WO2014104177A1 - ニオブコンデンサ陽極用化成体及びその製造方法 - Google Patents
ニオブコンデンサ陽極用化成体及びその製造方法 Download PDFInfo
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- WO2014104177A1 WO2014104177A1 PCT/JP2013/084849 JP2013084849W WO2014104177A1 WO 2014104177 A1 WO2014104177 A1 WO 2014104177A1 JP 2013084849 W JP2013084849 W JP 2013084849W WO 2014104177 A1 WO2014104177 A1 WO 2014104177A1
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C27/00—Alloys based on rhenium or a refractory metal not mentioned in groups C22C14/00 or C22C16/00
- C22C27/02—Alloys based on vanadium, niobium, or tantalum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/12—Metallic powder containing non-metallic particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/14—Treatment of metallic powder
- B22F1/142—Thermal or thermo-mechanical treatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/14—Treatment of metallic powder
- B22F1/148—Agglomerating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/10—Sintering only
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/34—Anodisation of metals or alloys not provided for in groups C25D11/04 - C25D11/32
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/48—After-treatment of electroplated surfaces
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/048—Electrodes or formation of dielectric layers thereon characterised by their structure
- H01G9/052—Sintered electrodes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/048—Electrodes or formation of dielectric layers thereon characterised by their structure
- H01G9/052—Sintered electrodes
- H01G9/0525—Powder therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
- B22F2998/10—Processes characterised by the sequence of their steps
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/16—Making metallic powder or suspensions thereof using chemical processes
- B22F9/18—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds
- B22F9/20—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from solid metal compounds
Definitions
- the present invention relates to a chemical composition for a capacitor anode obtained from a niobium granulated product. More specifically, the present invention relates to a method for producing a niobium granulated product, a method for producing a niobium sintered body, a niobium capacitor formation and its production method, and a niobium capacitor and its production method.
- the niobium granulated product according to the present invention has a high binding strength, and a capacitor having a large capacitance can be obtained by using as an anode a chemical formed by forming a dielectric layer on the sintered product of the granulated product.
- the granulated product has a structure in which hundreds of primary particles are connected.
- the primary particles of the granulated product are made smaller, so that the binding portion between the primary particles becomes thin, so that the binding strength decreases.
- the voids formed inside the particles are filled with primary particles that have lost their binding state, and the porous surface area is reduced and the specific surface area is reduced. Electric capacity decreases.
- this porous body is sintered, formed, attached with a cathode material, attached to a frame and sealed with resin to finish it as a solid electrolytic capacitor.
- the granulated material is physically damaged by heat and pressure at the sealing stage, and leakage current increases or conducts, so that the performance as a capacitor is not exhibited.
- Patent Document 1 discloses a metal powder structure in which an oxide or salt of metallic cobalt is granulated in the presence of a binder, a solvent and the like, and this is reduced with hydrogen. Although the particles are disclosed, the solvent and binder used in the granulation operation are completely removed during the reduction with hydrogen, and the attached photograph does not have a porous shape like the metal powder for capacitors.
- Patent Document 2 discloses a method for preparing a sintered sintered body having wear resistance by pre-sintering a raw material powder and mixing it with an intergranular bond inhibitor. A method of removing the intergranular bond inhibitor after ligation is disclosed.
- Patent Document 3 describes an example in which an electrolytic capacitor is produced by mixing and sintering a fluoride in tantalum powder or niobium powder and measuring the capacity. It describes the use of materials that do not evaporate at low temperatures so as to maintain porosity up to the actual sintering temperature.
- Patent Document 3 describes the use of materials that do not evaporate at low temperatures so as to maintain porosity up to the actual sintering temperature.
- these prior arts have hints that lead to improvements in the binding performance of niobium powder granules, damage to sintered porous bodies under resin sealing conditions, and deterioration of capacitor performance due to increased leakage current. No such technology is described.
- JP 2000-500826 (US Pat. No. 6,126,712) JP 2001-303106 A JP-A-48-25859
- the present invention has an object to solve the above-mentioned problems in niobium capacitors, and is a porous niobium granule having a high binding strength, an electrolytic capacitor having a large capacitance, and a niobium capacitor anode capable of producing an element.
- An object of the present invention is to provide a chemical compound of the above and a production method thereof.
- the present inventors have mixed niobium hydride and a compound containing a metal element other than niobium to form a mixture, and the heat treatment temperature at which the mixture is aggregated to form granulated particles, A conversion product obtained by setting a temperature higher than the diffusion start temperature of a compound containing a metal element other than niobium to obtain a niobium granulated product, which is sintered and formed, and having a dielectric layer on the surface.
- the inventors have found that the above-described problems can be solved by using a capacitor anode chemical composition characterized in that metal elements other than niobium are distributed so as to surround the periphery of niobium, and the present invention has been completed.
- the present invention relates to the following niobium granulated product production method [1] to [8], [9] production method of sintered body, [10] chemical production method, [11] to [11] [13] A method for producing a capacitor, [14] to [17] chemicals, and [18] capacitor.
- Method. [10] A method for producing a chemical conversion body for a capacitor, comprising obtaining a sintered body by the method described in the preceding item 9, and electrolytically oxidizing the sintered body to form a dielectric layer on the surface. [11] A method for producing a capacitor, characterized in that a chemical compound is obtained by the method described in item 10 above, and a cathode is formed on a dielectric layer on the surface of the chemical compound.
- a method for manufacturing a capacitor comprising sintering a niobium granulated material to obtain a sintered body, electrolytically oxidizing the sintered body to obtain a chemical compound, and forming a cathode on a dielectric layer on the surface of the chemical compound
- a method for producing a capacitor comprising adjusting a heat treatment temperature.
- the metal oxide is a valve action metal oxide.
- the valve action metal oxide is tantalum pentoxide, tin (IV) oxide, or tungsten (VI) oxide.
- a capacitor comprising the chemical composition according to any one of the above items 14 to 17 and a cathode on a dielectric layer on a surface of the chemical composition.
