• 专利附录
  • 专利说明
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  • 类似技术
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    • 专利摘要:
    In the present invention, a compound represented by the formula Li x M y PO 4 (wherein x is in the range of O <x? 2, y is in the range of 0.8? Y? 1.2 and M is in the 3d transition metal) By using this positive electrode active material containing Li x M y PO 4 having a particle diameter of 10 m or less in the nonaqueous electrolyte secondary battery, excellent cycle characteristics and high capacity can be realized.
    公开号:KR20010025117A
    申请号:KR1020007013776
    申请日:2000-03-28
    公开日:2001-03-26
    发明作者:아쯔오 야마다；구오화 리；히데또 아즈마
    申请人:이데이 노부유끼；소니 가부시끼 가이샤；
    IPC主号:
    专利说明:

    BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a positive electrode active material, a nonaqueous electrolyte secondary battery, and a method for manufacturing a positive electrode active material,
    BACKGROUND ART [0002] In recent years, research on rechargeable secondary batteries as a battery that can be conveniently and economically used for a long time along with the remarkable progress of various electronic devices has been made. BACKGROUND ART [0002] Lead secondary batteries are known as lead-acid batteries, alkaline secondary batteries, and lithium secondary batteries.
    Of the secondary batteries, lithium secondary batteries in particular have advantages such as high output and high energy density. The lithium secondary battery is composed of a positive electrode and a negative electrode having an active material capable of reversibly inserting lithium ions at least, and a nonaqueous electrolyte.
    LiCoO 2 or LiNiO 2 as a positive electrode active material of such a lithium secondary battery, LiMn 2 O 4 having a positive spinel structure and a space group Fd 3 m, etc. are practically used. However, there is a demand for a cathode active material capable of achieving more economical and stable supply, stability, high capacity and good cycle characteristics.
    At present, as a cathode active material of a lithium secondary battery, a compound having an olivine structure, for example, Li x M y PO 4 (wherein x is in the range of O <x ≦ 2, y is in the range of 0.8 ≦ y ≦ 1.2, Contains a 3d transition metal) is a promising material.
    Among the compounds represented by Li x M y PO 4 , for example, the use of LiFePO 4 as a positive electrode of a lithium ion battery has been proposed in Japanese Patent Laid-Open No. 9-171827.
    LiFePO 4 has a theoretical capacity as large as 170 mAh / g and contains one per one Fe atom which can be electrochemically undoped in an initial state, and thus is a promising material as a cathode active material of a lithium ion battery.
    LiFePO 4 was synthesized by calcining at a relatively high temperature of 800 캜 under a reducing environment by using a ferrous salt such as iron ( III ) chloride Fe (CH 3 COO) 2 as an Fe source to be a starting material for synthesis.
    However, it has been reported in the above-mentioned publication that only an actual capacity of about 60 mAh / g to 70 mAh / g can be obtained in an actual battery constructed using LiFePO 4 synthesized by the above-described synthesis method as a cathode active material. Thereafter, in the Journal of the Electrochemical Society, 144, 1188 (1997), an actual capacity of about 120 mAh / g is reported. Considering that the theoretical capacity is 170 mAh / g, none.
    Comparing LiFePO 4 and LiMn 2 O 4 , LiFePO 4 had a volume density of 3.6 g / cm 3 and an average voltage of 3.4 V, while LiMn 2 O 4 had a volume density of 4.2 g / cm 3 and an average voltage of 3.9 V and has a capacity of 120 mAh / g, LiFePO 4 is 10% smaller in both voltage and volume density than LiMn 2 O 4 . Therefore, if the same capacity is 120 mAh / g, LiFePO 4 has a weight energy density of 10% or more and a volume energy density of 20% or more smaller than that of LiMn 2 O 4 . Because of this, there is in order to achieve the same level or higher energy density and LiMn 2 O 4 as a LiFePO 4 requires 140 mAh / g or more of capacity, roneun LiFePO 4 was not achieved such a high dose so far.
    In addition, LiFePO 4 synthesized by firing at a relatively high temperature of 800 ° C may undergo excessive crystallization and interfere with the diffusion of lithium. For this reason, the nonaqueous electrolyte secondary battery can not obtain a sufficiently high capacity. The higher the temperature at the time of firing, the more energy is consumed and the load on the reactor is also increased.
    DISCLOSURE OF THE INVENTION &lt;
    Disclosed is a positive electrode active material which realizes a high capacity when used in a battery, and a nonaqueous electrolyte secondary battery using the positive electrode active material.
    In order to accomplish the above object, the cathode active material of the present invention has the formula Li x M y PO 4 wherein x is in the range of O <x 2, y is in the range of 0.8 Y 1.2, M is the 3d transition metal , And Li x M y PO 4 has a particle diameter of 10 탆 or less.
