This mixed slurry was sprayed into hot air of about 130 ° C. with a spray dryer to obtain a dry granulated product having a particle size of 10 μm to 100 μm. From this granulated material, coarse particles having a particle size exceeding 100 μm were removed using a sieve.

  The granulated product was put into an electric furnace and held at 500 ° C. for 8 hours, and then heated to 900 ° C. and held for 3 hours for firing. At this time, the gas which mixed oxygen and nitrogen was supplied in the electric furnace so that the oxygen concentration in an electric furnace might be set to 5000 ppm.

  The obtained fired product was pulverized with a hammer mill and classified using a vibration sieve to obtain ferrite particles having an average particle size of 30 μm.

  The porosity, apparent density, magnetic properties, and electric resistance in the cross section of the obtained ferrite particles were measured by the methods shown below. Table 1 summarizes the measurement results. FIG. 1 shows an SEM photograph of the particle cross section.

(Porosity in particle cross section)
The obtained ferrite particles were dispersed in a thermosetting resin, and then the resin was cured by heating. The surface of the cured product was polished using a cross section polisher (manufactured by JEOL Ltd.). The polished particle surface was observed using a scanning electron microscope (manufactured by JEOL Ltd.), and a cross-sectional photograph of the particle was taken. The photographed cross section of the particle was separated into a particle portion and a void portion using the image analysis software “Image-Pro”, and the area ratio of the void portion to the total area was measured to obtain the porosity. This porosity was measured for 100 particles, and the average value was defined as the porosity.

(Apparent density)
The apparent density of the ferrite particles was measured according to JIS Z 2504.

(Magnetic properties)
Using a vibration sample type magnetometer (VSM) dedicated to room temperature (“VSM-P7” manufactured by Toei Kogyo Co., Ltd.), the external magnetic field ranges from 0 to 79.58 × 10 ⁴ A / m (10000 Oersted) for one cycle. The magnetization σ ₁₀₀₀ (Am ² / kg) in a magnetic field of saturation magnetization, residual magnetization, coercive force, and 79.58 × 10 ³ A / m (1000 oersted) was measured.

(Electrical resistance)
Two brass plates as electrodes having a thickness of 2 mm whose surfaces were electropolished were arranged to face each other with a distance of 2 mm. After inserting 200 mg of ferrite particles between the electrodes, a magnet having a sectional area of 240 cm ² (ferrite magnet having a surface magnetic flux density of 1500 gauss) is arranged behind each electrode to form a bridge of ferrite particles between the electrodes. It was. Then, a DC voltage of 1000 V was applied between the electrodes, the current value flowing through the ferrite particles was measured, and the electrical resistance of the ferrite particles was calculated.

Examples 2-6, Comparative Examples 1-4
Ferrite particles were produced in the same manner as in Example 1 with the starting materials, blending amounts and firing temperatures shown in Table 1. And each physical property was measured like Example 1. FIG. Table 1 summarizes the measurement results. Moreover, the cross-sectional SEM photograph of the ferrite particle of the comparative example 1 is shown in FIG.

As is apparent from Table 1, the ferrite particles of Examples 1 to 6 according to the production methods of the present invention using two kinds of metal carbonates having different decomposition temperatures at a specific weight ratio have a porosity of 13. It was as high as 2% or more, and the apparent density was as low as 1.43 g / cm ³ or less. Further, as apparent from FIG. 1, in the ferrite particles of Example 1, pores were uniformly formed inside the particles.

In contrast, the ferrite particles of Comparative Example 1 that did not use metal carbonate as the M component raw material had a porosity of as low as 7.2% and an apparent density as high as 1.61 g / cm ³ . Moreover, all of the ferrite particles of Comparative Examples 2 to 4 using only one kind of metal carbonate as the M component raw material have a porosity of as low as 9.2% or less and an apparent density of 1.55 g / cm ^3. It was higher than above.

  In the production method of the present invention, by using two kinds of metal carbonates having different decomposition temperatures as the M component raw material at a specific weight ratio, pores can be formed almost uniformly inside the particle, and the strength of the particle is reduced. This is useful because the specific gravity can be reduced while suppressing the above.

Claims (5)

M _X Fe _{3 -X} O ₄ (where M is at least one metal element selected from the group consisting of Mg, Mn, Ca, Ti, Cu, Zn, Sr, Ni, 0 ≦ X ≦ 1) A step of obtaining a slurry by adding an Fe component raw material and an M component raw material whose components are adjusted so as to produce ferrite particles having a composition to obtain a slurry; and a step of spray-drying the slurry to obtain a granulated product; A method for producing ferrite particles comprising a step of firing the granulated product to obtain a fired product,
The M component raw material includes at least a first metal carbonate having a decomposition temperature in the range of 100 ° C. to 600 ° C. in a low oxygen atmosphere and a second metal carbonate having a decomposition temperature in the range of 650 ° C. to 1200 ° C. A method for producing ferrite particles, wherein the ratio of the first metal carbonate and the second metal carbonate is in the range of 10: 1 to 100: 1 by weight.   In the step of firing the granulated material to obtain a fired product, after maintaining a predetermined temperature in the range of 300 ° C. to 600 ° C. for 5 hours or more, the predetermined temperature in the range of 800 ° C. to 1200 ° C. is maintained for 3 hours or more. Item 2. The production method according to Item 1.   The production method according to claim 1 or 2, wherein the ratio of the average particle diameter of the first metal carbonate and the second metal carbonate is in the range of 1: 1 to 10: 1.   The manufacturing method according to claim 1, wherein the first metal carbonate is manganese carbonate or magnesium carbonate.   The manufacturing method according to any one of claims 1 to 4, wherein the second metal carbonate is any one of calcium carbonate, barium carbonate, and strontium carbonate.