- the binding strength of the niobium granule is improved, and the element molded using this granule has a porous body, a specific surface area, and a capacitor with a large capacitance.
- the additive acts as an auxiliary agent for fusion of niobium. For this reason, sintering the molded element results in a sintered body with a strength exceeding the required standard, so increasing the capacitance by lowering the heat treatment temperature and the sintering temperature until the required standard strength is exhibited. Can be made.
- an oxide of a valve metal is used as an additive, it becomes a dielectric that is compatible with a niobium dielectric oxide film. Therefore, in an electrolytic capacitor made using this granulated product, the additive is electrically Since the properties are not affected, it is not necessary to remove the additive in a later step.
- FIG. 6 is a TEM photograph of a cross section of the chemical conversion element of Example 5.
- 6 is a photograph showing the distribution of Sn L ⁇ rays by EDX in the cross section of the chemical conversion element of Example 5.
- FIG. 6 is a photograph showing the distribution of O k ⁇ rays by EDX in the cross section of the conversion element of Example 5.
- FIG. The chemical element cross section of Example 7 is TEM.
- FIG. 10 is a photograph showing the distribution of O k ⁇ rays by EDX on the cross section of the chemical conversion element of Example 7.
- FIG. 10 is a photograph showing the distribution of O k ⁇ ray
- the chemical compound according to the present invention is prepared by mixing niobium hydride and a compound containing a metal element other than niobium (hereinafter sometimes abbreviated as “additive”) to form a mixture, and aggregating the mixture.
- a compound containing a metal element other than niobium hereinafter sometimes abbreviated as “additive”
- additive a compound containing a metal element other than niobium
- Niobium hydride is used as a raw material.
- Niobium hydride is generally a niobium ingot that has been occluded by heating under a hydrogen atmosphere.
- niobium reduced powder obtained by sodium reduction of niobium fluoride is used as an acid containing hydrofluoric acid. Washing with hydrogen to remove impurities, and at the same time, absorbing hydrogen, niobium deoxygenated powder obtained by magnesium deoxygenation of niobium oxide, acid-washed to remove the reducing agent magnesium, further washed with hydrofluoric acid
- the raw material manufacturing method is not limited as long as it is a hydrogen embrittled niobium powder such as a hydrogen occluded one.
- niobium powder with a low hydrogen occlusion degree or dehydrogenated by vacuum heat treatment loses brittleness and malleability ductility appears, and in subsequent milling, the powder does not become fine and changes to a flat shape. In many cases, such a shape is difficult to granulate.
- the hydrogen concentration of niobium hydride for obtaining hydrogen embrittlement is 0.4 to 1.0%, preferably 0.7 to 1.0%.
- Td 0.757Tm
- Td the diffusion start temperature
- Tm the melting point (absolute temperature) measured under a pressure of 1 atm.
- a compound (additive) containing an element other than niobium added to niobium hydride is a substance having a diffusion start temperature of 1100 ° C. or less and not reacting with niobium or other additives.
- Examples include tantalum (diffusion start temperature 1045 ° C.), tungsten (VI) (diffusion start temperature 1049 ° C.), and tin (IV) oxide (diffusion start temperature 919 ° C.). These are all oxides, but inorganic salts of these metals can also be used. However, only a few types of fluorides and sulfides have a diffusion start temperature within the processing temperature range, and fluorine and sulfur may affect subsequent capacitor characteristics. It is preferable to use a compound. In addition, since a compound that decomposes during heat treatment does not become a fusion aid, it is preferable to use a compound that does not decompose during heat treatment.
- stirring ball mill As a method for microscopic mixing of these additives and niobium hydride, it is preferable to use a stirring ball mill method in which the raw material can be refined and mixed at the same time.
- the stirring ball mill for example, an attrition ball mill and a bead mill are preferable.
- the bead diameter used in the bead mill is 0.3 to 3 mm, preferably coarsely pulverized with 3 mm beads, and finely pulverized with 0.5 mm beads. .
- the bead diameter for pulverizing the particles becomes large, the dead space in the mill increases, and pulverization becomes inefficient.
- the degree of attainment of pulverization depends on the bead diameter, it is desirable to replace the bead with one having a smaller diameter when the average particle diameter of the material reaches several ⁇ m.
- the bead filling amount is preferably 60 to 90%. If it is less than 60%, the number of collisions between the beads and the raw material is small, and the crushing efficiency is inferior.
- the stirring speed is preferably 20 to 30 Hz. If it is less than 20 Hz, the collision speed between the beads and the raw material is small and the pulverization efficiency is inferior. If it exceeds 30 Hz, the collision speed is too high and the apparatus itself is damaged.
- the pulverization rate is preferably about 0.7 to 1.3 kg / hour (h) depending on the capacity of the apparatus. When the material is less than the capacity of the device, grinding proceeds in a short time, and mixing is insufficient when the desired average particle size is reached. Therefore, the pulverization ratio is preferably within the above range.
- the end point of grinding is determined by determining the average particle size of the material.
- a laser diffraction particle size distribution meter is preferably used as the quickest and most convenient method.
- the primary particle diameter is reached in advance because there is an exponential relationship between the grinding time and the average particle diameter.
- the crushing time to be estimated can be estimated and efficient work can be performed. In this way, a slurry in which niobium hydride and an additive are microscopically mixed is obtained.
- the particles are densely packed. If heat treatment is performed in this state, all of them are integrated and the requirement as a niobium granulated product is not satisfied. Therefore, it is necessary to granulate appropriately.
- the pore forming material can be used without limitation so that the particles after the heat treatment become porous.
- the pore-forming material is not reactive with a mixture of niobium hydride and a compound containing a metal element other than niobium, can be easily removed, and can be added directly to the slurry in the form of fine particles having an average particle size of 0.5 to 5 ⁇ m.
- a substance is preferred.
- the pore forming material include metal oxides, inorganic salts, and organic compounds.
