WO2006064979A1 - アルカリ二次電池用ニッケル電極及びその製造方法並びにアルカリ二次電池 - Google Patents
アルカリ二次電池用ニッケル電極及びその製造方法並びにアルカリ二次電池 Download PDFInfo
- Publication number
- WO2006064979A1 WO2006064979A1 PCT/JP2005/023689 JP2005023689W WO2006064979A1 WO 2006064979 A1 WO2006064979 A1 WO 2006064979A1 JP 2005023689 W JP2005023689 W JP 2005023689W WO 2006064979 A1 WO2006064979 A1 WO 2006064979A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- nickel
- particles
- active material
- electrode
- hydroxide
- Prior art date
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/32—Nickel oxide or hydroxide electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0404—Methods of deposition of the material by coating on electrode collectors
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/049—Manufacturing of an active layer by chemical means
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
- H01M4/366—Composites as layered products
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/381—Alkaline or alkaline earth metals elements
- H01M4/382—Lithium
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present invention relates to a nickel electrode for an Al force secondary battery, a manufacturing method thereof, and an Al force secondary battery having the nickel electrode as a positive electrode. More specifically, the present invention relates to a discharge capacity as compared with a conventional product. The present invention relates to a nickel electrode, a manufacturing method thereof, and an Al force secondary battery for realizing an Al force secondary battery having a large charge and discharge cycle characteristic. Background art
- the active material of the nickel electrode is, for example, a high-density nickel hydroxide ⁇ Ni (OH) 2 ⁇ powder deposited via an ammine complex salt, in which zinc (Zn) is dissolved in nickel hydroxide.
- ⁇ -NiOOH the production of ⁇ -NiOOH is suppressed, and further, the cobalt (C o) is dissolved to suppress the generation of oxygen at the nickel electrode during charging.
- the active material particles are mixed with a conductive material such as carbon powder or metal powder, and the mixture
- the current collecting function of the electrode plate is secured by supporting the electrode on the substrate.
- the active material filling density is increased and the current collecting function is secured.
- a method is used in which a conductive network composed of higher-order cobalt compounds is formed in an aggregate of active material particles composed of OH (OH) 2 and higher-order nickel compounds supported on a substrate. .
- the conductive network made of the higher cobalt compound is made of nickel hydroxide.
- Cobalt compounds with a cobalt oxidization number such as cobalt monoxide or Co (OH) 2 such as cobalt ⁇ j powder are added to the active material powder, or core layer particles containing Ni (OH) 2 as the main component
- a cobalt hydroxide layer is formed on the surface, and an alkaline secondary battery is assembled using a nickel electrode plate filled with the active material powder. Then, by charging, the oxidation number of Co is +2. It can be formed by oxidizing a cobalt compound to produce a higher order cobalt compound which is a good conductor.
- this method has a drawback in that the discharge reserve generation amount increases and the discharge capacity of the battery decreases.
- a layer of Co (OH) 2 is formed on the surface of the core layer particle mainly composed of nickel hydroxide, and the active material powder is used in the presence of an aqueous alkaline solution. Oxidize with an oxidant and change the cobalt compound in the surface layer to a highly conductive higher-order cobalt compound or oxidize part of the Ni (OH) 2 in the core layer before being incorporated into the battery. Therefore, a method for making the oxidation number of Ni larger than +2 has been proposed. According to this method, the amount of discharge reserve generation can be reduced, but the capacity of the nickel electrode itself and the charging efficiency cannot be increased.
- a method for modifying a nickel electrode active material (hereinafter also simply referred to as an active material), a method of adding an alkali metal to the active material has been proposed, and an example in which the alkali metal is Li is also shown.
- the addition of an alkaline solution containing Li + to an active material containing Zn or the like in a solid solution state and heating can suppress the decrease in capacity when overdischarged.
- a mixed solution of Na OH and Li OH is added to a mixed powder of nickel hydroxide powder in which 2 mol% of zinc is dissolved and Co (OH) 2 powder.
- An example of heat treatment with C is shown. (For example, see Patent Document 1)
- Patent Document 1 Japanese Patent Application Laid-Open No. 8-148146 (page 4, paragraph 0029, page 6, paragraph 0044)
- a nickel-metal hydride storage battery including a positive electrode made of nickel hydroxide in which at least one transition metal and at least one alkali metal are dissolved is proposed.
- the preferable amount of the solid solution is 2 to 10 atomic% (atm%) for the transition metal and 5 to 10 atm% for the Al force metal with respect to Ni of Ni (OH) 2 . (For example, see Patent Document 2).
- Patent Document 2 JP-A-10-289715 (Page 3, Paragraph 001 7) According to the method described in Patent Document 2, the oxidation number of Ni contained in the active material can be charged to a high value. Although the capacity density can be improved, there is a drawback that the charge / discharge cycle performance is not sufficient.
- An active material for an alkaline storage battery containing Ni (OH) as a main component comprising a nickel hydroxide whose Ni valence is higher than divalent, and a nickel hydroxide on the surface of the nickel hydroxide.
- Ni (OH) Ni
- a positive electrode active material comprising a higher order cobalt compound containing one allylic cation, wherein the dihydric hydroxide higher than the divalent valence contains a second allylic thione.
- Patent Document 3 JP 2000-223 1 19 (page 5, paragraphs 0026 to 00 27)
- the nickel hydroxide compound includes a type containing about 0.2 wt% sodium ion, and the nickel hydroxide compound contains a type containing about 0.7 wt% lithium ion. ing.
- the conductivity is improved, there is a possibility that the charge / discharge cycle characteristics may be inferior due to the excess of lithium ions contained in the active material. Only those containing sodium ions are shown, not those containing lithium ions.
- Patent Document 4 Japanese Patent Application Laid-Open No. 2 00 2- 1 1 0 1 5 4 (Page 5, paragraph 0 0 3 2) According to the method described in Patent Document 4, the utilization rate of the active material is not improved. However, according to this method, since the Li content ratio of the nickel electrode active material is not controlled, it is easy to fall into overcharge even during normal charging, and the charge / discharge cycle is similar to Patent Document 3. There is a possibility that the characteristics are inferior.
- lithium ions can be obtained by containing a lithium compound composed of a strong acid and a strong base salt or a weak acid and a strong base salt in the active material. Is incorporated into the crystal lattice of nickel hydroxide, increasing the number of lattice defects, facilitating the movement of electrons, improving the conductivity, and suppressing the generation of T 1 N i OOH, which has poor charge-discharge reversibility, and The utilization rate is expected to improve. (For example, see Patent Document 5)
- Patent Document 5 Japanese Patent Application Laid-Open No. 2 00 1-6 6 7 9 (page 3, paragraph 0 0 1 4)
- the present invention has been made in order to solve the above-mentioned problems, and has a high discharge capacity, a small irreversible capacity, and has a high cycle capacity, high rate discharge characteristics, and excellent charging efficiency.
- Li dissolved in the active material refers to Li that does not elute from the active material even when the active material particles are washed with water.
- the amount of Li solid solution means that 100 parts by weight of active material particles are dispersed in 350 to 400 parts by weight of pure water at room temperature (5 to 30 ° C), and the supernatant liquid is obtained by a decantation method. This is the amount of Li contained in the active material particles after repeated washing until the pH of the liquid becomes 11.5 or less.
- the active material for a nickel electrode according to the present invention comprises contacting the particles mainly composed of higher-order nickel hydroxide having an oxidation number of Ni greater than +2 with a LiOH aqueous solution. An active material having a Li holding function in which Li is contained in substance particles and Li does not elute even when washed with water can be obtained.
- Li can be contained in the active material particles in a short time. It has been found that it is contained, and the present invention has been achieved. Further, the present inventors have found that an aqueous solution of at least one compound of lithium carbonate, sulfate, nitrate, phosphate, halide, and acetate can be applied instead of the LiOH solution. It was. According to the present invention, the above-described problem can be solved by adopting the following configuration.
- a nickel electrode for an Al force secondary battery in which active material particles comprising composite particles provided with a surface layer mainly composed of a higher-order cobalt compound having a main component of more than +2 are supported on a conductive substrate, the active material particles
- a nickel electrode for an alkaline secondary battery characterized in that lithium (L i) is dissolved in an amount of 0.01 to 0.5 wt% as a simple substance.
- the active material particles are selected from the group of elements of holmium (Ho), erbium (E r), thulium (Tm), ytterbium (Yb), and lutetium (Lu)
- Ho holmium
- E r erbium
- Tm thulium
- Yb ytterbium
- Lu lutetium
- active material particles according to any one of (1) to (3), wherein the active material particles contain at least one element selected from calcium (Ca) and magnesium (Mg) Nickel electrode for alkaline secondary battery.
- It contains the above-mentioned active material, and contains a natural polysaccharide consisting of glucose, mannose, and glucuronic acid, or a natural polysaccharide consisting of glucose, mannose, rhamnose, and dalc sulfonic acid.
- the nickel electrode for alkaline secondary batteries according to any one of (1) to (4).
- Oxidation number of cobalt on the surface of particles mainly composed of higher-order nickel hydroxide whose nickel oxidation number exceeds +2 or core layer particles mainly composed of the higher-order nickel hydroxide Lithium (L i) is dissolved in the particles or the composite particles by bringing the composite particles provided with a surface layer mainly composed of a higher-order cobalt compound with a primary component exceeding +2 into contact with a lithium hydroxide aqueous solution.
- the particles provided with the surface layer are oxidized with an oxidizing agent or electrolytically oxidized to produce particles having the higher order nickel hydroxide as a main component or the composite particles, and this is hydroxylated.
- the particles provided with a surface layer mainly composed of a secondary cobalt compound are oxidized using an oxidizing agent, or lithium hydroxide is contained in a reaction bath for oxidation by electrolytic oxidation, whereby The method for producing a nickel electrode for an alkaline secondary battery according to any one of 1 to 5 above, wherein oxidation and impregnation of lithium into the particles are performed in one step.
- a surface layer mainly composed of a higher-order cobalt compound is provided on the surface of the particles mainly composed of the higher-order nickel hydroxide or the core layer particles mainly composed of the higher-order nickel hydroxide.
- a surface layer mainly composed of a higher-order cobalt compound is formed on the surface of the particles mainly composed of the higher-order nickel hydroxide or the core layer particles mainly composed of higher-order nickel hydroxide.
- the composite particles provided and a paste containing an aqueous solution of at least one of lithium carbonate, sulfate, nitrate, phosphate, halide and acetate are supported on a conductive substrate.
- the method for producing a nickel electrode for an alkaline secondary battery according to any one of (1) to (5).
- a surface layer mainly composed of a higher-order cobalt compound is formed on the surface of the particles mainly composed of higher-order nickel hydroxide or the core layer particles mainly composed of higher-order nickel hydroxide.
- a surface layer mainly composed of a higher-order cobalt compound is formed on the surface of the particles mainly composed of the higher-order nickel hydroxide or the core layer particles mainly composed of the higher-order nickel hydroxide.
- the provided composite particles are supported on a conductive substrate to form an electrode plate, at least one compound of lithium carbonate, sulfate, nitrate, phosphate, halide and acetate is formed on the electrode plate.
- An alkaline secondary battery comprising the -eckel electrode for an alkaline secondary battery according to any one of (1) to (5) above.
- the content (wt%) of the lithium metal in the active material particles in the above (1) is obtained by dividing the weight of the lithium metal by the total weight of the higher order nickel hydroxide, the higher order cobalt compound and the lithium metal. It is a value calculated by multiplying 1 0 0, and the value of the denominator of this division does not include the weight of the binder.
- the denominator value includes the weight of zinc metal.
- the content (wt%) of zinc metal in the active material particles is calculated by dividing the weight of zinc metal by the total weight of higher-order nickel hydroxide, higher-order cobalt compound, lithium metal and zinc metal. This is a value calculated by multiplying by 0.
- the denominator value in this division does not include the weight of the binder.
- the weight of the rare earth element compound is not included in the denominator of the division as in the case of the binder.
- calcium and magnesium are included in the above denominator.
- the configuration (1) it is possible to obtain a nickel electrode for an Al force linear battery having a large discharge capacity, a small irreversible capacity, and excellent in high rate discharge characteristics and charge / discharge cycle characteristics.
- the active material composite particles for nickel electrode of (6) can be efficiently synthesized.
- the Li which does not elute even when washed with water. It is possible to efficiently produce a nickel electrode provided with active material composite particles for a nickel electrode that contain. .
- the Li salt aqueous solution is impregnated instead of the Li OH aqueous solution. It is possible to suppress the plate from absorbing moisture and absorbing carbon dioxide contained in the atmosphere.