    The cathode active material of the present invention constituted as described above contains Li x M y PO 4 having a particle diameter of 10 μm or less. Thus, the positive electrode active material has a particle size distribution such that, for example, lithium, which is a charge carrier, can be sufficiently diffused in the positive electrode active material particle.
    In addition, the cathode active material of the present invention has a composition represented by the general formula Li x (Fe y M 1-y ) PO 4 wherein x is in the range of 0.9 X 1.1, y is in the range of 0 <y 1, And Li x (Fe y M 1-y ) PO 4 is a compound having an isomer shift value of not less than 0.1 mm / sec and not more than 0.7 mm / sec in a spectrum obtained by Mössbauer spectroscopy And A / B is less than 0.3 when the area intensity of the spectrum in the range in which the isomer shift value is in the range of 0.8 mm / sec to 1.5 mm / sec is B .
    Since the cathode active material of the present invention having the above-described structure has an A / B ratio of less than 0.3, the presence of an electrochemically inactive impurity is small and a high capacity is realized.
    Also, the nonaqueous electrolyte secondary battery of the present invention is a non-aqueous electrolyte secondary battery having a structure Li x M y PO 4 (in which x is in the range of O <x 2 and y is in the range of 0.8 Y 1.2 And M is a transition metal), a negative electrode having a negative electrode active material capable of reversibly doping / undoping lithium, and a nonaqueous electrolyte secondary battery having a nonaqueous electrolyte. , Li x M y PO 4 has a particle diameter of 10 탆 or less.
    The nonaqueous electrolyte secondary battery of the present invention constituted as described above contains Li x M y PO 4 having a particle diameter of 10 μm or less as a cathode active material. The positive electrode active material has a particle size distribution such that lithium as a charge carrier can be sufficiently diffused in the particles. Accordingly, a non-aqueous electrolyte secondary battery having a high capacity can be realized.
    Also, the non-aqueous electrolyte secondary battery of the present invention is a non-aqueous electrolyte secondary battery comprising a Li x (Fe y M 1 -y ) PO 4 wherein x is in the range of 0.9 X 1.1 and y is 0 &lt; y &lt; = 1 and M is a divalent transition metal), a negative electrode having a negative electrode active material capable of reversibly doping / undoping lithium, and a nonaqueous electrolyte Li x (Fe y M 1-y ) PO 4 in the nonaqueous electrolyte secondary battery having a non-aqueous electrolyte secondary cell according to the present invention is characterized in that in the spectrum obtained by the Mössbauer spectroscopy, the isomeric shift value is in the range of 0.1 mm / sec to 0.7 mm / The area strength of the spectrum is A and the area strength of the spectrum in which the isomer shift value is in the range of 0.8 mm / sec to 1.5 mm / sec is B, the A / B is less than 0.3.
    The nonaqueous electrolyte secondary battery of the present invention constituted as described above contains a positive electrode active material having an A / B ratio of less than 0.3 and less electrochemically inactive impurities. As a result, a nonaqueous electrolyte secondary battery having a high capacity can be realized.
    It is another object of the present invention to provide a method for producing a positive electrode active material which realizes a high capacity when used in a battery.
    In order to accomplish the above object, the present invention provides a method for producing a cathode active material, comprising the steps of: Li x M y PO 4 wherein x is in the range of O <x 2, y is in the range of 0.8 Y A transition metal is contained), and a calcination step in which the precursor obtained in the mixing step is calcined and reacted. In the calcination step, the precursor is calcined at a temperature of 400 ° C or more and 700 ° C or less And calcining the precursor at a range of temperatures.
    In the method for producing a cathode active material of the present invention, the precursor of Li x M y PO 4 is sintered at a temperature in the range of 400 ° C to 700 ° C in the sintering process. As a result, the chemical reaction and the crystallization proceed uniformly and the crystallization does not proceed excessively, so that a single phase Li x M y PO 4 free of impurities is obtained. Also, the powder characteristics of Li x M y PO 4 change dramatically depending on the difference in temperature at which the precursor of Li x M y PO 4 is sintered in the sintering process.
    The present invention relates to a cathode active material capable of reversibly doping / undoping lithium, a nonaqueous electrolyte secondary battery using the cathode active material, and a method for producing a cathode active material.
    1 is a sectional view showing a configuration example of a nonaqueous electrolyte secondary battery to which the present invention is applied.
    2 is a characteristic graph showing a powder X-ray diffraction pattern of LiFePO 4 synthesized in Samples 1 to 5.