- metal oxides include magnesium oxide
- inorganic salts include ammonium chloride
- organic compounds include camphor. Of these, alkaline earth metal oxides (such as magnesium oxide) that have a high melting point and do not evaporate during heat treatment and are easily removed by acid cleaning are preferred.
- Granulation is performed to improve the physical properties of the powder.
- the non-granulated powder is an agglomerate having an indeterminate particle shape and inferior in fluidity, whereas the granulated powder is round and rich in fluidity, which is preferable in terms of molding.
- the binding strength of the granulated product is small, fine particles with several primary particles are generated, which deteriorates the fluidity and causes die leakage and die galling in the molding machine.
- the granulated product is also preferable from the viewpoint that the primary particles are not shaped so as to be lost.
- the raw material after granulation is heat treated to desorb hydrogen from the raw material to form niobium, and at the atomic level by thermal diffusion to form a network with neighboring particles, thereby increasing the bonding strength.
- the heat treatment temperature at this time needs to be equal to or higher than the temperature at which the raw material atoms start to diffuse. If the temperature is too high, the diffused atoms tend to decrease the surface energy, so the specific surface area decreases. This is directly linked to a decrease in the capacitance of the anode body obtained from the granulated product, so that the required bonding strength and the required capacitance to provide the required binding strength of the granulated product.
- the heat treatment conditions are naturally determined by appropriately setting.
- Niobium diffusion start temperature is 614 ° C. Since the heat treatment temperature normally used in the production of niobium powder exceeds 1000 ° C., niobium has a temperature condition sufficient for diffusion, and a network of particles is formed and grows through the contact points of the particles. At this time, the additive (the material whose diffusion start temperature is 1100 ° C. or less) also exceeds its own diffusion start temperature, but diffuses. However, the difference between the heat treatment temperature and the diffusion start temperature is not as great as that of niobium atoms. Does not happen on a large scale like niobium.
- the additive is pushed away by the movement of niobium and is positioned so as to surround the periphery of niobium.
- the neck portion is formed so that the surface energy is reduced because the niobium atoms diffuse so as to be low in energy.
- the additive is removed from the neck interface and moves to the periphery of the neck. Since the additive itself also exceeds the diffusion start temperature, it diffuses at the neck portion, resulting in the effect of reinforcing the neck portion of the particles.
- niobium will be agglomerated, so it will be crushed into particles by an appropriate method and the particle size distribution will be adjusted.
- a roll granulator, a pin mill, a speed mill, etc. can be used as a crusher.
- the particle size can be adjusted by using a sieve in combination so as to obtain a granulated product having a required particle size distribution.
- the fragments of the crushed particles become fine particles, and this strongly influences the physical property values related to the dynamic characteristics of the granulated material such as the angle of repose and fluidity, so it is particularly desirable to adjust the particle size on the fine particle side. .
- a pore forming material is used, it is preferably removed at this stage.
- the pore forming material is an inorganic salt, it is removed with an appropriate solvent, and when it is an oxide, it is removed with an appropriate acid, alkali or chelating agent.
- the additive is a titanium compound, it is preferable to use an acid other than hydrochloric acid.
- heat of reaction is generated at the time of removal, and niobium has a high affinity with oxygen, so the surface may be oxidized.
- the dissolution removal temperature is desirably less than 50 ° C., particularly preferably 0 to 30 ° C.
- the excess solvent is washed with water or alcohol.
- the pore-forming material is an organic compound, it is decomposed during heat treatment and already removed from the particles. However, fine particles can be further removed by the washing (water tank) effect of this washing, so it is washed once with an appropriate solvent. It is desirable.
- the solvent is removed from the washed particles with a dryer.
- a general vacuum dryer can be used without limitation.
- the solvent is water
- the drying temperature is desirably less than 50 ° C. until the water has sufficiently evaporated. If water is removed in advance with a water-soluble organic solvent, the drying time is fast.
- the solvent evaporates, the pressure in the dryer decreases, but it is desirable to raise the temperature to 50 ° C. or higher when bumping stops. At this time, if the temperature in the dryer is raised to a nitrogen atmosphere and the temperature is raised, the surface of the alloy particles can be nitrided, which has an effect of preventing oxidation.
- the particles obtained in this way are a niobium granule for a normal capacitor, a molding device using a tantalum granule for a capacitor, a sintering device, a chemical conversion device, an impregnation device, a paste coating device, It can be used without particular limitation in equipment such as a frame mounting device and a sealing device.
- Chemical analysis values (contents of oxygen, tin, and tungsten) of the granulated materials of Examples and Comparative Examples, specific surface area, bulk density, powder binding strength index, electrostatic capacity of chemical compounds of Examples and Comparative Examples, Conditions for the analysis method of leakage current and sintered body strength are as follows.
- Chemical analysis value Metal elements other than oxygen and niobium were quantified with an ICP (Inductively coupled plasma) emission spectrometer after dissolving the sample in hydrofluoric acid.
- Specific surface area (m 2 / g) Measured using a BET surface area measuring device (manufactured by QUANTACHROME).
- Bulk density (g / cm 3 ): Measured using a JIS Z 2504 bulk density meter.
- Powder binding strength index Using a laser diffraction particle size distribution analyzer, the sample was dispersed in pure water, and the particle size distribution of the sample treated with an ultrasonic homogenizer with an output of 200 W for 3 minutes and the sample not treated were measured. The ratio of the area where the shape of the distribution graph of the treated sample overlaps the distribution shape of the untreated sample to the distribution area of the untreated sample was taken as the powder strength index.
- Particle size distribution Measured by a laser diffraction scattering method using HRA9320-X100 manufactured by Microtrack. Average particle diameter (D50): The particle diameter corresponding to 50 volume% of the cumulative volume% of the particle size distribution measured above was defined as the average particle diameter (D50).
- Capacitance ( ⁇ FV / g) was measured using a platinum black electrode with a measurement solution of 30% sulfuric acid and a 120 Hz bias voltage of 1.5 V.