- FIG. 1 is a graph showing the relationship (Table 1) between the discharge capacity when the nickel electrode evaluation cell is charged at an ambient temperature of 20 ° C. and the lithium content of the nickel electrode active material particles.
- Fig. 2 is a graph showing the relationship between the discharge capacity when the nickel electrode evaluation cell is charged at a temperature of 60 ° C and the lithium content of the nickel electrode active material particles (Table 1).
- Fig. 3 is a graph showing the relationship (Table 2) between the discharge capacity and the lithium content of the nickel electrode active material particles when a cylindrical nickel hydride secondary battery is charged at an ambient temperature of 20 ° C. .
- Fig. 4 is a graph showing the relationship between the discharge capacity and the lithium content of the nickel electrode active material particles when the cylindrical nickel hydride secondary battery is charged at an ambient temperature of 60 ° C (Table 2). .
- FIG. 5 is a graph showing the relationship between the charge / discharge cycle life of the cylindrical nickel hydride secondary battery and the lithium content in the nickel electrode active material particles (Table 2).
- Figure 6 shows the discharge capacity of the nickel electrode evaluation cell and the recharged nickel electrode active material particles. It is a graph which shows the relationship (Table 3) with the content ratio of thium.
- FIG. 7 is a graph showing the relationship (Table 3) between the irreversible capacity of the nickel electrode evaluation cell and the lithium content ratio of the active material particles for the nickel electrode.
- Figure 8 is a graph showing the relationship (Table 4) between the cycle life of a cylindrical nickel-hydrogen battery and the lithium content of nickel electrode active material particles.
- FIG. 9 is a powder X-ray diffraction diagram of the modified ytterbium compound and ytterbium oxide contained in the nickel electrode of the alkaline secondary battery according to the present invention and ytterbium oxide.
- FIG. 10 is a graph showing a change in viscosity with time when the nickel electrode active material paste according to the present invention was left at an ambient temperature of 20 ° C.
- FIG. 10 is a graph showing a change in viscosity with time when the nickel electrode active material paste according to the present invention was left at an ambient temperature of 20 ° C.
- the higher order nickel hydroxide having an oxidation number of Ni greater than +2 in the present invention is a compound obtained by oxidizing nickel hydroxide using an oxidizing agent or electrolytically oxidizing it in an alkaline electrolyte. It is.
- the oxidation number of Ni varies with charge / discharge of the battery.
- the oxidation number of Ni here refers to the nickel electrode active material particles before the nickel electrode is incorporated into the battery. It is a value in the process of dissolving Li in the solution.
- the oxidation number of Ni is preferably greater than +2 and not more than +2.4, preferably +2.02 to 2.4, and 2.05 to 2.2. More preferably.
- the oxidation number of Ni is preferably 2.18 or less.
- the oxidation value of Ni When the oxidation value of Ni is not more than +2.0, it is difficult to dissolve Li in nickel hydroxide, and the discharge reserve amount may be increased. If the oxidation number of Ni exceeds 2.4, the battery capacity is limited by the negative electrode, which may reduce the discharge capacity. Such deterioration of the negative electrode characteristics is hardly observed when the oxidation number of Ni is 2.18 or less. Therefore, by setting the oxidation number of Ni to 2.18 or less, the deterioration of the negative electrode characteristics due to the reduction of the discharge reserve is almost eliminated, so that a battery having a large discharge capacity can be obtained.
- the nickel electrode active material particles preferably contain the higher-order nickel hydroxide as a main component, and contain a small amount of Z ⁇ and C o in a solid solution state in the nickel hydroxide hydroxide.
- ⁇ Addition of ⁇ exerts the effect of suppressing the generation of inactive y—N i OOH as an active material, and addition of Co shifts the charging potential of the nickel battery in a base direction, and improves the charging efficiency. Demonstrate the effect of increasing.
- the content ratio of Zn in the higher order nickel hydroxide is preferably:! To 6 wt%.
- the ratio is less than 1 wt%, the effect of Zn addition is not exhibited, and if it exceeds 6 wt%, the capacity of the active material (mAh / g) may be reduced.
- the content ratio of Co is preferably 0.1 to 5 wt%. When the ratio is less than ⁇ .lwt%, the effect of Co addition is not exhibited, and when it exceeds 5 wt%, the capacity of the active material (mA h / g) may be reduced.
- the nickel electrode active material particles are preferably composite particles composed of a core layer made of the higher-order hydroxide-packet and a surface layer made of a higher-order cobanoleto compound.
- the higher cobalt compound is a good conductor with an oxidation number of Co in the compound of approximately +3, and exhibits the effect of enhancing the current collecting function of the nickel electrode.
- the ratio of the high-order cold compound constituting the surface layer in the nickel electrode active material particles is 3 to 1 Owt%. When the ratio is less than 3 wt%, the effect of forming the surface layer is small, and when it exceeds 10 wt%, the active material capacity (mAh / g) may be small.
- the higher-order cobalt compound forming the surface layer preferably contains Li.
- the Li-containing high-order cobalt compound is superior in reduction resistance compared to conventional Li-containing high-order cobalt compounds, and is stably present without being reduced even after deep discharge. This is effective for fully extracting the capacity of the active material because it does not lose its electrical properties. Therefore, deep discharge is possible and irreversible capacity can be reduced as compared with the case where a conventional high-order cobalt compound not containing Li is applied. .
- the oxidation number of nickel is calculated according to the following formula (Ni oxidation number calculation formula).
- Oxidation number of Ni (average oxidation number of transition metal elements in the active material particles 1 3 XCo molar ratio) ZNi molar ratio
- Li contained in the active material particles according to the present invention is distributed in the solid solution state in the present invention in the active material particles and does not elute from the particles even after being washed with water. It is presumed that they are not retained in the pores that are open, but are taken into the crystal of the active material particles mainly composed of higher-order nickel hydroxide.
- the content ratio of Li contained in the nickel electrode active material in the present invention is determined by the gradient method (decantation) in which pure water is applied to the active material particles at room temperature. This is the ratio of Li (converted to a simple substance) contained in the active material particles washed with water until the pH is 11.5 or less.
- L i taken into the crystal of higher-order nickel hydroxide has an effect of improving the stability of the crystal of Ni (OH) 2 .
- Ni (OH) 2 the oxidation number of Ni exceeds about +3.1, it becomes unstable and begins to collapse, whereas the nickel electrode according to the present invention is used.
- the active material particles have stable Ni oxidation numbers from +3.2 to 10.3.4.
- the active material particles for nickel electrodes according to the present invention contain 0.01 to 0.5 wt% of Li in the active material particles as a simple substance.
- the content ratio of Li is 0.03 to 0.5 wt%, it is preferable because the discharge capacity of the nickel electrode is large and the irreversible capacity is small, and 0.05 to 0.5 wt%, It is more preferable because it has a large discharge capacity and excellent cycle characteristics, and is more preferably 0.05 to 0.3 wt%.
- the Li content is less than 0.01 wt%, the effect of containing Li cannot be exhibited. On the other hand, if the Li content exceeds 0.5 wt%, the active material utilization rate may decrease due to the low discharge voltage. Also, the generation of —N i OOH, which is prone to overcharging and inactive due to overcharging, is encouraged. Since the amount of oxygen generated by the decomposition of the electrolyte is increased and the corrosion of the hydrogen storage alloy is promoted, the capacity may decrease rapidly when the charge / discharge cycle is repeated.
- Ni a and K do not have the effect of Li is thought to be because the ionic radius of N a K is large and it is difficult to incorporate it into the nickel hydroxide crystal.
- the method for incorporating Li into the nickel electrode active material is not particularly limited, and the methods described below can be applied.
- the element group of Ho, Er, Tm, Yb, and Lu (hereinafter also referred to as heavy rare earth element). It is preferable to contain a rare earth compound containing at least one selected element.
- the compound of heavy rare earth element added to the nickel electrode increases the overvoltage (oxygen overvoltage) of the oxygen generation reaction at the nickel electrode when the battery is charged in an atmosphere up to a high temperature (60 ° C). Widens the difference between the charge potential of the nickel electrode and the oxygen generation potential, and suppresses the electrolytic reaction of the electrolyte due to charge. For this reason, in particular, in a liquid volume-restricted alkaline secondary battery, the Saigle performance can be remarkably improved by applying a nickel electrode containing a heavy rare earth element compound.
- the heavy rare earth element compound In order to incorporate the heavy rare earth element compound into the nickel electrode, it is possible to add easily available heavy rare earth element oxide particles, hydroxide particles, halide particles and post-modified heavy rare earth compound particles to the positive electrode active material particles. Can be obtained. Among these heavy rare earth element compounds, oxides and halides are unstable in an alkaline electrolyte, and in the presence of an alkaline electrolyte, they change to hydroxides. In contrast, heavy rare earth element hydroxides and modified heavy rare earth compounds exist stably in alkaline electrolytes. Therefore, the nickel electrode for an alkaline secondary battery according to the present invention is considered to contain a heavy rare earth element hydroxide or a modified heavy rare earth compound in addition to the positive electrode active material particles. It is considered that hydroxides and modified heavy rare earth compounds increase the oxygen overvoltage of the nickel electrode.
- oxides and hydroxides are oxygen in the nickel electrode. Although the overvoltage is increased, when these compounds coexist with an alkaline electrolyte, the oxide changes to a hydroxide. Also, the hydroxide may change to its hydrate. In the course of these changes, oxides and hydroxides react with the water molecules that make up the electrolyte. Therefore, water may be consumed in a battery incorporating a nickel electrode containing these compounds.
- a compound having an intrinsic diffraction peak at 76 nm acts to increase the oxygen overvoltage of the nickel electrode in the same manner as the nickel electrode containing the hydroxide, and is an alkali. It does not react with the electrolyte solution, and the electrolyte water is not consumed even if it coexists with the electrolyte solution. Therefore, the addition of the modified heavy rare earth compound to the nickel electrode is particularly effective for improving the characteristics of the liquid volume limited alkaline secondary battery.
- the heavy rare earth element oxide or hydroxide powder is dispersed in an aqueous KOH or NaOH solution having a concentration of 30 wt% and a temperature of 60 to 80 ° C. It can be obtained by leaving it for 3 days.
- the effect of increasing the oxygen overvoltage of the nickel electrode can be obtained by mixing and adding the powder to the positive electrode active material particles.
- the heavy rare earth element oxide powder is mixed with the active material powder of the nickel electrode, and the mixed powder is mixed with a KOH or NaOH aqueous solution having a concentration of 30 wt% and a temperature of 60 to 80 ° C. as described above. When the dispersion is heated to 60 to 80 ° C.
- the oxide of the heavy rare earth element is once dissolved in alkali, and water on the active material powder surface. After being deposited as an oxide, it is changed to the modified heavy rare earth compound. Then, since the heavy rare earth element oxide is once dissolved in the alkali and deposited as a hydroxide on the surface of the active material powder, the precipitated heavy rare earth element hydroxide is uniformly mixed with the active material particles. Since the mixture of the rare earth element compound and the active material particles as the final product is uniformly mixed, it is preferable because a remarkable effect can be obtained even if the ratio of the heavy rare earth compound is small.
- the content ratio of the heavy rare earth element hydroxide and the modified heavy rare earth element compound in the nickel electrode is particularly limited
- the ratio of heavy rare earth element hydroxide or oxide to the sum of active material particles and heavy rare earth element hydroxide or oxide is 0.5 to 3 wt% by weight. It is preferable that If the ratio is less than 0.5% by weight, the effect of adding a heavy rare earth element hydroxide or oxide cannot be obtained. If the ratio exceeds 3% by weight, the capacity of the nickel electrode is reduced and the current collector is reduced.
- the positive electrode active material particles in the present invention preferably contain at least one element selected from magnesium (M g) and calcium (C a) in a solid solution state of 0.1 to 3 wt%.
- M g magnesium
- C a calcium
- cobalt (C o) is included in the positive electrode active material particles in a solid solution state, the discharge potential of the nickel electrode is lowered, but by adding Mg in the solid solution state, the decrease in the discharge potential of the nickel electrode is suppressed. can do.
- Ca in solid solution in particles containing nickel hydroxide as the main component it was charged in a temperature atmosphere up to high temperatures (40 ° C) without using expensive heavy rare earth elements.
- the nickel electrode according to the present invention is a nickel electrode in which the active material particles for the nickel electrode are supported on a conductive substrate.
- the substrate applied to the nickel electrode according to the present invention is not particularly limited.
- nickel or nickel-plated steel sheets can be used suitably, and 2D equipment such as punched steel sheets can be used in addition to foam, formed fiber groups, and uneven 3D equipment. .
- the thickness is not particularly limited, but a thickness of 5 to 700 m is used.
- the substrate material is preferably nickel or nickel-plated copper plate that is excellent in corrosion resistance and harshness to alkali.