    3 is a characteristic chart showing the relationship between the sintering temperature of LiFePO 4 synthesized in Samples 1 to 5 and the charge / discharge capacity of a battery.
    4 is a characteristic diagram showing the relationship between the calcination temperature and the volume particle size distribution of LiFePO 4 synthesized in Samples 1 to 5. Fig.
    5 is a characteristic diagram showing the relationship between the sample 1 to the firing temperature of the LiFePO 4 synthesized in samples 5 and the volume cumulative diameter.
    6 is a characteristic diagram showing the relationship between the sintering temperature and volume cumulative diameter of LiFePO 4 having a particle diameter in the range of 0.1 탆 to 10 탆 synthesized in Samples 1 to 5;
    7 is a scanning electron microscope photograph showing the particle shape of LiFePO 4 having a sintering temperature of 500 ° C.
    8 is a scanning electron microscope photograph showing the particle shape of LiFePO 4 having a firing temperature of 600 캜.
    9 is a scanning electron microscope photograph showing the particle shape of LiFePO 4 with a firing temperature of 700 ° C.
    FIG. 10 is a characteristic diagram showing the BET specific surface area of LiFePO 4 synthesized in Samples 1 to 5. FIG.
    11 is a characteristic diagram showing a powder X-ray diffraction pattern of LiFePO 4 synthesized in Samples 1, 5, and 6. Fig.
    12 is a characteristic diagram showing charge / discharge characteristics of the battery fabricated in Sample 1. Fig.
    13 is a characteristic diagram showing the cycle characteristics of the battery fabricated in Sample 1. Fig.
    14 is a characteristic diagram showing charge / discharge characteristics of the battery fabricated in Sample 5. Fig.
    15 is a characteristic diagram showing charge / discharge characteristics of the battery fabricated in Sample 6. Fig.
    16 is a characteristic diagram showing an X-ray diffraction pattern of Li (Mn 0.6 Fe 0.4 ) PO 4 .
    17 is a graph showing charge / discharge characteristics of a battery fabricated using Li (Mn 0.6 Fe 0.4 ) PO 4 ;
    18 is a view showing the particle size distribution of Li (Mn 0.6 Fe 0.4 ) PO 4 obtained by firing at 600 캜.
    19 is a Mossbauer spectrum of LiFePO 4 of Sample 6 synthesized at a firing temperature of 320 ° C.
    20 is a Mossbauer spectrum of LiFePO 4 of Sample 2 synthesized at a firing temperature of 400 ° C.
    21 is a Mossbauer spectrum of LiFePO 4 of Sample 1 synthesized at a firing temperature of 600 ° C.
    22 is a Mossbauer spectrum of Fe 2+ of LiFePO 4 of Sample 6;
    23 is a Mossbauer spectrum of Fe 3+ of LiFePO 4 of Sample 6;
    24 is a Mossbauer spectrum of Fe 2+ of LiFePO 4 of sample 2. Fig.
    25 is a Mossbauer spectrum of Fe 3+ of LiFePO 4 of Sample 2. Fig.
    26 is a Mossbauer spectrum of Fe 2+ of LiFePO 4 of Sample 1. Fig.
    27 is a Mossbauer spectrum of Fe 3+ of LiFePO 4 of Sample 1. Fig.
    BEST MODE FOR CARRYING OUT THE INVENTION [
    Hereinafter, the present invention will be described in detail with reference to the drawings.
    1, the nonaqueous electrolyte battery 1 according to the present invention includes a negative electrode 2, a negative electrode can 3 for accommodating the negative electrode 2, a positive electrode 4, a positive electrode 4 for receiving the positive electrode 4, A separator 6 disposed between the anode 4 and the cathode 2 and an insulating gasket 7. The cathode can 3 and the anode can 5 are filled with a non-aqueous electrolyte .
    The negative electrode (2) has a negative electrode active material layer containing a negative electrode active material on the negative electrode collector. As the negative electrode current collector, for example, a nickel foil or the like is used.
    As the negative electrode active material, a material capable of doping / dedoping lithium is used. Specifically, metal lithium, a lithium alloy, a lithium-doped conductive polymer, a layered compound (such as a carbon material or a metal oxide) is used.
    As the binder contained in the negative electrode active material layer, known resin materials generally used as a binder for the negative electrode active material layer of this kind of nonaqueous electrolyte battery can be used.
    As the cathode 2, for example, a metal lithium foil serving as a negative electrode active material may be used.
    The cathode can 3 accommodates the cathode 2 and becomes the external cathode of the non-aqueous electrolyte cell 1.
    The positive electrode 4 is formed by forming a positive electrode active material layer containing a positive electrode active material on a positive electrode current collector.