- As the leakage current ( ⁇ A / g) a voltage of formation voltage ⁇ 0.7 was applied, and the current value after 5 minutes was measured.
- Electrical characteristics after heating Assuming a reflow furnace when soldering a capacitor to a substrate, the chemical was heated at 260 ° C. for 20 minutes, and allowed to cool, and then the capacitance and leakage current were measured.
- Sintered body strength (N / mm 2 ): Using a rectangular parallelepiped sintered body element in which the wire of the anode terminal is embedded, the surface parallel to the embedded wire and having a smaller area is placed in the vertical direction. A value obtained by compressing the element using a digital force gauge and buckling fracture was obtained, and a value obtained by dividing the value by the area on the top and bottom of the element was defined as the sintered body strength.
- Example 1 The niobium hydride lump prepared by storing the niobium ingot with hydrogen was pulverized with an impact mill and classified with a gyro shifter using a sieve having an opening of 1 mm. Niobium hydride particles that passed through the sieve were used as raw materials for the following steps. The hydrogen concentration of the niobium hydride particles at this time was 0.95%. A commercially available special grade reagent tin (IV) oxide was prepared as an additive to be present during the heat treatment. These were mixed and refined at the same time using a bead mill using pure water as a dispersion medium.
- the bead mill setting conditions were zirconia beads having a diameter of 3 mm, a bead filling amount of 80%, and a stirring rotation speed of 25 Hz.
- the raw materials to be treated were blended so that the total amount of niobium was 10 kg and the tin (IV) tin was 1% by mass with respect to niobium, and wet pulverization was performed for 3 hours at a slurry concentration of 50%.
- the average particle diameter after 2 hours was measured with a laser diffraction particle size distribution analyzer, the D50 value was 2.2 ⁇ m.
- the beads were replaced with silicon nitride beads having a diameter of 0.5 mm, and pulverization was continued until the D50 value became 0.5 ⁇ m. After 6 hours, the slurry was recovered when the D50 value reached 0.48 ⁇ m.
- the niobium lump after the heat treatment was gradually oxidized so as not to ignite, and was then crushed to an average particle size of about 100 ⁇ m using a roll granulator. Further, the crushed powder was washed with nitric acid, and the magnesium oxide remaining in the particles was dissolved and removed to form pores. After the dissolution reaction was completed, the particles were washed with pure water by a gradient method and fine particles dispersed in a water stream were removed, and then the granulated particles of niobium powder were collected. Finally, the granulated particles were transferred to a container and dried under reduced pressure at 50 ° C., followed by finishing drying at 250 ° C. to obtain a granulated sample.
- Example 2 In Example 1, a granulated material sample was obtained in the same procedure as in Example 1 except that the maximum heat treatment temperature was 1060 ° C.
- Example 1 In Example 1, a granulated material sample was obtained in the same procedure as in Example 1 except that the maximum heat treatment temperature was 900 ° C.
- Example 3 A granulated sample was obtained in the same procedure as in Example 1 except that a commercially available special grade reagent tungsten (VI) was used in place of the tin (IV) oxide in Example 1.
- Example 4 In Example 3, a granulated material sample was obtained in the same procedure as in Example 1 except that the maximum heat treatment temperature was 1060 ° C.
- Example 3 In Example 3, a granulated material sample was obtained in the same procedure as in Example 3 except that the maximum heat treatment temperature was 1140 ° C.
- Example 3 In Example 3, a granulated material sample was obtained in the same procedure as in Example 3 except that the maximum heat treatment temperature was 1020 ° C.
- Example 4 In Example 1, the same process was followed using only niobium hydride particles without using additives, and a granulated product was obtained.
- Comparative Example 5 In Comparative Example 1, a granule sample was obtained in the same procedure as in Comparative Example 4 except that the maximum heat treatment temperature was 1060 ° C.
- Example 6 In Example 1, a granulated material sample was obtained in the same procedure as in Example 1 except that a commercially available reagent, tungsten (IV) oxide, was used. Table 1 shows the physical property values of the samples of Examples 1 to 4 and Comparative Examples 1 to 6.
- the sample containing tin and tungsten has a concentration of about 60% to 80% of the initial input amount concentration (1% by mass). This is due to a decrease during the process such as dropping during mixing and heat treatment.
- the specific surface area (m 2 / g) correlates with the maximum temperature (Tmax) of the heat treatment, and the specific surface area increases as the temperature decreases.
- the powder binding strength index correlates with the presence or absence of additives, and the index of the one using tungsten (VI) is kept at a large value.
- tungsten oxide (IV) (Td: 1220 ° C) sublimates and decomposes during heat treatment to produce tungsten oxide (VI).
- tungsten oxide (VI) is used from the beginning because it is dispersed from the vicinity of niobium.
- the powder binding strength is not significantly increased.
- Tmax maximum temperature
- Td diffusion start temperature
- the body binding strength index is low.
- Example 5 The sample obtained in Example 1 was mixed with 3% by mass of camphor, and a niobium compact was produced using an automatic element molding machine. The element was adjusted so that a niobium wire was planted in the center, the volume was about 20 mm 3 , and the molded body density was about 3.0 g / cm 3 . This element was placed in a vacuum sintering furnace and maintained at a maximum temperature of 1200 ° C. for 30 minutes at a vacuum of 10 ⁇ 3 Pa or less to produce a sintered body. This sintered body was used as an anode, and a 1% by mass 90 ° C.
- phosphoric acid aqueous solution was used as an electrolyte, and anodization was performed at 20 V at a current density of 200 mA / g. After the voltage reached 20 V, the voltage was maintained at a constant voltage for 3 hours. A chemical was produced. This chemical was washed with running water, dried and subjected to various tests. Further, this chemical was cut, observed with a TEM (Transmission Electron Microscope), and subjected to elemental analysis by EDX (Energy Dispersive X-ray spectrometry).