- a metal foam which is a three-dimensional porous body excellent in a current collecting function and an active material holding function.
- Active material particles whose main component is higher-order nickel hydroxide whose nickel oxidation number exceeds +2 may be composite particles with a surface layer whose main component is higher-order cobalt compound on the surface)
- a thickening agent solution is added and kneaded into a paste, and the paste is applied onto a substrate, dried, and pressed to form a nickel electrode having a predetermined thickness.
- a conductive aid such as nickel powder can be added to the paste as necessary.
- the thickening material is not particularly limited, and has been widely used in the past. Ruboxymethylcellulose (CMC) and methylcellulose (MC) can also be used. However, in the present invention, active material particles that have been subjected to an oxidation treatment in advance to form a higher order compound are applied when preparing the paste. In this case, for example, if carboxymethylcellulose (CMC) or methylcellulose (MC) is applied to the thickener, CMC or MC is oxidatively decomposed. There is a possibility that it becomes difficult to carry the paste on the conductive substrate.
- CMC carboxymethylcellulose
- MC methylcellulose
- the thickener consists of natural polysaccharides (xanthan gum) consisting of glucose, mannose, and dalucuronic acid, and glucose, mannose, rhamnose, and dalc mouth acid. It is preferable to use natural polysaccharides (welan gum). These natural polysaccharides have superior oxidation resistance compared to CMC and MC, and the thickener molecules do not decompose when mixed with active material particles that have undergone oxidation treatment to produce pastes. There is an advantage that the viscosity of the paste can be kept stable over time.
- the particles mainly composed of nickel hydroxide in the present invention include the cobalt compound that forms the surface layer, a part of nickel hydroxide that forms the core layer, and cobalt dissolved in the cobalt compound before being incorporated into the battery. More preferably, the acid is converted into a higher order nickel compound such as oxy nickel hydroxide or a higher order cobalt compound such as oxy cobalt hydroxide.
- Particles mainly composed of nickel hydroxide are oxidized with an oxidizing agent such as hypochlorite in the presence of, for example, sodium hydroxide or aqueous solution of lithium hydroxide, thereby increasing nickel hydroxide and cobalt hydroxide It can be changed to the compound of By performing the oxidation treatment, it is possible to suppress the discharge reserve generation of the Al force secondary battery.
- an oxidizing agent such as hypochlorite
- Li is impregnated in the active material powder for nickel electrode composed of particles mainly composed of high-order nickel hydroxide that has been previously oxidized in the process before producing the nickel electrode.
- the active material particles for nickel electrode in which a cobalt hydroxide layer is formed on the surface of core layer particles containing Ni (OH) 2 as a main component, are oxidized in an alkaline aqueous solution using an oxidizing agent. It is possible to produce composite particles in which high-order nickel hydroxide is used as a core layer and a high-order cobalt compound is arranged on the surface by oxidation by force or electrolysis.
- the method of oxidizing using an oxidizing agent is simple and preferable (oxidation treatment).
- the obtained composite particles are brought into contact with a LiOH aqueous solution to impregnate the composite particles with Li (Li impregnation treatment).
- the method for controlling the content ratio of Li in the composite particles is not particularly limited.
- the lithium content ratio has a specific value by making the processing conditions such as the temperature of the reaction bath (processing solution) for performing the Li impregnation treatment, the concentration of LiOH in the processing solution, and the processing time constant. Active material can be obtained.
- the amount of active material used in the reaction, the concentration of Li + contained in the treatment solution, and the amount of treatment solution should be specified, and the reaction should be sufficiently performed. This is a preferable method because the accuracy of the ratio of Li contained in the active material can be increased.
- Na OH and KOH may coexist in addition to LiOH.
- the concentration of alcohol contained in the oxidation treatment liquid is 2 Ow% or less and the oxidation treatment temperature is 60 ° C. or less. If the alkali concentration of the oxidation treatment liquid exceeds 20 wt% or the treatment temperature exceeds 60 ° C, the density of the active material particles may be reduced.
- an electrolysis cell is constructed in which particles are filled in a conductive container, a formed hydrogen storage alloy electrode is used as a counter electrode, and a 6 to 8 mo 1 Z 1 aqueous KOH solution is used as the electrolyte. Then, it should be electrolyzed so that the average oxidation number of Ni and Co contained in the particles becomes a predetermined value at a rate of 0.02 to 0.05 ItA. .
- the oxidized composite particles are immersed in an aqueous solution where the concentration of alkali such as Na or KOH is 30 wt% or more and the temperature exceeds 80 ° C. It is preferable to mix and wet the composite particles with an alkaline aqueous solution and to heat to a temperature exceeding 80 ° C because the powder resistance (electrical resistance) of the active material particles can be reduced. (Heat treatment)
- the active material particle for nickel electrode in which Li is incorporated in the crystal is an active material particle mainly composed of higher-order nickel hydroxide whose oxidation number of Ni exceeds +2 (higher-order cobalt on the surface). May be obtained by heat-treating in contact with an aqueous lithium hydroxide solution.
- the concentration of lithium hydroxide contained in the aqueous solution to be applied is not particularly limited, but is preferably from 0.:! To 3mo 1 to 1. When the concentration is less than 0.1 mo 1/1, the reaction (Li impregnation treatment) takes time. When the concentration exceeds 3 mo 1/1, the viscosity of the aqueous solution is high, and the active material particles are difficult to wet with the treatment solution. There is.
- the treatment temperature is 30 ° C or higher, preferably 50 ° C or higher, the processing proceeds rapidly and can be performed in a short time.
- the treatment temperature is preferably 80 ° C. or lower, more preferably 60 ° C. or lower, since it is possible to avoid a decrease in the density of the active material particles when the treatment is performed.
- the method for synthesizing the positive electrode active material particles having different Li contents of the first embodiment and the characteristics of the nickel metal hydride battery using the positive electrode active material according to the examples will be described.
- the relationship between the amount of i and the characteristics of the battery is common to other embodiments described later, and is not limited to the first embodiment.
- the spherical high-density nickel hydroxide particles 1 O O g were put into 400 ml of an alkaline aqueous solution whose pH was controlled to 1 2 ⁇ 0.2 with NaOH. While stirring the solution, an aqueous solution containing cobalt sulfate and ammonia at a predetermined concentration was added dropwise. During this time, an aqueous Na 2 O 2 H solution was appropriately added dropwise to maintain the reaction bath temperature at 45 ⁇ 2 ° C. and pH within the range of 12 ⁇ 0.2.
- the temperature was maintained within 45 ⁇ 2 ° (:, pH in the range of 12 ⁇ 0.2 for about 1 hour, and a surface layer made of mixed hydroxide containing Co was formed on the surface of the nickel hydroxide particles.
- the resulting particles were mixed with 12 g of 18 mol 1 aqueous NaOH solution to obtain a wet state, and held for 1 hour at 120 ° C. Next, the aqueous sodium hydroxide solution was filtered off, washed with water and dried.
- the ratio of the surface layer of the composite hydroxide particles obtained is the core layer mother particles
- the core layer (Hereinafter simply referred to as the core layer) was 7 wt%.
- 100 g of the particles after forming the surface layer were added to and dispersed in 400 g of a 4.5 mol Z 1 aqueous NaOH solution and heated so that the temperature of the dispersion was 50 ° C. . While stirring the dispersion, 30 ml of sodium hypochlorite solution was added and stirring was continued for about 3 hours. During this time, the temperature of the solution was kept at 50 ° C. The particles were separated from the dispersion by filtration, washed with water and dried.
- the average oxidation number of transition metal elements (N i, Co) contained in the active material particles after the oxidation treatment is determined by a known method (after reacting the active material particles with ferrous sulfate ammonium, permanganic acid Perform redox titration with potassium). As a result, the average oxidation number of transition metal elements (Ni, Co) was +2.1.5.
- 100 g of the composite particles after the oxidation treatment are dispersed in 4 OO g of a mixed aqueous solution of Na OH and LiOH containing Na OH 4.5 mo 1 1, LiOH 1.2 mo 1/1, and 3 hours. While stirring, the temperature of the dispersion was kept at 50 ° C. The mixed water after completion of the reaction The solution was filtered off. The obtained particles were dispersed in 400 ml of pure water at room temperature (25 ° C.) and washed with water by a decantation method (decantation). The supernatant was repeatedly washed with water until the pH reached 11 and then dried to obtain active material particles for nickel electrodes.
- the amount of Li contained in the nickel electrode active material particles was quantified by atomic absorption analysis.
- the amount of lithium contained in the active material particles obtained in this example (converted to a simple substance) was 0.2 wt%.
- the obtained active material particles and an aqueous xanthan gum solution with a concentration of 0.6 wt% and a dispersion of polytetrafluoroethylene powder with a solid content ratio of 4 awt% using water as a dispersion medium are 7 6.7: 22. 9: 0.4 was mixed to obtain an active material paste.
- the active material paste is filled in a foam nickel substrate having a surface density of 450 mm / m.2 and a thickness of 1.4 mm, dried, and rolled to form a nickel electrode base plate having a thickness of 0.8 mm.
- the original plate is cut to a predetermined dimension (3 Omm x 30 mm), and the capacity calculated from the active material filling amount (active material particle filling amount (g) X nickel hydroxide in the active material particles (higher nickel)
- active material particle filling amount (g) X nickel hydroxide in the active material particles (higher nickel) A nickel electrode having a ratio of (including compound) (wt%) X 2 8 9 mAh / g ⁇ of 460 mAh was obtained.
- the hydrogen storage alloy electrode was used as a negative electrode, and a cell having a nickel electrode as a positive electrode, which was easily separated from the nickel electrode of this evaluation, was assembled and formed by a predetermined method.
- Nickel electrode An open cell was fabricated by placing a hydrogen storage alloy electrode that had been converted through a separator on both sides of the battery and injected a predetermined amount of alkaline electrolyte containing 7mo 1 -1 K OH.
- Ten nickel electrode evaluation cells were prepared, 5 of which were charged at an ambient temperature of 20 ° C and the other 5 were charged at an ambient temperature of 60 ° C. Batteries charged at an ambient temperature of 60 ° C were transferred to an ambient temperature of 20 ° C immediately after the end of charging. Both the battery charged at an ambient temperature of 20 ° C and the battery charged at an ambient temperature of 60 ° C were left for 3 hours after charge termination, and then discharged at an ambient temperature of 20 ° C. Charging was performed for 7.5 hours at a rate of 0.2 It A (92 mA) with respect to the positive electrode. Discharge was performed at a rate of 0.2 1 tA (92 mA), and the discharge was turned on when the potential of the positive electrode became 0 V with respect to the potential of the reference electrode (HgZHgO electrode).
- the ratio of the discharge capacity (mAh) obtained by discharging after charging at 60 ° C in the charge / discharge test to the discharge capacity (mAh) obtained by discharging after charging at 20 ° C was calculated, The calculated value was defined as the charging efficiency (%) at 60 ° C charging.
- the base plate of the nickel electrode and the base plate of the hydrogen storage alloy electrode are cut to a predetermined size and laminated through a separator made of a nonwoven fabric of polypropylene having a thickness of 100 / zm and subjected to hydrophilic treatment. Turned to configure the electrode group.
- the electrode plate group is inserted into a metal battery case that also serves as a negative electrode terminal, and after injecting a predetermined amount of alkaline electrolyte containing 6.8 mo 1-1 KOH and 0.8 mo 1 1 LiOH, Using a cap that also serves as a terminal, the open end of the metal battery case was hermetically sealed to provide a cylindrical sealed nickel hydride secondary battery.
- the filling capacity of the positive electrode (nickel electrode) of the secondary battery was 2000 mAh, and the filling capacity of the negative electrode (hydrogen storage alloy electrode) was 320 OmAh.
- the fabricated battery was left for a whole day and night, charged at 1 ° C 30 ItA for 30 hours at an ambient temperature of 20 ° C, and then charged for 6 hours at 0.1 ItA. After that, the battery was discharged at 0. l. I tA with a cut voltage of 1.0V. Subsequently, the battery was charged at 0. II t A for 15 hours. After charging, the battery was discharged at 0.2 It A at a cut voltage of 1.0 V.
- the charge / discharge cycle was defined as one cycle, and the charge / discharge cycle was repeated four times from the second cycle to the fifth cycle. (Charge / discharge test of cylindrical nickel hydride secondary battery)
- the battery was discharged at a cut voltage of 1.0V.
- the value is the charging efficiency (%) when charging at 60 ° C. .
- Example 2 in the lithium impregnation process to the composite particles obtained after the oxidation treatment, the LiOH concentration of the mixed aqueous solution of NaOH and LiOH was set to 0.1 mo 1/1. Otherwise, the configuration was the same as in Example 1. The ratio of Li contained in the obtained active material particles was 0.01 wt%. This example is referred to as Example 2.