    As the cathode active material, a preparation method will be described later, but it has an olivine structure and has the formula Li x M y PO 4 (where x is in the range of O <x 2, y is in the range of 0.8 Y 1.2, A transition metal is contained).
    Examples of the compound represented by Li x M y PO 4 include Li x Fe y PO 4 , Li x Mn y PO 4 , Li x Co y PO 4 , Li x Ni y PO 4 , Li x Cu y PO 4 , Li x (Fe, Mn) y PO 4, Li x (Fe, Co) y PO 4, Li x (Fe, Ni) y PO 4, Li x (Cu, Mn) y PO 4, Li x (Cu, such as Co) y PO 4, Li x (Cu, Ni) y PO 4, Li x (Mn, Ti) y PO 4, Li x (Mn, Zn) y PO 4, Li x (Mn, Mg) y PO 4 (The composition ratio in () is arbitrary).
    The Li x M y PO 4 includes those having a particle diameter of 10 μm or less. When the Li x M y PO 4, which contains a positive electrode active material does not contain the His particle size of 10 ㎛ or less Li x M y PO 4, since no proper particle size distribution within the particles of the charge carrier of lithium cathode materials It can not be sufficiently diffused.
    It is also preferable that Li x M y PO 4 has a 10% volume cumulative diameter of 1 m or less. When the 10% volume cumulative diameter is larger than 1 占 퐉, the crystallization of Li x M y PO 4 proceeds excessively, and most of the large particles are liable to occupy. For this reason, there is a possibility that lithium as a charge carrier can not be diffused smoothly in the particles of the positive electrode active material.
    It is preferable that Li x M y PO 4 has a Bronard-Emmett-Teller (BET) specific surface area of 0.5 m 2 / g or more. In the case of the positive electrode active material having a large particle diameter, the surface area becomes small. When a large current is supplied under such circumstances, that is, when a large amount of lithium ions are introduced into the active material in a short time, the diffusion of lithium in the active material can not follow the supply of lithium from the outside, and the apparent phase capacitance decreases. Therefore, in order to secure a sufficient capacity even under a large electric current, a technical measure for increasing the specific surface area and further reducing the particle diameter as described above is required.
    By setting the BET specific surface area of Li x M y PO 4 to 0.5 m &lt; 2 &gt; / g or more, the diffusion of lithium in the active material is accelerated, and a sufficient capacity can be secured even under a large current.
    Also, in the compound represented by the chemical formula Li x M y PO 4 , it is preferable that M is a compound containing Fe as a 3d transition metal, that is, a compound represented by the formula Li x (Fe y M 1 -y ) PO 4 1.1, y is in the range of 0 &lt; y &amp;le; 1, and M is the 3d transition metal), the isomer shift value is preferably from 0.1 mm / sec to 0.7 mm / sec in the spectrum obtained by Mossbauer spectroscopy. sec or less and the area strength of the spectrum in which the isomer shift value is in the range of 0.8 mm / sec to 1.5 mm / sec is A / B less than 0.3 use.
    For example, in Li x (Fe y M 1-y ) PO 4 , LiFePO 4 where x is 1 and y is 0 is determined by Mössbauer spectroscopy as a Mössbauer spectrum corresponding to Fe 2+ , This is about 1.2 ㎜ / sec and the quadrupole splitting is about 2.9 ㎜ / sec. Further, when Fe 2+ is oxidized and Fe 3+ is present in LiFePO 4 , a double line having an isomer shift value of 0.1 mm / sec or more and 0.7 mm / sec or less as a Mossbauer spectrum corresponding to Fe 3+ is observed do.
    During the initial charging process, LiFePO 4 is released, and at the same time, Fe 2+ is oxidized to Fe 3+ . If Fe 3+ is contained in LiFePO 4 in the state before the initial charging, the number of electrons contributing to the cell reaction decreases, resulting in a decrease in the charging capacity of the lithium ion secondary battery.
    Since the lithium ion secondary battery uses a material that does not contain Li such as carbon in the cathode, the initial charging capacity determines the subsequent battery capacity. In addition, even in the case where a material containing Li is used for the negative electrode of a lithium ion secondary battery, if the phase containing Fe 3+ is electrochemically inactive, there is a possibility that the capacity of the battery is lowered due to the presence of this inert phase. Therefore, it is preferable that Fe 3+ existing in LiFePO 4 is as small as possible in the initial state before charging.
    The above-mentioned area strength A is present in the amount of Fe 3+ present in LiFePO 4, the area strength B is proportional to the existing amount of Fe 2+ present in the LiFePO 4. Therefore, LiFePO 4 having A / B of less than 0.3 has a small amount of Fe 3+ , and a high capacity of nonaqueous electrolyte secondary battery containing this LiFePO 4 as a cathode active material is realized.