- Example 5 a chemical was prepared in the same manner as in Example 5 except that the granulated product obtained in Examples 2 to 4 was used as a sample, and subjected to various tests. In addition, about Example 7, the obtained chemical compound was cut
- Comparative Examples 7-12 In Example 5, a chemical was produced in the same manner as in Example 5 except that the granulated product obtained in Comparative Examples 1 to 6 was used as a sample, and subjected to various tests. Table 2 shows the electrical characteristic values of the chemicals of Examples 5 to 8 and Comparative Examples 7 to 12.
- the sample with the highest reached temperature of 1060 ° C. in the heat treatment of the granulated dry mass has a larger capacitance than the sample with 1100 ° C. It is worth noting that the capacitance correlates with the specific surface area after the heat treatment, but the behavior of the sintered body strength is changed. Although substantially the same capacitance was obtained under the conditions of the heat treatment temperature of 1100 ° C. in Examples 5 and 7 and Comparative Example 4, the capacitance was obtained under the conditions of the heat treatment temperature of 1060 ° C. in Examples 6 and 8 and Comparative Example 5. The behavior of the strength of the sintered body has changed significantly.
- the sintered body is required to have a strength that can withstand the pressure required for resin sealing of the product at the time of producing the capacitor, but the excessive strength of the sintered body here is wasted.
- the elements of Examples 6 and 8 can be heat-treated and sintered at a lower temperature, thereby exhibiting the effect of relatively increasing the specific surface area and the capacitance.
- the strength of the sintered body increases, but the leakage current increases. Judging from this is not preferable.
- the maximum temperature reached is higher as in Comparative Example 8, only the capacitance is reduced and the effect of the additive is not manifested.
- the element of Comparative Example 12 has a smaller sintered body strength than the element of Example 7. This also shows that it is preferable to use tungsten oxide (VI) rather than tungsten oxide (IV).
- Example 9 Except for setting the sintering temperature of the sintered body to 1170 ° C., a chemical compound was produced in the same process as in Example 8, and subjected to various tests. Table 3 shows the electrical property values of this chemical.
- the results in Table 3 are the results of the electrical properties of the chemicals with the sintered body strength set to about 98 (N / mm 2 ). While satisfying the sintered body strength, an element with a larger capacitance can be easily obtained. Can be made. In this example, the capacitance is increased by 4% just by lowering the sintering temperature, but a further increase can be expected by adjusting other setting conditions.
- FIGS. 1 to 4 and FIGS. 5 to 8 are observations of the chemical products of Example 5 (using the granulated product of Example 1) and Example 7 (using the granulated product of Example 3), 1 and FIG. 5 are transmission electron microscope (TEM) photographs ( ⁇ 200,000 times) of the cross section of the chemical conversion element of Example 1 and Example 5, respectively, and FIGS. 2 to 4 are cross sections of the chemical conversion element of Example 5.
- FIGS. 6 to 8 are photographs ( ⁇ 200,000 times) showing distributions of Nb k ⁇ ray, Sn L ⁇ ray and O k ⁇ ray, respectively, by energy dispersive X-ray analysis (EDX).