- Example 3 in the lithium impregnation process in the composite particles obtained after the oxidation treatment, the LiOH concentration of the mixed aqueous solution of NaOH and LiOH is 0.2. mo 1 1 Otherwise, the configuration was the same as in Example 1. The ratio of Li contained in the obtained active material particles was 0.03 wt%. This example is referred to as Example 3.
- Example 1 in the lithium impregnation process in the composite particles obtained after the oxidation treatment, the LiOH concentration of the mixed aqueous solution of NaOH and LiOH to be applied was set to 0.4 mo1Z1. Otherwise, the configuration was the same as in Example 1. The ratio of Li contained in the obtained active material particles was 0.05 wt%. This example is referred to as Example 4.
- Example 5 in the lithium impregnation process in the composite particles obtained after the oxidation treatment, the LiOH concentration of the mixed aqueous solution of NaOH and LiOH was set to 0.8 mo1 / 1. Otherwise, the configuration was the same as in Example 1. The ratio of Li contained in the obtained active material particles was 0.1% wt%. This example is referred to as Example 5.
- Example 1 in the lithium impregnation process to the composite particles obtained after the oxidation treatment, the LiOH concentration of the mixed aqueous solution of NaOH and LiOH to be applied was set to 1.5 mo ⁇ / ⁇ . Otherwise, the configuration was the same as in Example 1. The ratio of Li contained in the obtained active material particles was 0.3 wt%. This example is referred to as Example 6.
- Example 7 in the lithium impregnation process in the composite particles obtained after the oxidation treatment, the LiOH concentration of the mixed aqueous solution of NaOH and LiOH was set to 2mo11. Otherwise, the configuration was the same as in Example 1. The ratio of Li contained in the obtained active material particles was 0.5 wt%. This example is referred to as Example 7.
- Example 1 the lithium impregnation process was not performed. In the obtained active material particles The ratio of Li included was 0.0 wt%. Otherwise, the configuration was the same as in Example 1. This example is referred to as Comparative Example 1.
- Example 1 100 g of nickel hydroxide particles obtained after the heat treatment process and before the oxidation treatment process were mixed with NaOH 4.5mo 1/1, LiOH l. 2m o 1/1 N a Dispersed in 400 g of a mixed aqueous solution of OH and LiOH 'and stirred for 3 hours, while maintaining the temperature of the dispersion at 50 ° C. After completion of the reaction, the mixed aqueous solution was filtered off. Disperse the obtained particles in 400 ml pure water at room temperature and disperse them in 400 ml pure water at room temperature. Disperse the supernatant in 400 ml pure water at room temperature using the decantation method. Washing with water was repeated until the pH reached 11. Also, the lithium impregnation process after the oxidation process was omitted. Otherwise, the configuration was the same as in Example 1. The ratio of Li contained in the obtained active material particles was 0.005 wt%. This example is referred to as Comparative Example 2.
- Example 1 the LiO concentration of the mixed aqueous solution of NaOH and LiOH to be applied in the lithium impregnation process to the composite particles after the oxidation treatment was 2.4 moI1. Other than that, the configuration was the same as in Example 1. The ratio of Li contained in the insulted active material particles was 0.7 wt%. This example is referred to as Comparative Example 3.
- Example 1 shows the Li content ratio of the active material particles for nickel electrodes and the test results of the nickel electrode evaluation cell obtained in Examples 1 to 7 and Comparative Examples 1 to 4. Also, Fig. 1 shows the relationship between the discharge capacity obtained by discharging after discharging at an ambient temperature of 20 ° C and the Li content ratio. Figure 2 shows the discharge obtained by discharging after charging at an ambient temperature of 60 ° C. The relationship between the capacity and the Li content ratio is shown.
- the embodiment of the present invention has higher discharge capacity and charging efficiency than the comparative example, and the capacity is calculated from the active material filling amount (calculated as 2 89 mAh per 1 g of active material).
- the capacity of 4 6 O mA h is 1.1 3 to 1.2 times as large.
- such a high discharge capacity was obtained because of the Li force S inserted in the crystal of the nickel electrode active material, and the active material when the Ni oxidation number increased by charging. This is thought to be due to stabilization of crystals and an increase in the amount of charge accepted for the nickel electrode active material.
- Comparative Example 1 with no Li added shows a capacity close to the calculated value, and Comparative Example 2 has a smaller capacity increase than Comparative Example 1.
- Comparative Example 2 it is considered that the significant effect of adding Li was not obtained because the Li content ratio of the nickel electrode active material was small. Further, Comparative Example 3 and Comparative Example 4 in which the Li content ratio of the nickel electrode active material is large maintain a higher capacity than Comparative Examples 1 and 2, but the Li content ratio is 0.05. The discharge capacity is slightly smaller than that of Example 4 to Example 7 which is ⁇ 0.5 wt%. This is because the utilization rate of the active material decreased slightly due to the low discharge potential of the nickel electrode. It is considered. In Comparative Example 1 and Comparative Example 2, the charge efficiency when charging at 60 ° C is lower than that of the Example. This is probably because inactive ⁇ - ⁇ i OOH was generated by charging. .
- Comparative Example 3 and Comparative Example 4 with high Li content Comparative Example 1 and Comparative Example 2]!: The charging efficiency when charging at 60 ° C is high, but the charging efficiency is low compared to the examples.
- a high discharge capacity was obtained when the Li ratio of the nickel electrode active material was in the range of 0.01 to 0.5 wt%. It was found that a high discharge capacity was obtained at 0.05 to 0.5 wt%, and a particularly high discharge capacity was obtained at 0.:! To 0.5 wt%.
- a high discharge capacity is obtained when the Li content of the nickel electrode active material is in the range of 0 ⁇ 0 1 to 0.5 wt%. In particular, it was found that a particularly high discharge capacity was obtained at 0.1 to 0.5 wt%.
- the content ratio of Li in the nickel electrode active material is preferably 0.01 to 0.5 wt%, and preferably 0.05 to 0.5 wt%. It was found that 0.:! To 0.5 wt% was more preferable.
- the content ratio of Li in the nickel electrode active material is 0.05 to 0.3 wt%.
- Table 2 shows the test results of the cylindrical nickel-metal hydride storage batteries according to Example 1 to Example 7, Comparative Example 2, and Comparative Example 3.
- Fig. 3 shows the relationship between the discharge capacity obtained by discharge after discharge at an ambient temperature of 20 ° C and the Li content ratio
- Fig. 4 shows the relationship after discharge after charging at an ambient temperature of 60 ° C.
- FIG. 5 shows the relationship between the charge cycle life and the lithium content ratio of the nickel electrode active material particles.
- Table 2 shows the test results of the cylindrical nickel-metal hydride storage batteries according to Example 1 to Example 7, Comparative Example 2, and Comparative Example 3.
- Fig. 3 shows the relationship between the discharge capacity obtained by discharge after discharge at an ambient
- the discharge capacity of the cylindrical nickel hydride secondary battery reflects the discharge capacity of the applied nickel electrode, and the examples were compared at both ambient temperatures of 20 ° C and 60 ° C during charging. The discharge capacity was higher than that of the example.
- the nickel-metal hydride storage battery using a nickel electrode with a Li content ratio of 0.1 to 0.5 wt% shows a high capacity as shown in Figs. I understood.
- a nickel metal hydride storage battery using a nickel electrode with a Li content ratio of 0.05 to 0.5 wt% shows a high capacity, and when it is charged at 60 ° C, it is shown in Fig. 4.
- the nickel-metal hydride storage battery using a nickel electrode having a Li content ratio of 0.1 to 0.5 wt% showed a particularly high capacity.
- the increase in internal pressure when charging is suppressed as compared with the comparative example. This is because, as shown in Table 1, when the nickel electrode according to the example is applied, high charging efficiency can be obtained, and since the oxygen gas generated from the positive electrode during charging is small, the internal pressure of the battery during charging increases. This is considered to have been able to be suppressed.
- the battery is overcharged each time it is charged, and the generation of ⁇ -NiOOH is promoted or the electrolyte is not charged when the battery is charged. It is thought that as the amount of oxygen generated by decomposition increases, the corrosion of the hydrogen storage alloy is accelerated and the discharge capacity is rapidly reduced.
- a predetermined amount (in the above examples) 100 g) of the oxidized and heat-treated active material particles in a predetermined amount (400 g in the example) of a mixed solution of NaOH and LiOH at a temperature of 50 ° C for a predetermined time (in the example 3 hours) Rather than filtering and separating the particles and the treatment liquid after immersion, a predetermined amount of a LiOH aqueous solution having a predetermined concentration is added to a predetermined amount of the active material particles, and the active material particles are wetted with the LiOH aqueous solution.
- the kneading is continued while maintaining the temperature of the mixture at 60 to 80 ° C., and after evaporating and removing the water, the obtained particles are washed with water in the same manner as in Examples 1 to 7 according to Embodiment 1 above. Impregnation treatment can be performed.
- This method is preferable because most of the added i is taken into the active material particles, so that Li is not wasted and the concentration of Li taken into the active material can be accurately controlled. It is a method.
- the amount of the Li aqueous solution to be added is preferably set so that the mixture becomes a paste that is easily kneaded.
- 100 g of the core layer particles were put into 400 ml of an alkaline aqueous solution whose pH was adjusted to 12 ⁇ 0.2. While stirring the solution, 100 ml of an aqueous solution containing 1 mo 1 Z 1 cobalt sulfate and 1 mo 1/1 ammonium sulfate was added dropwise in small portions. During this time, an aqueous NapH solution was appropriately added dropwise to maintain the reaction bath temperature at 45 ⁇ 2 ° C. and p.H within the range of 1 2 ⁇ 0.2.
- the average oxidation number of the transition metal elements (N i, Co) contained in the active material particles after the immersion treatment is determined by a known method (after the active material particles are reacted with ferrous sulfate ammonium, Measure redox titration using potassium ganate).
- the average oxidation number of the transition metal elements (Ni, Co) was +2.15.
- the value was substituted into the formula for calculating the oxidation number of Ni, and the oxidation number of Ni was calculated to be 2.10.
- 100 g of the composite oxide particles subjected to the oxidation treatment are mixed aqueous solution of Na OH and LiOH containing 4.5 mol l Z l Na OH and 0.8 mol 1 Z 1 LiOH. 4 It was immersed in 0 0 g for 3 hours. During this time, the temperature of the solution was kept at 50 ° C., and the solution was slowly stirred. The resulting particles are then centrifuged to remove the solution adhering to the particle surfaces, and the resulting composite oxide particles are dispersed in 400 ml of pure water at room temperature (25 ° C). Washed with water by the decantation method. The top solution was washed repeatedly with water until the pH dropped to 11 and then dried. When the composite oxide particles were subjected to atomic absorption spectroscopy and the amount of Li contained in the composite oxide particles was quantified, the amount of Li was 0.1 l w t%.
- the active material paste was filled in a foam nickel base having a surface density of 4500 g / m and a thickness of 1.4 mm, dried, and rolled to obtain a nickel electrode base plate having a thickness of 0,8 mm.
- C ⁇ 7 ⁇ 1 3 ⁇ 3 (Mm A dispersion of SBR (styrene butadiene rubber) as a binder and an aqueous solution of methyl cellulose (MC) as a thickener are added and kneaded to a hydrogen storage alloy powder having a composition to form a paste. After being applied to a nickel-plated perforated steel plate-like substrate, it was dried and rolled to obtain a hydrogen storage electrode base plate.
- the nickel electrode original plate was cut into a predetermined dimension (30 ⁇ 3 Omm) to obtain a positive electrode of a nickel electrode evaluation cell.
- the positive electrode filling capacity ⁇ filling amount of active material particles (g) X ratio of nickel hydroxide (including higher nickel compound) in active material particles (w t%) X 289 mAh7g ⁇ was 460 mAh.
- the hydrogen storage electrode original plate was cut into a predetermined dimension (35 ⁇ 35 mm) to form a negative electrode for a nickel electrode evaluation cell.
- the filling capacity of the negative electrode (filling amount of hydrogen storage alloy powder X capacity per unit weight of hydrogen storage alloy powder) was 730 mAh.
- One positive electrode was placed in the middle, a formed negative electrode was placed on both sides of the positive electrode via a separator, and a predetermined amount of an alkaline electrolyte containing 7mo 1/1 KOH was injected to produce an open cell.
- the cell was formed by a predetermined method. '.