    As the positive electrode current collector, for example, an aluminum foil or the like is used.
    As the binder contained in the positive electrode active material layer, a known resin material generally used as a binder for the positive electrode active material layer of this kind of nonaqueous electrolyte battery can be used.
    The anode can 5 accommodates the anode 4 and becomes the external anode of the non-aqueous electrolyte cell 1.
    The separator 6 separates the positive electrode 4 and the negative electrode 2 from each other. A known material commonly used as a separator of this type of nonaqueous electrolyte battery can be used. For example, a polymer film such as polypropylene is used do. Further, from the relation between the lithium ion conductivity and the energy density, it is necessary that the thickness of the separator is as thin as possible. Specifically, the thickness of the separator is preferably 50 占 퐉 or less, for example.
    The insulating gasket 7 is inserted into the anode can 3 and integrated therewith. This insulating gasket 7 is for preventing leakage of the non-aqueous electrolyte filled in the anode can 3 and the anode can 5.
    As the non-aqueous electrolyte, a solution in which an electrolyte is dissolved in an aprotic non-aqueous solvent is used.
    Examples of the nonaqueous solvent include propylene carbonate, ethylene carbonate, butylene carbonate, vinylene carbonate, -Butyrolactone, sulfolane, 1,2-dimethoxyethane, 1,2- Diethoxyethane, 2-methyltetrahydrofuran, 3-methyl-1,3-dioxolane, methyl propionate, methyl butyrate, dimethyl carbonate, diethyl carbonate, dipropyl carbonate and the like can be used. Particularly, in view of voltage stability, cyclic carbonates such as propylene carbonate and vinylene carbonate, and chain carbonates such as dimethyl carbonate, diethyl carbonate and dipropyl carbonate are used . These non-aqueous solvents may be used singly or in combination of two or more.
    As the electrolyte to be dissolved in the non-aqueous solvent, for example, lithium salts such as LiPF 6 , LiClO 4 , LiAsF 6 , LiBF 4 , LiCF 3 SO 3 and LiN (CF 3 CO 2 ) 2 can be used. Among these lithium salts, it is preferable to use LiPF 6 and LiBF 4 .
    The nonaqueous electrolyte battery 1 using the above-described Li x M y PO 4 as a cathode active material is produced, for example, as follows.
    As the negative electrode 2, first, the negative electrode active material and the binder are dispersed in a solvent to prepare a negative electrode mixture of the slurry. Subsequently, the obtained negative electrode mixture is uniformly coated on a current collector and dried to form a negative electrode active material layer, whereby the negative electrode 2 is produced. As the binder for the negative electrode mixture, a known binder may be used, and additives known as the negative electrode mixture may be added. Further, metal lithium, which is a negative electrode active material, may be used as the negative electrode 2 as it is.
    As the anode 4, Li x M y PO 4 , which is a cathode active material, and a binder are dispersed in a solvent to prepare a slurry cathode mix. Subsequently, the obtained positive electrode mixture is uniformly coated on a current collector and dried to form a positive electrode active material layer, whereby the positive electrode 4 is produced. As the binder for the positive electrode mixture, a known binder may be used, and additives known as a positive electrode mixture may be added.
    A non-aqueous electrolyte is prepared by dissolving an electrolyte salt in a non-aqueous solvent.
    The anode 2 is held in the anode can 3 and the anode 4 is received in the anode can 5 and a separator made of a polypropylene porous film or the like is provided between the cathode 2 and the anode 4. [ (6). The nonaqueous electrolyte solution is injected into the negative electrode can 3 and the positive electrode can 5 and the negative electrode can 3 and the positive electrode can 5 are caulked and fixed via the insulating gasket 7 to complete the nonaqueous electrolyte battery 1 do.
    However, in the method for producing a cathode active material according to the present invention, it has an olivine structure and has the formula Li x M y PO 4 (where x is in the range of 0.9 X 1.1, y is in the range of 0 & is synthesized as the 3d transition compound represented by the box containing the metal), for example, indicating the LiFePO 4 below.
    First, iron acetate (Fe (CH 3 COO) 2 ), ammonium hydrogen phosphate (NH 4 H 2 PO 4 ) and lithium carbonate (Li 2 CO 3 ) are mixed at a predetermined ratio to prepare a precursor do. Here, the starting materials for synthesis are sufficiently mixed. By thoroughly mixing the starting materials for synthesis, the raw materials are uniformly mixed and the contact points are increased, so that it is possible to synthesize LiFePO 4 at a lower temperature than in the prior art.