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Abstract
Description
例えば、特表2000-500826号公報(US6126712)(特許文献1)には、金属コバルトの酸化物または塩を、結合剤、溶剤などの存在下で造粒し、これを水素還元した金属粉末造粒が開示されているが、造粒操作に用いた溶剤や結合剤は水素による還元時に完全に除去されており、添付写真からもコンデンサ用金属粉末のようなポーラスな形状を有するものではない。
しかしながら、これら先行技術には、ニオブ粉造粒物の結着強度の問題や樹脂封止の条件下での焼結多孔質体の損傷、漏れ電流の増大によるコンデンサ性能の悪化の改善につながるヒントとなるような技術は記載されていない。
[1] 水素化ニオブとニオブ以外の金属元素を含む化合物とを混合して混合物とし、前記ニオブ以外の金属元素を含む化合物の拡散開始温度よりも高い温度で熱処理することを特徴とするニオブ造粒物の製造方法。
[2] 前記熱処理温度が1100℃以下である前項1に記載のニオブ造粒物の製造方法。
[3] 前記ニオブ以外の金属元素を含む化合物が金属酸化物である前項1に記載のニオブ造粒物の製造方法。
[4] 前記金属酸化物が弁作用金属酸化物である前項3に記載のニオブ造粒物の製造方法。
[5] 前記弁作用金属酸化物が五酸化タンタル、酸化スズ(IV)、酸化タングステン(VI)である前項4に記載のニオブ造粒物の製造方法。
[6] 前記ニオブ以外の金属元素を含む化合物が金属の無機塩である前項1に記載のニオブ造粒物の製造方法。
[7] 前記金属の無機塩が塩化リチウム、塩化セシウム、窒化カルシウム、テルル化亜鉛、二リン酸カルシウムである前項6に記載のニオブ造粒物の製造方法。
[8] 前記ニオブ以外の金属元素を含む化合物の一部を熱処理後に除去する前項1~7のいずれかに記載のニオブ造粒物の製造方法。
[9] 前項1~8のいずれかに記載の方法でニオブ造粒物を得、該造粒物を焼結することを特徴とする焼結体強度98N/mm2以上の焼結体の製造方法。
[10] 前項9に記載の方法で焼結体を得、該焼結体を電解酸化して表面に誘電体層を形成することを特徴とするコンデンサの化成体の製造方法。
[11] 前項10に記載の方法で化成体を得、該化成体表面の誘電体層上に陰極形成することを特徴とするコンデンサの製造方法。
[12] ニオブ造粒物を焼結して焼結体を得、該焼結体を電解酸化して化成体を得、該化成体表面の誘電体層上に陰極形成するコンデンサの製造方法であって、前項1~8のいずれかに記載の方法でニオブ造粒物を得、コンデンサの製造工程上必要な最低限の焼結体強度となる温度にて焼結することを特徴とするコンデンサの製造方法。
[13] ニオブ造粒物を焼結して焼結体を得、該焼結体を電解酸化して化成体を得、該化成体表面の誘電体層上に陰極を形成するコンデンサの製造方法であって、前項1~8のいずれかに記載の方法でニオブ造粒物を得、コンデンサの製造工程上必要な最低限の焼結体強度となるように、前記造粒物を得る工程で熱処理温度を調整することを特徴とするコンデンサの製造方法。
[14] 表面に誘電体層を有し、ニオブとニオブ以外の金属元素を含む化合物からなるコンデンサの陽極の化成体であって、ニオブ以外の金属元素がニオブの周辺を囲むように分布することを特徴とする化成体。
[15] 前記ニオブ以外の金属元素を含む化合物が金属酸化物である前項14に記載の化成体。
[16] 前記金属酸化物が弁作用金属酸化物である前項15に記載の化成体。
[17] 前記弁作用金属酸化物が五酸化タンタル、酸化スズ(IV)、酸化タングステン(VI)である前項16に記載の化成体。
[18] 前項14~17のいずれかに記載の化成体と該化成体表面の誘電体層上に陰極とを有するコンデンサ。
Td=0.757Tm
上記式において、Tdは拡散開始温度(絶対温度)、Tmは圧力1atmのもとで測定した融点(絶対温度)である。
本発明において水素化ニオブに添加するニオブ以外の元素を含む化合物(添加物)は、拡散開始温度が1100℃以下の、ニオブや他の添加物と反応しない物質であり、具体例としては五酸化タンタル(拡散開始温度1045℃)、酸化タングステン(VI)(拡散開始温度1049℃)、酸化スズ(IV)(拡散開始温度919℃)が挙げられる。これらはいずれも酸化物であるが、これら金属の無機塩をも使用することができる。ただし、フッ化物や硫化物については処理温度の範囲に拡散開始温度のあるものが数種見られるだけであり、さらにフッ素や硫黄はその後のコンデンサ特性に影響が出る場合があるので、それら以外の化合物を用いるのが好ましい。また熱処理中に分解するものなどは融着助剤にならないので、熱処理中に分解しない化合物を用いるのが好ましい。
原材料粒子は目開き1mmのふるいを通過したものを使用し、ビーズミルに使用するビーズ直径は0.3~3mm、好ましくは3mmビーズで粗粉砕し、0.5mmビーズで微粉砕を行うことが望ましい。原材料粒子が1mmを越えるとこれを粉砕するためのビーズ直径が大きくなり,ミル内のデッドスペースが増加して粉砕が非効率になる。また粉砕到達度はビーズ直径に依存するので、材料の平均粒径が数μmになったところでビーズを直径が小さいものに交換することが望ましい。
撹拌速度は20~30Hzが好ましい。20Hz未満ではビーズと原材料の衝突速度が小さく粉砕効率が劣り、30Hzを超えると衝突速度が大きすぎて装置自体が損傷する。
粉砕割合は装置の容量にもよるがおおむね0.7~1.3kg/時間(h)が好ましい。装置の容量に対し材料が少ないと短時間で粉砕が進み、希望の平均粒径に至る時点で混合が不十分であり、材料が多いと装置内により長時間材料が留まるため装置由来の不純物成分が増加するので、粉砕割合は上記範囲内とするのが好ましい。
実施例及び比較例の造粒物の化学分析値(酸素、スズ、タングステンの含有量)、比表面積、かさ密度、粉体結着強度指数、実施例及び比較例の化成体の静電容量、漏れ電流、焼結体強度の解析手法の条件は次の通りである。
化学分析値:酸素及びニオブ以外の金属元素は、サンプルをフッ化水素酸に溶解しICP(Inductively coupled plasma;誘導結合プラズマ)発光分光装置で定量した。
比表面積(m2/g):BET式表面積測定器(QUANTACHROME社製)を使用して測定した。
かさ密度(g/cm3):JIS Z 2504かさ密度測定器を使用して測定した。
粒度分布:マイクロトラック社製HRA9320-X100を用いたレーザー回折散乱法で測定した。
平均粒径(D50):前記で測定した粒度分布の累積体積%が50体積%に相当する粒子径を平均粒径(D50)とした。
加熱後の電気特性:コンデンサを基板に半田付けする際のリフロー炉を想定し、化成体を260℃で20分加熱し、放冷後に静電容量と漏れ電流を測定した。
焼結体強度(N/mm2):陽極端子のワイヤーを埋め込んだ直方体型の焼結体素子を用いて、埋め込みワイヤーと並行でかつ面積が小さい方の面を天地方向に置き、株式会社イマダ製デジタルフォースゲージを用いて素子を圧縮し座屈破壊するときの値を求め、それを素子の天地側の面積で除した値を焼結体強度とした。
ニオブインゴットを水素吸蔵させて調製した水素化ニオブ塊をインパクトミルにて粉砕し、目開き1mmの篩を用いてジャイロシフターにて分級した。ふるいを通過した水素化ニオブ粒子を原材料とし以下の工程に使用した。このときの水素化ニオブ粒子の水素濃度は0.95%であった。
熱処理時に存在させる添加物として市販の特級試薬の酸化スズ(IV)を準備した。
これらを、純水を分散媒とし、ビーズミルを用いて混合と微細化を同時に行った。ビーズミル設定条件は直径3mmのジルコニアビーズを使用しビーズ充填量80%、撹拌回転数25Hzとした。処理する原材料はニオブ純分として総量が10kg、酸化スズ(IV)のスズがニオブに対して1質量%になるように配合し、スラリー濃度50%の設定で3時間湿式粉砕を行った。2時間後の平均粒径をレーザー回折式粒度分布計で測定するとD50値で2.2μmであった。次にビーズ直径を0.5mmの窒化珪素ビーズに交換し、D50値が0.5μmになるまで続けて粉砕を実施した。6時間後D50値が0.48μmになったところでスラリーを回収した。