- the nickel electrode original plate and the hydrogen storage alloy electrode original plate are cut into predetermined dimensions, and the thickness 1 Lamination was carried out through a separator made of a nonwoven fabric made of polypropylene subjected to hydrophilic treatment of 0 .mu.m, and the laminate was wound to constitute an electrode plate group. Insert the electrode plate group into a metal battery case that also serves as the negative electrode terminal, and inject 3.7 ml of an alkaline electrolyte containing 6.8 mo 1-in-1 KOH and 0.8 mol Z l LiOH. After that, the open end of the metal battery case was hermetically sealed using a cap that also served as the positive electrode terminal, and a liquid-restricted cylindrical sealed nickel-hydrogen battery was obtained.
- the filling capacity of the positive electrode (nickel electrode) of the battery was 2200 mAh, and the filling capacity of the negative electrode (hydrogen storage electrode) was 320 OmAh.
- the fabricated battery was left for a whole day and night, then charged at 1/30 It A for 30 hours at an ambient temperature of 20 ° C, and then charged at 0.1 It A for 6 hours. After that, it was discharged at 0.1 It A as a cut voltage of 1. OV. Subsequently, the battery was charged at 0. II t A for 15 hours, and after charging, the battery was discharged at 0.2 It A at a cut voltage of 1.0 V.
- the charge / discharge cycle was defined as one cycle, and the charge / discharge cycle was repeated four times from the second cycle to the fifth cycle.
- Ten pre-formed batteries were prepared and charged at an ambient temperature of 20 ° C.
- the battery was charged for 6 hours at a charge rate of 0.21 tA (400 mA).
- the battery was discharged at an ambient temperature of 20 ° C at a rate of 0.2 It A (40 mA) and a discharge force voltage of 1.0 V after being left for 1 hour after charge termination.
- the average discharge voltage (V) and discharge capacity (mAh) in the charge / discharge were examined.
- the ratio (%) of the discharge capacity obtained by the discharge to the positive electrode filling capacity (2 0 0 OmAh) was determined and used as an index for evaluating the characteristics of the test battery.
- Example 8 the i OH concentration of the treatment liquid (mixed aqueous solution of NaOH and LiOH) was set to 0.1 m o 1/1 in the process of performing the Li impregnation immersion treatment on the composite oxide particles. Others were the same as in Example 8. The ratio of Li contained in the obtained composite oxide particles was 0.01 wt%. This example is referred to as Example 9.
- Example 8 the i OH concentration of the treatment liquid (mixed aqueous solution of NaOH and LiOH) was set to 0.2 m o 1 Z 1 in the process of performing the Li impregnation immersion treatment on the composite oxide particles. Others were the same as in Example 8. The ratio of Li contained in the obtained composite oxide particles was 0.03 wt%. This example is referred to as Example 10.
- Example 1 In Example 8, in the process of subjecting the composite oxide particles to Li impregnation immersion treatment, the treatment liquid (mixed aqueous solution of NaOH and LiOH)! 4 mo 1 1 1 Others were the same as in Example 8. The ratio of Li contained in the obtained composite oxide particles was 0.05 wt%. This example will be referred to as Example 11.
- Example 8 the process liquid (mixed aqueous solution of NaOH and LiOH) in the course of subjecting the composite oxide particles to Li impregnation immersion treatment had an iOH concentration of 1.5 mo 1 Z 1. The others were the same as in Example 8. The ratio of Li contained in the obtained composite oxide particles was 0.3 wt%.
- Example 12 This example is referred to as Example 12. (Example 1 3)
- Example 8 the i OH concentration of the treatment liquid (mixed aqueous solution of NaOH and LiOH) was set to 2. Omo 1/1 in the course of performing the Li impregnation immersion treatment on the composite oxide particles. Others were the same as in Example 8. The ratio of Li contained in the obtained composite oxide particles was 0.5 wt%. This example is referred to as Example 13.
- Example 8 the process of immersing the composite oxide particles in the LiOH aqueous solution was omitted.
- the ratio of Li contained in the obtained composite oxide particles was 0.00% by weight.
- This example is referred to as Comparative Example 1.
- Example 8 100 g of the composite hydroxide particles before the oxidation treatment were mixed with 4.5 OH 1 NO 1 Na OH and 0.8 mol L 1 OH containing Na OH and L i OH. It was immersed in the combined aqueous solution for 3 hours. During this time, the temperature of the solution was kept at 50 ° C., and the solution was stirred gently. Next, the obtained particles are centrifuged to remove the solution adhering to the particle surface, and then the obtained composite oxide particles are dispersed in 400 ml of pure water by the gradient method (decantation). Washed with water. The top solution was washed repeatedly with water until the pH dropped to 11, and then dried. Also, the Li impregnation treatment after the oxidation treatment process was omitted. Others were the same as Example 8. The ratio of Li contained in the obtained composite oxide particles was 0.05 5 wt%. This example is referred to as Comparative Example 2.
- Example 8 in the process of immersing the composite oxide particles in an aqueous solution of NaOH and LiOH, the LiOH concentration of the treatment liquid was set to 2.4 mo 1/1. Others were the same as Example 8. The ratio of Li contained in the obtained composite oxide particles was 0.7 wt%. This example is referred to as Comparative Example 7. (Comparative Example 8)
- Example 8 in the process of immersing the composite oxide particles in an aqueous solution of NaOH and LiOH, the LiOH concentration of the treatment liquid was 3. Omo 1/1. Others were the same as Example 8. The ratio of Li contained in the obtained composite oxide particles was 1.0 wt%.
- Comparative Example 8 Table 3 shows the Li content ratios of the active material grains for the nickel electrode obtained in Examples 8 to 13 and Comparative Examples 5 to 8, and the test results of the nickel electrode evaluation cell (10 flat samples). Average value).
- Figure 6 shows the relationship between the discharge capacity shown in Table 3 and the Li content ratio
- Figure 7 shows the relationship between the irreversible capacity and the Li content ratio.
- the embodiment of the present invention has a larger discharge capacity than the comparative example 5 in which an active material not containing Li is applied, and the capacity is a capacity calculated from the active material filling amount 4 6 OmAh (289 mAh / g) 1.02 ⁇ : I. 08 times the size and irreversible capacity is small.
- the high discharge capacity was obtained because the Li material inserted in the nickel electrode active material crystal, and the active material crystal when the Ni oxidation number increased by charging were stabilized. This is thought to be due to an increase in the amount of charge of the nickel electrode active material.
- Comparative Example 5 shows a capacity slightly lower than the calculated value, and Comparative Example 6 has a smaller capacity increase than Comparative Example 5.
- Comparative Example 6 since the Li content of the nickel electrode active material is small, a significant effect cannot be obtained by adding Li. It is thought that In Comparative Example 5 and Comparative Example 6, the amount of ⁇ -NiOOH produced is large. This is because the irreversible capacity is larger than in Examples, and Comparative Examples 7 and 8 have a large Li content ratio. Although the discharge voltage is low, the amount of charge accepted
- the irreversible capacity is large due to the small ratio of the discharge capacity to Oc.
- a high discharge capacity was obtained when the ratio of Li of the nickel electrode active material was 0.01 wt% or more. It was found that a high discharge capacity was obtained at%, and a particularly high discharge capacity was obtained within a range of 0.1% or more. Moreover, as shown in FIG. 7, the irreversible capacity is small when the Li content ratio of the nickel electrode active material is in the range of 0.01 to 0.5 wt%, and in particular, 0.05 to 0.5 wt%. In particular, the irreversible capacity 0) was found to be O 0) small.
- the content ratio of Li in the nickel electrode active material ⁇ is preferably set to 0.05 to 0.5 wt%, and is 0.05 to 0.5 wt%. It was found that 0.:! To 0.5 wt% was more preferable.
- the Li content in the nickel electrode active material is particularly preferably 0.05 to 0.3 wt% as shown in Table 4 and FIG. 8 below. Table 4 shows the test results of the cylindrical nickel hydrogen batteries according to Example 8 to Example 13 and Comparative Example 5 to Comparative Example 8. Figure 8 shows the cycle test results.
- Example 8 0. 10 2084 1771 423
- Example 9 0.010 2030 101.5 1786 398
- Example 10 0.03 2063 103.0 1772 415
- Example 11 0.05 2071 104.5 1800 416
- Example 12 2102 105.
- Comparative Example 7 and Comparative Example 8 had a large discharge capacity at 20 ° (:, 0.21 tA discharge, but a small discharge capacity at 10 ° C, II tA discharge, and It was found that the cycle life was inferior, as shown in Fig. 8.
- Comparative Example 7 and Comparative Example 8 the diffusion of protons in the active material particles was reduced due to the high Li content ratio of the active material particles.
- Slow force ⁇ High discharge rate (1 I t A discharge) When compared with Example 8 to Example 13, Comparative Example 5, and Comparative Example 6, the discharge voltage is lower and the discharge duration is shorter. (The discharge capacity is small.) In the charge / discharge cycle test conducted at an ambient temperature of 20 ° C, the same tendency as the 10 ° C, 1 It A discharge was observed.
- the amount of electricity charged is fixed ⁇ charge rate (charge current) and charge time are fixed ⁇ . 7.
- the degree of overcharge per cycle is larger than in Examples 8 to 13 and Comparative Examples 5 and 6, and ⁇ -N is inactive due to the overcharge. It is considered that the discharge capacity decreased rapidly due to the promotion of i OOH generation First Embodiment (b) — Inclusion of the rare earth element compounds of (2) and (3) above (Example 14), (Production of nickel electrode, nickel electrode evaluation cell, cylindrical nickel hydride secondary battery)
- Example 14 the nickel electrode active material particles 98 parts by weight and erbium hydroxide ⁇ E r (OH) 3 ⁇ 2 parts by weight instead of the nickel electrode active material particles in the process of preparing the nickel electrode Of mixed particles were applied. Otherwise, the nickel electrode evaluation cell and the cylindrical nickel hydride secondary battery had the same configuration as in Example 1. The filling capacity of the nickel electrode applied to the nickel electrode evaluation cell was 450 mAh, and the filling capacity of the nickel electrode applied to the cylindrical nickel hydride secondary battery was 1 960 mAh. This example is referred to as Example 14.
- the discharge capacity (mAh) obtained by the discharge and the ratio of the discharge capacity (mAh) to the discharge capacity obtained by the discharge in the charge / discharge test at the ambient temperature of 20 ° C are the charge efficiency at 60 ° C charge. (%), And discharge capacity (mAh) and charge efficiency (%) were used as indices for evaluating the characteristics of the test battery.
- the battery was charged at a rate of 1 ItA (2744 mAh) for 84 minutes, left for 1 hour after the charge was terminated, and then discharged at a rate of 1 ItA and a discharge cut voltage of 1.0V.
- the charge / discharge cycle was taken as one cycle, and when the discharge capacity dropped to 80% of the first cycle of the charge / discharge cycle, the charge / discharge cycle was terminated, and the number of cycles at that time was taken as the cycle life.
- Example 14 nickel electrode active material particles 98 instead of mixed particles of 98 parts by weight of nickel electrode active material particles and 2 parts by weight of erbium hydroxide ⁇ E r (OH) 3 ⁇ in the process of preparing the nickel electrode 98 Mixed particles of parts by weight and 2 parts by weight of ytterbium hydroxide ⁇ Yb (OH) 3 ⁇ were applied. Otherwise, nickel electrode evaluation cell, cylindrical The nickel hydride secondary battery has the same configuration as in Example 14. This example is referred to as Example 15.
- Example 15 active material particles not impregnated with i were applied as the active material for the nickel electrode, and the other O had the same configuration as in Example 15.
- This example is referred to as Comparative Example 9.
- Table 5 shows the test results of the nickel electrode evaluation cell according to Example 14, Example 15, and Comparative Example 9, and Table 6 shows the test results of the cylindrical nickel hydride secondary battery.
- the nickel electrode evaluation d-valent cell according to Example 14 and Example 15 has higher charging efficiency than that of Example 1.
- the charging efficiency when charging at an ambient temperature of 60 ° C is greatly improved.
- Example 14 and Example 15 also have high charging efficiency when charged at 60 ° C. in comparison with Comparative Example 9.
- the charging efficiency is improved by adding rare earth element hydroxides of Er and Yb to the nickel electrode. It is considered that the charging efficiency was particularly noticeably improved when charging at a high temperature of 60 ° C.
- Li content Cycle life Category Additive 20 ° C charge 60 ° C charge 20 ° C charge 60 ° C charge '60 ° C charge
- Example 14 Er (OH) 3 0.5 0.5 7 2236 1580 455
- Example 15 Yb (OH) 3 0. 20 0.5, 0.F 2245 1620 470
- Comparative Example 9 Yb (OH) 3 0.0 0.8 1. 0 2109 1413 67.0 430
- the cylindrical nickel hydride secondary batteries according to Example 14 and Example 15 had a large increase in pressure inside the battery when charged at a high ambient temperature of 60 ° C. Indicates discharge capacity.