    Subsequently, this precursor is fired at a predetermined temperature in an inert gas atmosphere such as nitrogen to synthesize LiFePO 4 .
    Conventionally, LiFePO 4 is calcined at a relatively high temperature of, for example, 800 ° C. When the temperature at the time of firing is high, energy is consumed by that much, and the load on the reaction apparatus is also large.
    Thus, it is possible to synthesize LiFePO 4 at a much lower temperature than the conventional 800 ° C, for example, at 300 ° C, by thoroughly mixing the starting materials for synthesis and calcining the precursor in a nitrogen stream. That is, it is possible to synthesize LiFePO 4 over a wider temperature range than in the prior art, and the selection range of the temperature at which the precursor is fired (hereinafter referred to as the firing temperature) is widened. The inventors of the present invention focused on the relationship between the firing temperature for firing the precursor and the capacity of the battery using LiFePO 4 as an active material and studied the optimum firing temperature of LiFePO 4 .
    As a result, the firing temperature of LiFePO 4 is specifically in the range of 400 ° C or more and 700 ° C or less. The firing temperature of LiFePO 4 is preferably in the range of 400 ° C or more and 600 ° C or less.
    If the calcination temperature of LiFePO 4 is lower than 400 캜, a phase containing impurities such as a ternary iron compound, that is, an Fe 3 + -containing phase, can not be obtained and uniform LiFePO 4 can not be obtained. If the calcination temperature of LiFePO 4 is higher than 700 ° C, there is a fear that the crystallization proceeds excessively and the precipitation of impurities is not suppressed.
    In addition, in the above-mentioned method for producing a cathode active material, it is preferable that deaeration treatment is performed on the precursor before the precursor is baked to remove air contained in the precursor.
    If air remains in the precursor, Fe 2+ in iron acetate, which is a divalent iron compound, is oxidized by oxygen in the air to form Fe 3+ upon firing LiFePO 4 . As a result, the trivalent iron compound, which is an impurity, is incorporated into the product LiFePO 4 . By removing the air contained in the precursor by the degassing treatment, oxidation of Fe 2+ in the iron acetate can be prevented. As a result, the trivalent iron compound is not incorporated into the product LiFePO 4 , so that a single phase LiFePO 4 can be obtained.
    In addition to the above-mentioned compounds, various raw materials such as lithium hydroxide, lithium nitrate, lithium acetate, lithium phosphate, ferrous phosphate, and ferrous oxide can be used as the starting materials for the synthesis of LiFePO 4 . For firing at low temperature, it is preferable to use a raw material having high reactivity.
    The nonaqueous electrolyte secondary battery 1 manufactured as described above contains Li x M y PO 4 as a positive electrode active material.
    Since this positive electrode active material contains Li x M y PO 4 having a particle diameter of 10 μm or less, lithium having a charge carrier is sufficiently diffused, so that it has a suitable particle size distribution. Therefore, the nonaqueous electrolyte secondary battery 1 has good cycle characteristics and high capacity because the lithium is well doped / undoped.
    In addition, since this positive electrode active material contains Li x M y PO 4 having a 10% volume cumulative diameter of 1 m or less, diffusion of lithium as a charge carrier occurs more smoothly, so that it has a suitable particle size distribution. Therefore, the nonaqueous electrolyte secondary battery 1 has a better cycle characteristic and a higher capacity because the lithium is doped / undoped more satisfactorily.
    In the above-mentioned method for producing a positive electrode active material, a compound represented by the chemical formula Li x M y PO 4 , for example, LiFePO 4 is mixed to prepare a precursor, and the precursor is calcined at a temperature of 400 ° C or more and 700 ° C or less , The chemical reaction and the crystallization proceed uniformly and the crystallization does not proceed excessively. As a result, a single phase LiFePO 4 free of impurities is obtained as the positive electrode active material. Therefore, this positive electrode active material can realize a high capacity exceeding 120 mAh / g of the conventional nonaqueous electrolyte secondary battery.
    In addition, by setting the firing temperature of LiFePO 4 to 400 ° C. or more and 600 ° C. or less, a high actual capacity close to 170 mAh / g which is the theoretical capacity of LiFePO 4 can be realized.
    Further, the cathode active material of the present invention is not limited to LiFePO 4 as described above, but is also applied to a compound represented by the formula Li x M y PO 4 .
    The configuration of the nonaqueous electrolyte secondary battery of the present invention is not limited to the above-described configuration, and a case where a solid electrolyte or a swelling solvent-containing gel-like solid electrolyte is used as the nonaqueous electrolyte is also applicable. Further, the non-aqueous electrolyte secondary battery of the present invention is not particularly limited in its shape such as a cylindrical shape, a square shape, a coin shape, and a button shape, and may be various sizes such as a thin shape and a large shape.