さらにこの解砕粉は硝酸を用いて洗浄し、粒子内に残留する酸化マグネシウムを溶解除去して空孔を形成させた。溶解反応が終了した後、純水を用いて傾斜法により水洗するとともに水流で分散する微細な粒子を除去した後、ニオブ粉の造粒粒子を回収した。最後にこの造粒粒子を容器に移し50℃で減圧乾燥した後に、250℃で仕上げの乾燥を行い造粒物サンプルを得た。
実施例1において、熱処理最高到達温度を1060℃とした以外は実施例1と同様の手順で造粒物サンプルを得た。
実施例1において、熱処理最高到達温度を900℃とした以外は実施例1と同様の手順で造粒物サンプルを得た。
実施例1の酸化スズ(IV)に替えて市販の特級試薬の酸化タングステン(VI)を用いたこと以外は実施例1と同様の手順で造粒物サンプルを得た。
実施例3において、熱処理最高到達温度を1060℃とした以外は実施例1と同様の手順で造粒物サンプルを得た。
実施例3において、熱処理最高到達温度を1140℃とした以外は実施例3と同様の手順で造粒物サンプルを得た。
実施例3において、熱処理最高到達温度を1020℃とした以外は実施例3と同様の手順で造粒物サンプルを得た。
実施例1において、添加物を使用せず、水素化ニオブ粒子のみで同様の工程をたどり、造粒物を得た。
比較例1において、熱処理最高到達温度を1060℃とした以外は比較例4と同様の手順で造粒物サンプルを得た。
実施例1において、添加物を市販試薬の酸化タングステン(IV)を用いたこと以外は実施例1と同様の手順で造粒物サンプルを得た。
これら実施例1~4、比較例1~6のサンプルの物性値を表1に示す。
実施例1で得られたサンプルにカンファを3質量%混合し、自動素子成形機を用いてニオブ成形体を作製した。素子は中央にニオブワイヤを植立し、体積約20mm3、成形体密度が約3.0g/cm3になるよう調整した。この素子は真空焼結炉に入れ10-3Pa以下の真空度で最高温度1200℃で30分保持させ焼結体を作製した。この焼結体を陽極とし、1質量%の90℃りん酸水溶液を電解液とし電流密度200mA/gで20Vにて陽極酸化を行い、電圧が20Vに達してから定電圧で3時間保持して化成体を作製した。この化成体は流水で洗浄後乾燥させ、各種試験に供した。またこの化成体を切断し、TEM(Transmission Electron Microscope;透過型電子顕微鏡)観察し、EDX(Energy Dispersive X-ray spectrometry;エネルギー分散型X線分析)により元素分析を行った。
実施例5において、サンプルに実施例2~4で得られた造粒物を使用した以外は実施例5と同様な工程で化成体を作製し、各種試験に供した。なお、実施例7については得られた化成体を切断し、TEM観察、EDXによる元素分析を行った。
実施例5において、サンプルに比較例1~6で得られた造粒物を使用した以外は実施例5と同様な工程で化成体を作製し、各種試験に供した。
これら実施例5~8、比較例7~12の化成体の電気特性値を表2に示す。
焼結体の焼結温度を1170℃にした以外は実施例8と同様な工程で化成体を作製し、各種試験に供した。この化成体の電気特性値を表3に示す。
図2~4ではスズ元素が、図6~8ではタングステン元素が、ともにニオブの周辺を囲むように分布していることを確認することができる。この観察結果及び表1~3の結果から、ニオブ以外の金属元素がニオブの周辺を囲むように分布する化成体を使用したコンデンサが優れた電気特性を有することがわかる。
Claims (18)
- 水素化ニオブとニオブ以外の金属元素を含む化合物とを混合して混合物とし、前記ニオブ以外の金属元素を含む化合物の拡散開始温度よりも高い温度で熱処理することを特徴とするニオブ造粒物の製造方法。
- 前記熱処理温度が1100℃以下である請求項1に記載のニオブ造粒物の製造方法。
- 前記ニオブ以外の金属元素を含む化合物が金属酸化物である請求項1に記載のニオブ造粒物の製造方法。
- 前記金属酸化物が弁作用金属酸化物である請求項3に記載のニオブ造粒物の製造方法。
- 前記弁作用金属酸化物が五酸化タンタル、酸化スズ(IV)、酸化タングステン(VI)である請求項4に記載のニオブ造粒物の製造方法。
- 前記ニオブ以外の金属元素を含む化合物が金属の無機塩である請求項1に記載のニオブ造粒物の製造方法。
- 前記金属の無機塩が塩化リチウム、塩化セシウム、窒化カルシウム、テルル化亜鉛、二リン酸カルシウムである請求項6に記載のニオブ造粒物の製造方法。
- 前記ニオブ以外の金属元素を含む化合物の一部を熱処理後に除去する請求項1~7のいずれかに記載のニオブ造粒物の製造方法。
- 請求項1~8のいずれかに記載の方法でニオブ造粒物を得、該造粒物を焼結することを特徴とする焼結体強度98N/mm2以上の焼結体の製造方法。
- 請求項9に記載の方法で焼結体を得、該焼結体を電解酸化して表面に誘電体層を形成することを特徴とするコンデンサの化成体の製造方法。
- 請求項10に記載の方法で化成体を得、該化成体表面の誘電体層上に陰極形成することを特徴とするコンデンサの製造方法。
- ニオブ造粒物を焼結して焼結体を得、該焼結体を電解酸化して化成体を得、該化成体表面の誘電体層上に陰極形成するコンデンサの製造方法であって、請求項1~8のいずれかに記載の方法でニオブ造粒物を得、コンデンサの製造工程上必要な最低限の焼結体強度となる温度にて焼結することを特徴とするコンデンサの製造方法。
- ニオブ造粒物を焼結して焼結体を得、該焼結体を電解酸化して化成体を得、該化成体表面の誘電体層上に陰極を形成するコンデンサの製造方法であって、請求項1~8のいずれかに記載の方法でニオブ造粒物を得、コンデンサの製造工程上必要な最低限の焼結体強度となるように、前記造粒物を得る工程で熱処理温度を調整することを特徴とするコンデンサの製造方法。
- 表面に誘電体層を有し、ニオブとニオブ以外の金属元素を含む化合物からなるコンデンサの陽極の化成体であって、ニオブ以外の金属元素がニオブの周辺を囲むように分布することを特徴とする化成体。
- 前記ニオブ以外の金属元素を含む化合物が金属酸化物である請求項14に記載の化成体。
- 前記金属酸化物が弁作用金属酸化物である請求項15に記載の化成体。
- 前記弁作用金属酸化物が五酸化タンタル、酸化スズ(IV)、酸化タングステン(VI)である請求項16に記載の化成体。
- 請求項14~17のいずれかに記載の化成体と該化成体表面の誘電体層上に陰極とを有するコンデンサ。
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| EP13867356.1A EP2939760A4 (en) | 2012-12-27 | 2013-12-26 | CHEMICAL CONVERSION BODY FOR POSITIVE ELECTRODE OF AN NIOBIUM CONDENSATE AND METHOD OF MANUFACTURING THEREOF |
| US14/655,886 US20150352637A1 (en) | 2012-12-27 | 2013-12-26 | Chemical conversion body for niobium capacitor positive electrode, and production method therefor |
| JP2014554537A JP6258222B2 (ja) | 2012-12-27 | 2013-12-26 | ニオブコンデンサ陽極用化成体及びその製造方法 |
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| JP2012-284216 | 2012-12-27 | ||
| JP2012284216 | 2012-12-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2014104177A1 true WO2014104177A1 (ja) | 2014-07-03 |