- Example 14 and Example 15.15 as described in the nickel electrode evaluation cell, in addition to the fact that the nickel electrode active material contains Li, the rare earth elements of Ho to Lu are changed to nickel.
- the charging efficiency is improved, and the decomposition of the electrolyte is reduced, so the rise in pressure inside the battery is suppressed and a high capacity is obtained.
- the stability of the crystal structure of the nickel electrode active material has been improved, and the decrease in the discharge capacity of the nickel electrode during repeated charging and discharging has been suppressed. It is thought that the cycle life was improved because the increase in impedance was suppressed and the corrosion of the hydrogen storage alloy was suppressed.
- Example 8 instead of the nickel electrode active material particles alone in the process of producing the nickel electrode, a mixture comprising 98 parts by weight of the nickel electrode active material particles and 2 parts by weight of the ytterbium oxide powder ⁇ Y b 2 O 3 ⁇ powder It was used. Otherwise, the configuration was the same as in Example 8, and a cylindrical nickel-metal hydride storage battery having a nickel electrode filling capacity of 196 OmAh was obtained. This example is referred to as Example 16.
- Ten pre-formed storage batteries were prepared and charged at an ambient temperature of 20 ° C.
- the battery was charged for 6 hours at a charge rate of 0.2 ItA (392mA).
- the battery was discharged for 1 hour after termination of charge, and discharged at an ambient temperature of 20 ° C at a rate of 0.2 1 tA (392 mA) and a discharge cut voltage of 1.0 V.
- the average discharge voltage iN and the discharge capacity (mAh) in the charge / discharge were examined.
- Example 16 a Yb (OH) 3 powder was used in place of the Y b 2 0 3 powder in the process of producing the nickel electrode.
- Example 17 a cylindrical nickel-metal hydride storage battery having the same configuration as in Example 16 and having a nickel electrode filling capacity of 1 96 OmAh was obtained. This example is named Example 17.
- Example 16 a modified ytterbium compound powder was used in place of the Y b 2 0 3 powder in the process of producing the nickel electrode.
- Example 18 a cylindrical nickel-metal hydride storage battery having the same configuration as in Example 16 and having a nickel electrode filling capacity of 1 96 Om Ah was obtained. This example is referred to as Example 18.
- Example 18 holmium hydroxide ⁇ Ho (OH) 3 ⁇ was used instead of Yb (OH) 3 in the process of synthesizing the modified heavy rare earth compound.
- Example 18 erbium hydroxide ⁇ E r (OH) 3 ⁇ was used in place of Yb (OH) 3 in the process of synthesizing the modified heavy rare earth compound.
- Example 18 thulium hydroxide ⁇ Trri (OH) 3 ⁇ was used instead of Yb (OH) 3 in the process of synthesizing the modified heavy rare earth compound.
- d 0.88 nm
- d 0.84 nm
- d 0.76 nm.
- Ecke Both the cell for evaluating the electrode and the cylindrical nickel-metal hydride storage battery had the same configuration as in Example 18. This example is referred to as Example 21.
- Example 18 lutetium hydroxide ⁇ Lu (OH) 3 ⁇ was used instead of Yb (OH) 3 in the process of synthesizing the modified heavy rare earth compound.
- Table 7 shows the test results of the cylindrical nickel metal hydride batteries according to 16 to 22 in combination with Example 8.
- the cylindrical nickel-metal hydride batteries according to Examples 16 to 22 have higher charging efficiency than Example 8. In particular, the charging efficiency when charging at an ambient temperature of 60 ° C is greatly improved. In addition, the cylindrical nickel-metal hydride storage batteries according to Examples 16 to 22 showed an excellent cycle life as compared with Example 8. In Examples 16 to 22, the charging efficiency was increased by adding a heavy rare earth element compound to the nickel electrode in addition to the insertion of L ⁇ into the nickel electrode active material, and the ambient temperature was 60 °. It seems that the charging efficiency is remarkably improved when charging at a high temperature of C. As such It is considered that excellent cycle life was obtained because side reactions such as electrolysis of the electrolyte were suppressed due to the increase in electric efficiency.
- Example 18 to which the modified Yb compound was added was particularly excellent in cycle characteristics. Even when Ho, Er, Tm, and Lu compounds other than Yb were added, it was found that particularly excellent cycle characteristics were obtained when a modified heavy rare earth compound was added among these compounds. This is thought to be due to the fact that the use of a nickel electrode containing a modified heavy rare earth compound suppressed the consumption of water constituting the electrolytic solution and resulted in an excellent cycle life.
- Nickel hydroxide (Zn 3. Contains 8 wt% After formation of the surface layer described later, oxidation treatment and heating treatment of the composite hydroxide particles, and Li impregnation treatment into the composite hydroxide particles The content of zinc metal in the subsequent active material particles is 3.6 wt%. ) High-density spherical particles (hereinafter referred to as nickel hydroxide particles).
- the obtained particles were put into sodium hydroxide aqueous solution 4 O Oml containing sodium hydroxide 1 at a temperature of 120 ° C. and stirred while maintaining the temperature for 1 hour. The aqueous solution was then filtered off, washed with water and dried. The ratio of the surface layer of the obtained composite hydroxide particles was 5 wt% with respect to the core layer particles.
- 100 g of the particles after the surface layer is formed are dispersed in 400 g of a Na OH aqueous solution having a Na OH concentration of 4.5 mo 1/1, and the temperature of the dispersion reaches 50 ° C. So that it was warmed. While stirring the dispersion, sodium hypochlorite solution 3 Oml was added and stirring was continued for about 3 hours. During this time, the temperature of the solution was kept at 50 ° C to obtain composite oxide particles. (Oxidation treatment)
- the average oxidation number of transition metal elements (N i, Co) contained in the active material particles after the immersion treatment is determined by a known method (after reacting the active material particles with ferrous sulfate ammonium, Perform redox titration with potassium). As a result, the average oxidation number of transition metal elements (Ni, Co) was +2. 17. The value was substituted into the formula for calculating the oxidation number of Ni, and the oxidation number of N'i was calculated as 2.1 and 2.
- Li impregnation treatment in composite oxide particles and determination of Li content 100 g of the composite oxide particles subjected to the oxidation treatment was added to a mixed aqueous solution of NaOH and LiOH containing 4.5 mol / l NaOH and 0.8 mo1 Z1 LiOH for 3 hours. Soaked for a while. During this time, the temperature of the solution was kept at 50 ° C., and the solution was stirred gently. After removing the solution adhering to the particle surface by centrifuging the particles obtained in the next step, the resulting composite oxide particles are dispersed in 40 Om 1 pure water and decantation (decantation). Washed with water. It was repeatedly washed with water until the pH of the finished liquid dropped to 11 and then dried. When the composite oxide particles were subjected to atomic absorption analysis and the amount of Li contained in the composite oxide particles was quantified, the amount of Li was 0. lw t.%.
- Example 23 The nickel electrode original plate was cut to form a cylindrical nickel-metal hydride battery in the same manner as in Example 8 to obtain a cylindrical nickel-metal hydride battery having a nickel electrode filling capacity of 1980 mAh. This example is referred to as Example 23.
- Ten pre-formed storage batteries were prepared and charged at an ambient temperature of 20 ° C.
- the battery was charged for 6 hours at a charge rate of 0.2 ItA (396mA).
- the battery was discharged at an ambient temperature of 20 ° C with a rate of 0.2 It A (396 mA) and a discharge cut voltage of 1.0 V.
- the average discharge voltage (V) and discharge capacity (mAh) in the charge / discharge were examined.
- Example 18 the active material particle for nickel electrode provided with the core layer particle in which Mg shown in Example 23 was dissolved was applied as the positive electrode active material particle. Otherwise, the nickel electrode evaluation cell and the cylindrical nickel hydride secondary battery had the same configuration as in Example 18. This example is referred to as Example 26.
- Table 8 shows the test results of the cylindrical nickel hydride secondary batteries according to Examples 23 to 26 in combination with Example 8. Table 8
- Example 23 in which Mg was dissolved in the positive electrode active material particles, had higher average discharge voltage and discharge capacity than Example 8.
- the cylindrical nickel hydride secondary battery according to Example 26 is further improved in charging efficiency when charged at a high ambient temperature of 40 ° C. as compared with Example 23 and Example 25. ing.
- Example 26 when the heavy rare earth element (Y b) compound particles are mixed and added to the positive electrode active material particles, the charging efficiency is further remarkably increased when charging is performed at an ambient temperature of 40 ° C. It seems to have improved. Also, it is considered that the average discharge voltage was increased by adding Mg to the nickel electrode active material particles.
- the viscosity of the active material paste In order to apply the active material paste to the substrate, the viscosity of the active material paste must be at least 20 million millipascals (m Pa ⁇ s), and 1 5 0 0 O m P a ⁇ s or less is desirable, but in Example 8, in the production of the active material paste for producing the nickel electrode, carboxymethylcellulose (CMC), which has been widely used as a thickener in the past.
- CMC carboxymethylcellulose
- the core layer contains high-order nickel hydroxide as a main component.
- the surface layer is made of a higher-order cobalt compound, the oxidizing power is strong, and the CMC is activated by the oxidizing power and the alkaline component of the active material particles because of the inclusion of an alkaline component during the synthesis of the active material. It is thought that the paste viscosity decreased due to oxidative decomposition by the material particles.
- Example 8 in which xanthan gum was applied as a thickener, the paste viscosity was 60 0 O m Pa ⁇ s immediately after the paste adjustment, and the above requirement was satisfied.
- Xanthan gum is superior in alkali resistance and oxidation resistance compared to CMC, so it is an active material particle containing lithium, and has a higher order nickel compound on the surface with higher order nickel hydroxide as the core layer. It is considered that an active material paste having a stable viscosity for a long time was obtained even in an active material paste to which active material particles having strong oxidizing power were applied.
- xanthan gum was applied as a thickener.
- wean gum is applied instead of xanthan gum, an active material paste having a small viscosity change with time can be obtained in the same manner as when xanthan gum is applied.
- the second embodiment shown here is a method in which the oxidation treatment of particles mainly composed of nickel hydroxide and the Li impregnation treatment are performed in one step before the production of the nickel electrode ((8 See)).
- the temperature of the reaction bath (Li impregnation and oxidation treatment liquid) for oxidizing the active material particles for nickel electrode the concentration of LiOH contained in the Li impregnation and oxidation treatment liquid, and the treatment time
- the processing conditions such as constant, an active material having a specific lithium content ratio can be obtained.
- the particles can be electrolytically oxidized and simultaneously impregnated with Li.
- Na O H and K O H may coexist in addition to Li O H.
- the surface layer is mainly composed of particles containing Ni (OH) 2 as a main component or a lower cobalt compound such as Co (OH) 2 on the surface.
- Particles containing Ni (OH) 2 as the main component In the process of oxidation using an oxidizing agent in the presence of, by adding LiOH to the reaction bath for oxidation, the particles can be oxidized and impregnated with Li (solid solution) at the same time. This method is preferable because Li can be impregnated without adding a new process.
- Ammonium complex was formed by adding ammonium sulfate and aqueous potassium hydroxide solution to an aqueous solution in which nickel sulfate, zinc sulfate, and cobalt sulfate were dissolved so that each metal hydroxide had the mass ratio described below. . While stirring the reaction system vigorously, further potassium hydroxide solution was added dropwise, the temperature of the reaction bath was controlled to 45 ⁇ 2 ° C, pH was controlled to 12 ⁇ 0.2, and the average particle size was 10 ⁇ m.
- the obtained particles were put into an aqueous NaOH solution having a concentration of 35 wt% and a temperature of 100 ° C., and stirred while maintaining the temperature for 1 hour. Next, the aqueous NaOH solution was filtered off, washed with water and dried. The ratio of the surface layer of the obtained composite hydroxide particles was 7 wt% with respect to the core layer mother particles (hereinafter simply referred to as the core layer).
- 100 g of the particles after the surface layer is formed is dispersed in 400 g of a mixed aqueous solution containing NaOH 4.5 M / 1 and LiO HI. 2M / 1, and the temperature of the dispersion is Heated to 50 ° C. While stirring the dispersion, sodium hypochlorite 30 ml of solution was added and stirring was continued for about 3 hours. During this time, the temperature of the solution was kept at 50 ° C. Thereafter, the dispersion was heated and the temperature of the dispersion was maintained at 90 ° C. for 1 hour. After the particles of the dispersion liquid were filtered off, the obtained active material particles were washed with water by the decantation method and dried until the pH of the supernatant was 11 as in Example 1.