    Also, in the method for producing a positive electrode active material, a solid phase reaction method in which a powder of a compound as a starting material for synthesis of LiFePO 4 is mixed and fired has been described. However, the present invention is not limited thereto. A compound represented by the chemical formula Li x M y PO 4 can be synthesized by applying various chemical synthesis methods other than the solid phase reaction.
    Hereinafter, specific examples and comparative examples to which the present invention is applied will be described based on experimental results.
    <Experiment 1>
    In Experiment 1, a compound represented by the chemical formula Li x M y PO 4 was prepared as a cathode active material, and a nonaqueous electrolyte secondary battery using the cathode active material was fabricated as a test battery and various characteristics were evaluated.
    First, in order to evaluate the difference in characteristics of the non-aqueous electrolyte secondary cell due to the difference in particle size distribution of the cathode active material, the cathode active material was synthesized by changing the firing temperature. Then, using this, a test battery was produced.
    Sample 1
    First, LiFePO 4 was synthesized as a cathode active material at a firing temperature of 600 ° C.
    In order to synthesize LiFePO 4 , ammonium hydrogenphosphate (NH 4 H 2 PO 4 ), which is a raw material having a large crystal size, was sufficiently pulverized in advance. Then, iron acetate (Fe (CH 3 COO) 2 ), dihydrogen phosphate, ammonium (NH 4 H 2 PO 4) and lithium carbonate (Li 2 CO 3) molar ratio of 2: the precursor to be mixed thoroughly so that the 1: 2 . Subsequently, the precursor was calcined at 300 캜 for 12 hours under nitrogen atmosphere, and then the precursor was calcined at 600 캜 for 24 hours under a nitrogen atmosphere to synthesize LiFePO 4 .
    Then, LiFePO 4 obtained as described above was used as a positive electrode active material to prepare a battery.
    First, 70 wt% of dry LiFePO 4 as a positive electrode active material, 25 wt% of acetylene black as a conductive agent and 5 wt% of polyvinylidene fluoride as a binder were uniformly mixed in dimethylformamide as a solvent to prepare a paste-like positive electrode mixture . As polyvinylidene fluoride, # 1300 manufactured by Aldrich was used.
    Subsequently, this positive electrode mixture was coated on an aluminum mesh to be a current collector, and dried at 100 DEG C for 1 hour under a dry argon atmosphere to form a positive electrode active material layer.
    Then, an aluminum mesh on which the positive electrode active material layer was formed was punched out onto a circular plate having a diameter of 15 mm to prepare a pellet-shaped positive electrode. Further, 60 mg of the active material is carried on one of the positive electrodes.
    Subsequently, a lithium metal foil was punched out in substantially the same shape as the positive electrode to form a negative electrode.
    Subsequently, LiPF 6 was dissolved in a mixed solvent of propylene carbonate and dimethyl carbonate at a concentration of 1 mol / l to prepare a non-aqueous electrolyte.
    The positive electrode thus obtained was housed in the positive electrode can, the negative electrode was accommodated in the negative electrode can, and the separator was disposed between the positive electrode and the negative electrode. A non-aqueous electrolyte was injected into the positive electrode can and the negative electrode can, and the positive electrode can and the negative electrode can were caulked and fixed to manufacture a 2025-type coin type test battery.
    Sample 2
    A cathode active material was synthesized in the same manner as in the case of Sample 1 except that the firing temperature was set to 400 DEG C, and a test battery was prepared using this cathode active material.
    Sample 3
    A positive electrode active material was synthesized in the same manner as in the case of Sample 1 except that the firing temperature was set to 500 캜, and a test battery was prepared using this positive electrode active material.
    Sample 4
    A cathode active material was synthesized in the same manner as in Sample 1 except that the firing temperature was 700 캜, and a test battery was prepared using this cathode active material.
    Sample 5
    A cathode active material was synthesized in the same manner as in the case of Sample 1 except that the firing temperature was set to 800 DEG C, and a test battery was prepared using this cathode active material.
    Then, a powder X-ray diffraction pattern was measured on LiFePO 4 as a cathode active material synthesized by the above-described method. The measurement conditions of the powder X-ray diffraction are shown below.
    Equipment: Rigak RINT 2500 Rotary Pole Cathode
    X-ray: CuK , 40 kV, 100 mA
    Goniometer: Vertical standard, radius 185 mm
    Counter Monochrometer: Used
    Filter: Not used
    Slit width: divergent slit (DS) = 1 [deg.]