Family
ID=51021251
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2013/084849 Ceased WO2014104177A1 (ja) | 2012-12-27 | 2013-12-26 | ニオブコンデンサ陽極用化成体及びその製造方法 |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20150352637A1 (ja) |
| EP (1) | EP2939760A4 (ja) |
| JP (1) | JP6258222B2 (ja) |
| TW (1) | TW201446360A (ja) |
| WO (1) | WO2014104177A1 (ja) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10103831B2 (en) | 2015-04-29 | 2018-10-16 | Lg Electronics Inc. | Method for transmitting and receiving signal in wireless communication system and apparatus for performing same |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3767691A1 (en) * | 2019-07-18 | 2021-01-20 | NV Bekaert SA | Magnesiumdiboride powder-in-tube wire |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4825859A (ja) | 1971-08-09 | 1973-04-04 | ||
| JP2000500826A (ja) | 1995-11-27 | 2000-01-25 | エイチ・シー・スタルク・ゲゼルシヤフト・ミツト・ベシユレンクテル・ハフツング・ウント・コンパニー・コマンジツトゲゼルシヤフト | 金属粉末造粒物、その製造方法及びその使用 |
| JP2001303106A (ja) | 2000-04-26 | 2001-10-31 | Sanalloy Industry Co Ltd | 多孔性焼結成形体の製造方法 |
| WO2002015208A1 (en) * | 2000-08-10 | 2002-02-21 | Showa Denko K.K. | Niobium powder, sinter thereof, and capacitor employing the same |
| JP2006179886A (ja) * | 2004-11-29 | 2006-07-06 | Showa Denko Kk | 固体電解コンデンサ用多孔質陽極体、その製造方法、及び固体電解コンデンサ |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7713466B2 (en) * | 2003-04-28 | 2010-05-11 | Showa Denko K.K. | Valve acting metal sintered body, production method therefor and solid electrolytic capacitor |
| JP4727160B2 (ja) * | 2003-04-28 | 2011-07-20 | 昭和電工株式会社 | 弁作用金属焼結体、その製造方法及び固体電解コンデンサ |
| ATE482042T1 (de) * | 2004-10-06 | 2010-10-15 | Showa Denko Kk | Niobpulver, niobgranulat, niobsinterkörper und kondensator und herstellungsverfahren dafür |
-
2013
- 2013-12-26 US US14/655,886 patent/US20150352637A1/en not_active Abandoned
- 2013-12-26 WO PCT/JP2013/084849 patent/WO2014104177A1/ja not_active Ceased
- 2013-12-26 TW TW102148466A patent/TW201446360A/zh unknown
- 2013-12-26 EP EP13867356.1A patent/EP2939760A4/en not_active Withdrawn
- 2013-12-26 JP JP2014554537A patent/JP6258222B2/ja not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4825859A (ja) | 1971-08-09 | 1973-04-04 | ||
| JP2000500826A (ja) | 1995-11-27 | 2000-01-25 | エイチ・シー・スタルク・ゲゼルシヤフト・ミツト・ベシユレンクテル・ハフツング・ウント・コンパニー・コマンジツトゲゼルシヤフト | 金属粉末造粒物、その製造方法及びその使用 |
| US6126712A (en) | 1995-11-27 | 2000-10-03 | H. C. Starck Gmbh & Co. Kg | Metal powder granulates, method for their production and use of the same |
| JP2001303106A (ja) | 2000-04-26 | 2001-10-31 | Sanalloy Industry Co Ltd | 多孔性焼結成形体の製造方法 |
| WO2002015208A1 (en) * | 2000-08-10 | 2002-02-21 | Showa Denko K.K. | Niobium powder, sinter thereof, and capacitor employing the same |
| JP2006179886A (ja) * | 2004-11-29 | 2006-07-06 | Showa Denko Kk | 固体電解コンデンサ用多孔質陽極体、その製造方法、及び固体電解コンデンサ |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP2939760A4 |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10103831B2 (en) | 2015-04-29 | 2018-10-16 | Lg Electronics Inc. | Method for transmitting and receiving signal in wireless communication system and apparatus for performing same |
Also Published As
| Publication number | Publication date |
|---|---|
| US20150352637A1 (en) | 2015-12-10 |
| EP2939760A4 (en) | 2016-09-14 |
| JPWO2014104177A1 (ja) | 2017-01-12 |
| JP6258222B2 (ja) | 2018-01-10 |
| TW201446360A (zh) | 2014-12-16 |
| EP2939760A1 (en) | 2015-11-04 |
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