- Example 27 The average oxidation number and Li content ratio of Ni and Co contained in the active material particles were determined in the same manner as in Example 1. The average oxidation number of Ni and Co in the obtained active material particles was 2.15, and the Li content ratio was 0.2 wt%.
- a nickel electrode original plate was prepared in the same manner as in Example 1 by applying the nickel electrode active material particles. The original nickel electrode plate was cut to form a cylindrical nickel-metal hydride storage battery in the same manner as in Example 1. This example is referred to as Example 27.
- Li may be allowed to enter the active material particles by containing Li + in the active material paste using a surface layer having a main component (see (9) above). reference).
- lithium hydroxide can be allowed to enter the active material particles by dissolving lithium hydroxide in the electrolyte, the solubility of lithium hydroxide in the electrolyte is low and the electrolyte is injected into the battery. Since the amount is limited, there is a drawback that a predetermined amount of lithium cannot be secured.
- active material particles composite oxide particles: particles consisting of a high-order nickel hydroxide core layer and a high-order cobalt compound surface layer
- active material particles that were not impregnated with lithium in the process of preparing the two-dicel electrode were applied. did.
- An active material paste was obtained by mixing as 0.4.
- the paste was filled in foamed nickel in the same manner as in Example 1 and then dried in an air atmosphere at an ambient temperature of 100 ° C. for 3 hours. After drying, pressure was applied in the same manner as in Example 1 to obtain a nickel electrode original plate.
- the nickel electrode original plate was cut and the active material particles were sampled.
- the active material particles obtained by sampling were washed with water by applying a decantation method until the pH of the supernatant liquid became 11, and then dried, and the ratio of lithium contained in the active material particles was determined. 2 2%.
- the nickel electrode original plate was cut to form a cylindrical nickel hydride secondary battery in the same manner as in Example 1. This example is referred to as Example 28. Fourth embodiment
- an active material paste is applied to a conductive substrate and dried to prepare an electrode, and then impregnated with an aqueous solution containing lithium ions so that lithium is contained in the active material particles.
- Method see (1 1) above.
- This method has an advantage that the amount of lithium contained in the active material can be easily controlled by controlling the concentration of lithium hydroxide in the impregnating liquid and the amount of the impregnating liquid.
- Example 29 an electrode plate was prepared using composite oxide particles that had been subjected to oxidation treatment. However, after preparing an electrode plate using composite hydroxide particles that had not been subjected to oxidation treatment, The composite hydroxide can be oxidized to a composite oxide by electrolytic oxidation of the electrode plate.
- Example 28 paste obtained by applying active material particles (composite particles) not impregnated with Li in the nickel electrode preparation process was filled in expanded nickel and then dried. .
- the dried electrode plate is impregnated with 2.5 g of 5 wt% lithium hydroxide aqueous solution per 100 cm 2 of electrode plate, then kept at 60 ° C for 3 hours in an air atmosphere, dried, and pressurized.
- a nickel electrode original plate was obtained.
- the nickel electrode original plate was cut and the active material particles were sampled.
- the active material particles obtained by sampling were washed with water by applying decantation until the pH of the finished liquid reached 11 and then dried, and the ratio of Li contained in the active material particles was determined. It was 24%.
- the original nickel electrode plate was cut to form a cylindrical nickel hydride secondary battery in the same manner as in Example 1. This example is referred to as Example 29.
- Table 9 shows the test results of the cylindrical nickel hydride secondary batteries according to Example 27 to Example 29.
- each of Example 27 to Example 29 has a higher discharge capacity and cycle life than Comparative Example 1 in which the nickel electrode active material does not contain Li. It was found that the nickel electrode active material mainly composed of high-order nickel hydroxide formed in advance has characteristics not inferior to those of Example 1 in which treatment for adding Li was performed. From this, it was found that any of the methods for adding Li to the nickel electrode active material shown in Examples 27 to 29 is effective. Fifth embodiment
- the active material paste instead of the L i OH, L i carbonates (L i 2 C0 3), sulfates (L i 2 S 0 4 ), nitrates (L i NOs), phosphates (L i 3 .P0 4 ), acetates (CH 3 COOL i), halides (L i F, L i C l, L i B r) Add at least one of these compounds.
- Polysaccharides such as xanthan gum and uelan gum can be used in addition to carboxymethyl senorelose (CMC) and methinoresen relose (MC) as thickeners for nickel electrode active material paste.
- CMC and MC are In a system with poor potency and coexistence with Al force, the thickener decomposes and the viscosity change of the paste is large. Xanthan gum and melane gum are more resistant to alkali than CMC and MC, so the change in paste viscosity over time is suppressed. However, when the paste is left for a long time, the viscosity is unavoidable. If the viscosity of the active material paste decreases, there is a risk that the paste will flow down from the substrate when the electrode plate filled with the paste is dried, and the active material filling amount may be reduced. There is a possibility that the variation in the amount of the active material is increased.
- the viscosity of the active material pace cocoon decreases over time. This is suppressed.
- Example 28 instead of the active material particles (composite oxide particles) alone in the process of preparing the nickel electrode, mixed particles of 98 parts by weight of the active material particles and 2 parts by weight of erbium hydroxide ⁇ Yb (OH) 3 ⁇ Applied. Otherwise, a nickel electrode was produced in the same manner as in Example 28.
- the nickel plate original plate was cut and mixed particles of active material particles and erbium hydroxide were sampled.
- the mixed particles obtained by sampling were washed with water by applying the decantation method until the pH of the supernatant reached 11 and then dried, and the proportion of lithium contained in the mixed particles was determined. 2%.
- the nickel electrode original plate was cut to form a cylindrical nickel hydride secondary battery in the same manner as in Example 28.
- the discharge capacity when charged at 20 ° C and 60 ° C and the charging efficiency at 60 ° C were obtained. This example is referred to as Example 30.
- Example 30 in place of the aqueous solution containing xanthan gum and 3 wt% of L i OH in 0. 6 wt%, 0 '. It was applied an aqueous solution containing 6 wt% of xanthan gum and 6 wt% of L i 2 SO . Otherwise, a nickel electrode was produced in the same manner as in Example 30. The ratio of lithium contained in the mixed particles was determined in the same manner as in Example 30. However, it was 0.2%. The nickel electrode original plate was cut to form a cylindrical nickel hydride secondary battery in the same manner as in Example 30. In addition, the discharge capacity when charged at 20 ° C and 60 ° C and the charging efficiency at 60 ° C were determined. This example is referred to as Example 31.
- Example 30 instead of an aqueous solution containing 0.6 wt% xanthan gum and 3 wt% LiOH, an aqueous solution containing 0.6 wt% xanthan gum and 5 wt% LiCl was applied. Otherwise, a nickel electrode was produced in the same manner as in Example 30. When the ratio of lithium contained in the mixed particles was determined in the same manner as in Example 30, it was 0.2%. The nickel electrode original plate was cut to form a cylindrical nickel hydride secondary battery in the same manner as in Example 30. In addition, the discharge capacity when charged at 20 ° C and 60 ° C and the charging efficiency at 60 ° C were determined. This example is referred to as Example 32. Table 10 shows the test results of the batteries according to Example 30 to Example 32.
- Example 31 and Example 32 the discharge capacity and 60 ° C charge efficiency were not inferior to those in Example 30. It has been found that the same effect can be obtained even when Li 2 S0 4 or Li C 1 is used instead of OH.
- the active material paste of Examples 30 to 32 and the Li impregnation reagent were not added, and the Li impregnation reagent was added to Li OH, Li 2 S0 4 and Li C 1
- the active material when the active material using Li 2 CO 3 , CH 3 COOL i, Li N0 3 , Li Br, Li F, and Li 3 PO 4 is left at an ambient temperature of 20 ° C.
- Paste viscosity of paste The measurement was performed over time from the production of the test piece.
- Example 30 After leaving the active material pastes of Example 30 to Example 32 for 3 hours at an ambient temperature of 20 ° C., the paste was stirred so that the paste composition was uniform, and 200 positive electrode plates were produced using the paste. The degree of variation in the active material filling amount was examined. Although detailed results are omitted, the difference between the maximum value and the minimum value of the active material filling amount when the active material paste of Example 30 was used was about 5%, whereas Example 31 and Example In 32, the difference was less than 1%, and the variation in filling amount was small. In the case of Example 1, when the paste was allowed to stand for 3 hours, the paste viscosity decreased and solid-liquid separation occurred in the paste, resulting in a large variation in the active material filling amount.
- L i compounds impregnated in the nickel electrode plate in place of the L i OH, L i 2 C0 3, L i 2 S0 4, Impregnated with at least one compound selected from the group consisting of L i N0 3 , L i 3 PO 4, CHsCOOL i, L i F, L i C l and L i Br.
- the application of Li 2 S ⁇ 4, Li 3P O4, CH 3 COL i, Li F, Li Cl, and Li Br is the conductivity of the electrolyte. This is preferable because there is no possibility of lowering the pressure or promoting self-discharge.
- Example 29 mixed particles of 98 parts by weight of the active material particles and 2 parts by weight of ytterbium hydroxide ⁇ Yb (OH) were used instead of the active material particles (composite oxide particles) alone in the process of producing the nickel electrode.
- a cylindrical nickel hydrogen battery was produced in the same manner as in Example 29, and the discharge capacity and the charge efficiency at 60 ° C. when charged at 20 ° C. and 60 ° C. were determined. This example is referred to as Example 33.
- Example 33 in place of the 5 wt% aqueous solution of lithium hydroxide was applied 10w t% L i 2 SO 4 aqueous solution. Otherwise, a cylindrical nickel-metal hydride battery was prepared in the same manner as in Example 33, and the discharge capacity and the 60 ° C charging efficiency when charging at 20 ° C and 60 ° C were determined. This example is referred to as Example 34.
- Example 33 a 7 wt% LiCl aqueous solution was applied in place of the 5 wt% lithium hydroxide aqueous solution. Otherwise, a cylindrical nickel-metal hydride battery was prepared in the same manner as in Example 33, and the discharge capacity and 60 ° C charging efficiency when charging at 20 ° C and 60 ° C were determined. This example is referred to as Example 35.
- the test results of the batteries according to Example 33 to Example 35 are shown in Table 11. Examples The nickel electrode plates after drying according to 33 to Example 35 were simultaneously left in a temperature of 25 ° C. and a relative humidity of 70% RH for 1 hour (15 hours), and the change in the weight of the electrode plates was examined.
- Example 33 when the electrode plate according to Example 33 was dried and left in the atmosphere, an increase in the weight of the electrode plate, which seems to be due to moisture absorption or carbon dioxide absorption, was observed, whereas Examples 34 and 35. Even when the electrode plate according to the invention was dried and left in the atmosphere, almost no change in weight was observed. In Examples 33 to 35, since the battery was assembled immediately after leaving the electrode without leaving the electrode, the battery characteristics were not affected by leaving the nickel electrode. If left untreated, the electrode plate absorbs moisture and / or carbon dioxide gas, which changes the concentration of the electrolyte after battery assembly and may adversely affect battery characteristics.
- Embodiment 5 and Embodiment 6 an example in which an Li 2 SO 4 aqueous solution and an Li C 1 aqueous solution were used as impregnation reagents was shown, but Li 2 CO 3 , CH 3 COOL i, L i F, L i B r and L i 3 P_ ⁇ 4, L i 2 S 0 4 aqueous solution even when the aqueous solution has been the application of, L i C 1 as in the case of aqueous solution was applied good results are obtained .
- the active material powder is immersed in a solution containing alkali metal ions and heat-treated, and the nickel electrode active material is present in the presence of an alkali solution.
- the method of dissolving lithium hydroxide in the oxidation bath during the oxidation process using an oxidizing agent, the method of adding an alkali metal element to the pace tub during the process of preparing the active material paste, the alkali metal on the nickel electrode plate Although the method of impregnating a solution containing ions has been described, other than that, a method of adding alkali metal ions to a reaction bath for depositing a nickel S electrode active material containing nickel hydroxide as a main component can also be applied.
- the zinc content in the active material particles is preferably 2 to 4 wt%.
- the zinc content is within this range. This range is set based on the experimental fact that when the content is less than 2 wt%, the effect of adding zinc is not sufficient, and when the content exceeds 4 wt%, the utilization factor of the active material is extremely reduced. It is a thing. Industrial applicability
- the present invention improves the discharge capacity, high rate discharge characteristics, and charge / discharge cycle life of an alkaline secondary battery using a nickel electrode such as a nickel hydride secondary battery or a nickel-powered dome battery as a positive electrode. It is highly valuable.
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- Composite Materials (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006549075A JP5099479B2 (ja) | 2004-12-17 | 2005-12-16 | アルカリ二次電池用ニッケル電極及びその製造方法並びにアルカリ二次電池 |
CN2005800435411A CN101080831B (zh) | 2004-12-17 | 2005-12-16 | 碱二次电池用镍电极及其制造方法以及碱二次电池 |
US11/793,203 US8057934B2 (en) | 2004-12-17 | 2005-12-16 | Nickel electrode for alkaline secondary battery and alkaline secondary battery |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004-365178 | 2004-12-17 | ||
JP2004365178 | 2004-12-17 | ||
JP2005025692 | 2005-02-01 | ||
JP2005-025692 | 2005-02-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2006064979A1 true WO2006064979A1 (ja) | 2006-06-22 |
Family
ID=36588009
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2005/023689 WO2006064979A1 (ja) | 2004-12-17 | 2005-12-16 | アルカリ二次電池用ニッケル電極及びその製造方法並びにアルカリ二次電池 |
Country Status (4)
Country | Link |
---|---|
US (1) | US8057934B2 (ja) |
JP (1) | JP5099479B2 (ja) |
CN (1) | CN101080831B (ja) |
WO (1) | WO2006064979A1 (ja) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110117434A1 (en) * | 2008-07-09 | 2011-05-19 | Sanyo Electric Co., Ltd. | Positive electrode active material for non-aqueous electrolyte secondary battery, fabrication method thereof, positive electrode for non-aqueous electrolyte secondary battery, and non-aqueous electrolyte secondary battery |
WO2012096294A1 (ja) | 2011-01-11 | 2012-07-19 | 株式会社Gsユアサ | アルカリ蓄電池用正極活物質、その製造方法およびアルカリ蓄電池 |
WO2013015424A1 (ja) | 2011-07-28 | 2013-01-31 | 株式会社Gsユアサ | アルカリ蓄電池用負極、アルカリ蓄電池用外装缶及びアルカリ蓄電池 |
EP2713428A1 (en) | 2012-09-28 | 2014-04-02 | GS Yuasa International Ltd. | Alkaline storage battery and positive electrode material for alkaline storage battery |
EP2713425A1 (en) | 2012-09-28 | 2014-04-02 | GS Yuasa International Ltd. | Alkaline storage battery, positive electrode material for alkaline storage battery, and method for manufacturing positive electrode material for alkaline storage battery |
US8877372B2 (en) | 2011-01-11 | 2014-11-04 | Gs Yuasa International Ltd. | Alkaline secondary battery |
US8883349B2 (en) | 2010-08-05 | 2014-11-11 | Gs Yuasa International Ltd. | Alkaline secondary battery and method for manufacturing positive electrode material for alkaline secondary battery |
JP2019040684A (ja) * | 2017-08-23 | 2019-03-14 | トヨタ自動車株式会社 | 非水系二次電池 |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010030131A2 (ko) * | 2008-09-10 | 2010-03-18 | 주식회사 엘지화학 | 리튬 이차전지용 양극 활물질 |
CN101728531B (zh) * | 2009-11-28 | 2011-11-02 | 内蒙古科技大学 | 镍氢动力电池正极材料及制备方法 |
JP5675113B2 (ja) * | 2010-01-06 | 2015-02-25 | 三洋電機株式会社 | 非水電解質二次電池及び非水電解質二次電池用正極 |
CN111564623A (zh) * | 2020-04-29 | 2020-08-21 | 湖南科霸汽车动力电池有限责任公司 | 镍氢动力电池正极浆料 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000223119A (ja) * | 1999-01-29 | 2000-08-11 | Sanyo Electric Co Ltd | アルカリ蓄電池用正極活物質およびその製造方法ならびにこの正極活物質を用いたアルカリ蓄電池用正極の製造方法 |
JP2000294234A (ja) * | 1999-04-07 | 2000-10-20 | Sanyo Electric Co Ltd | ニッケル水素蓄電池及びその製造方法 |
JP2001006679A (ja) * | 1999-06-17 | 2001-01-12 | Sanyo Electric Co Ltd | アルカリ蓄電池用ニッケル極及びアルカリ蓄電池 |
JP2001052694A (ja) * | 1999-08-04 | 2001-02-23 | Sakai Chem Ind Co Ltd | アルカリ蓄電池正極活物質用コバルト固溶水酸化ニッケル粉末とその製造方法 |
JP2002279992A (ja) * | 2001-03-19 | 2002-09-27 | Yuasa Corp | アルカリ蓄電池用ニッケル電極およびアルカリ蓄電池 |
JP2004259515A (ja) * | 2003-02-25 | 2004-09-16 | Yuasa Corp | ニッケル電極用増粘剤、ニッケル電極及びその製造方法、並びに、アルカリ蓄電池 |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1552109A (en) * | 1925-02-09 | 1925-09-01 | Harold W Boyd | Pavement |
JP3448510B2 (ja) * | 1998-04-28 | 2003-09-22 | 三洋ジ−エスソフトエナジー株式会社 | アルカリ電池用水酸化ニッケル粉末およびこれを用いた水酸化ニッケル電極 |
EP1424741A4 (en) * | 2001-09-03 | 2006-10-04 | Yuasa Battery Co Ltd | NICKEL ELECTRODE MATERIAL AND MANUFACTURING METHOD AND NICKEL ELECTRODE AND ALKALINE BATTERY |
-
2005
- 2005-12-16 WO PCT/JP2005/023689 patent/WO2006064979A1/ja not_active Application Discontinuation
- 2005-12-16 US US11/793,203 patent/US8057934B2/en active Active
- 2005-12-16 CN CN2005800435411A patent/CN101080831B/zh active Active
- 2005-12-16 JP JP2006549075A patent/JP5099479B2/ja active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000223119A (ja) * | 1999-01-29 | 2000-08-11 | Sanyo Electric Co Ltd | アルカリ蓄電池用正極活物質およびその製造方法ならびにこの正極活物質を用いたアルカリ蓄電池用正極の製造方法 |
JP2000294234A (ja) * | 1999-04-07 | 2000-10-20 | Sanyo Electric Co Ltd | ニッケル水素蓄電池及びその製造方法 |
JP2001006679A (ja) * | 1999-06-17 | 2001-01-12 | Sanyo Electric Co Ltd | アルカリ蓄電池用ニッケル極及びアルカリ蓄電池 |
JP2001052694A (ja) * | 1999-08-04 | 2001-02-23 | Sakai Chem Ind Co Ltd | アルカリ蓄電池正極活物質用コバルト固溶水酸化ニッケル粉末とその製造方法 |
JP2002279992A (ja) * | 2001-03-19 | 2002-09-27 | Yuasa Corp | アルカリ蓄電池用ニッケル電極およびアルカリ蓄電池 |
JP2004259515A (ja) * | 2003-02-25 | 2004-09-16 | Yuasa Corp | ニッケル電極用増粘剤、ニッケル電極及びその製造方法、並びに、アルカリ蓄電池 |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110117434A1 (en) * | 2008-07-09 | 2011-05-19 | Sanyo Electric Co., Ltd. | Positive electrode active material for non-aqueous electrolyte secondary battery, fabrication method thereof, positive electrode for non-aqueous electrolyte secondary battery, and non-aqueous electrolyte secondary battery |
US8741483B2 (en) * | 2008-07-09 | 2014-06-03 | Sanyo Electric Co., Ltd. | Positive electrode active material for non-aqueous electrolyte secondary battery having rare earth hydroxide and/or oxyhydroxide |
US9929401B2 (en) | 2008-07-09 | 2018-03-27 | Sanyo Electric Co., Ltd. | Positive electrode active material for non-aqueous electrolyte secondary battery having rare earth hydroxide and/or oxyhydroxide |
US8883349B2 (en) | 2010-08-05 | 2014-11-11 | Gs Yuasa International Ltd. | Alkaline secondary battery and method for manufacturing positive electrode material for alkaline secondary battery |
WO2012096294A1 (ja) | 2011-01-11 | 2012-07-19 | 株式会社Gsユアサ | アルカリ蓄電池用正極活物質、その製造方法およびアルカリ蓄電池 |
US8877372B2 (en) | 2011-01-11 | 2014-11-04 | Gs Yuasa International Ltd. | Alkaline secondary battery |
US9269952B2 (en) | 2011-01-11 | 2016-02-23 | Gs Yuasa International Ltd. | Positive active material for alkaline secondary battery, method for manufacturing the same and alkaline secondary battery |
WO2013015424A1 (ja) | 2011-07-28 | 2013-01-31 | 株式会社Gsユアサ | アルカリ蓄電池用負極、アルカリ蓄電池用外装缶及びアルカリ蓄電池 |
EP2713428A1 (en) | 2012-09-28 | 2014-04-02 | GS Yuasa International Ltd. | Alkaline storage battery and positive electrode material for alkaline storage battery |
EP2713425A1 (en) | 2012-09-28 | 2014-04-02 | GS Yuasa International Ltd. | Alkaline storage battery, positive electrode material for alkaline storage battery, and method for manufacturing positive electrode material for alkaline storage battery |
US9419273B2 (en) | 2012-09-28 | 2016-08-16 | Gs Yuasa International Ltd. | Alkaline storage battery, positive electrode material for alkaline storage battery, and method for manufacturing positive electrode material for alkaline storage battery |
JP2019040684A (ja) * | 2017-08-23 | 2019-03-14 | トヨタ自動車株式会社 | 非水系二次電池 |
Also Published As
Publication number | Publication date |
---|---|
US8057934B2 (en) | 2011-11-15 |
CN101080831A (zh) | 2007-11-28 |
CN101080831B (zh) | 2011-06-15 |
JPWO2006064979A1 (ja) | 2009-05-14 |
JP5099479B2 (ja) | 2012-12-19 |
US20080166635A1 (en) | 2008-07-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2006064979A1 (ja) | アルカリ二次電池用ニッケル電極及びその製造方法並びにアルカリ二次電池 | |
CN101939863B (zh) | 用于可再充电的镍锌电池的涂膏氢氧化镍电极 | |
JP3191751B2 (ja) | アルカリ蓄電池及びその正極活物質の表面処理方法 | |
JP4321997B2 (ja) | アルカリ蓄電池用正極活物質ならびにそれを用いた正極およびアルカリ蓄電池 | |
WO2012096294A1 (ja) | アルカリ蓄電池用正極活物質、その製造方法およびアルカリ蓄電池 | |
JP4412936B2 (ja) | オキシ水酸化コバルトおよびその製造方法ならびにそれを用いたアルカリ蓄電池 | |
CN113314770B (zh) | 一种碱性二次电池及其制备方法 | |
Zhang et al. | Lead sulfate used as the positive active material of lead acid batteries | |
JP3617203B2 (ja) | ニッケル水素二次電池の製造方法 | |
JP2002216752A (ja) | コバルト化合物およびその製造方法ならびにそれを用いたアルカリ蓄電池用正極板およびアルカリ蓄電池 | |
Bui et al. | Hydrothermal preparation of Fe2O3 nanoparticles for Fe-air battery anodes | |
JP5743185B2 (ja) | アルカリ蓄電池用正極活物質およびアルカリ蓄電池 | |
JP4569068B2 (ja) | ニッケル電極用増粘剤、ニッケル電極及びその製造方法、並びに、アルカリ蓄電池 | |
JP2003523481A (ja) | コバルトオキシヒドロキシドの電気化学的合成 | |
JP4908716B2 (ja) | アルカリ蓄電池およびアルカリ蓄電池用ニッケル電極、ニッケル電極用活物質粉末。 | |
JP3744642B2 (ja) | ニッケル−金属水素化物蓄電池及びその製造方法 | |
CN107403932B (zh) | 电池用正极、其制备方法以及具有该正极的电池 | |
JP2003249215A (ja) | アルカリ蓄電池用正極活物質の製造方法およびこの製造方法にて得られた正極活物質を用いたアルカリ蓄電池 | |
JP2003077468A (ja) | ニッケル電極材料の製造方法 | |
CN103426635A (zh) | 负极集流体的制备方法 | |
JP3895985B2 (ja) | ニッケル・水素蓄電池 | |
JP4120752B2 (ja) | ニッケル水素蓄電池 | |
JP2003068293A (ja) | 非焼結式正極、その製造方法および前記正極を用いたアルカリ蓄電池 | |
JP3744306B2 (ja) | アルカリ蓄電池用燒結式ニッケル電極の製造法 | |
JP3691257B2 (ja) | アルカリ蓄電池用焼結式カドミウム負極の製造方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KM KN KP KR KZ LC LK LR LS LT LU LV LY MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU LV MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2006549075 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 11793203 Country of ref document: US Ref document number: 200580043541.1 Country of ref document: CN |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 05820250 Country of ref document: EP Kind code of ref document: A1 |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 5820250 Country of ref document: EP |