    Receiving slit (RS) = 1 °
    Scattering slit (SS) = 0.15 mm
    Counting device: Scintillation counter
    Measuring method: Reflection method, continuous scanning
    Scanning range: 2 [theta] = 10 [deg.] To 80 [deg.]
    Scan speed: 4 ° / min
    A powder X-ray diffraction pattern of LiFePO 4 synthesized in Samples 1 to 5 is shown in Fig. All also in the presence of impurities other than LiFePO 4 in the product LiFePO 4 synthesized from 2, Samples 1 to 5 do not make it was found that a single phase LiFePO 4 was obtained.
    Then, the test battery produced in Samples 1 to 5 was subjected to a charge-discharge test. First, each test cell was charged with a constant current, and when the battery voltage reached 4.5 V, the constant-current charging was switched to the constant-voltage charging, and the battery was charged while maintaining the voltage at 4.5 V. The charging was terminated when the current became 0.01 mA / cm 2 or less. Thereafter, the discharge was ended when the battery voltage dropped to 2.0 V by discharging. In addition, both charging and discharging were performed at room temperature (23 占 폚), and the current density at this time was 0.12 mA / cm2.
    As a result of the charge-discharge test, the relationship between the sintering temperature of LiFePO 4 synthesized in Samples 1 to 5 and the charge-discharge capacity of the cell is shown in Fig. It can be seen from Fig. 3 that the nonaqueous electrolyte secondary battery has a high capacity by firing LiFePO 4 , which is a positive electrode active material, in a range of 400 ° C or higher and 700 ° C or lower. In addition, it was found that the non-aqueous electrolyte secondary battery has a very high capacity when the firing temperature of the precursor is 400 ° C or more and 600 ° C or less.
    Then, the cathode active material synthesized in Samples 1 to 5 was measured for volume particle size distribution. Microtrack particle size analyzer LA-920 (manufactured by Horiba Seisakusho Co., Ltd.) was used as a measurement apparatus of the volume particle size distribution. The volume particle size distribution was measured by measuring the scattering of the laser light using this measuring apparatus. The measurement results of the volume particle size distribution are shown in Fig.
    As can be seen from Figure 4, when the sintering temperature is greater than 600 ℃, particle size volume distribution of LiFePO 4 is greater than lO ㎛ was increased while the center of the distribution shifted towards larger particles. Also, the volume distribution of LiFePO 4 having a particle diameter of 10 탆 or less was remarkably reduced.
    On the other hand, when the sintering temperature is not more than 600 ℃, particle size volume distribution of less than or equal to 10 ㎛ LiFePO 4 was increased and the distribution center is shifted toward smaller particles.
    4 From the results of the volume particle size distribution results and the charge-discharge capacity of the sintering temperature and the battery shown in Fig. 3 shown in, it is to contribute to the capacity of the battery was found that the LiFePO 4 particles of less than 10 ㎛.
    From this, it was found that the non-aqueous electrolyte secondary battery has a very high capacity by containing LiFePO 4 having a particle diameter of 10 μm or less as a cathode active material.
    5 shows the relationship between the firing temperature and the volume cumulative diameter of LiFePO 4 from the measurement results of the volume particle size distribution. From Figure 5, it is identified that there is a clear correlation between particle size and sintering temperature of LiFePO 4 of LiFePO 4. Thus, in Fig. 5, an enlarged view of the particle diameter in the range of 0.1 to 10 mu m is shown in Fig.
    As can be seen from Fig. 6, when the firing temperature of LiFePO 4 was 600 캜 or less, it was found that LiFePO 4 having a particle diameter of 1 탆 or less accounted for 10% or more. On the other hand, when the firing temperature of LiFePO 4 is higher than 600 ° C, the amount of LiFePO 4 having a particle diameter of 1 탆 or less of LiFePO 4 is less than 10%.
    From the results of the relationship between the calcination temperature of LiFePO 4 and the volume cumulative diameter (particle diameter in the range of 0.1 to 10 탆) shown in Fig. 6 and the relationship between the calcination temperature and the charge / discharge capacity of the battery shown in Fig. 3, It was found that the secondary battery preferably contains LiFePO 4 having a 10% volume cumulative diameter of 1 μm or less as a cathode active material, and thus has a high actual capacity close to the theoretical capacity of LiFePO 4 .
    Further, the cathode active materials of Sample 3, Sample 1 and Sample 4, in which LiFePO 4 was baked at temperatures of 500 캜, 600 캜, and 700 캜, were observed with a scanning microscope. The scanning electron microscope photographs are shown in Figs. 7, 8, and 9, respectively. As can be seen from these Figs. 7, 8 and 9, it is clear that LiFePO 4 grows specifically as the firing temperature rises, and becomes large particles. This corresponds well to the result of the volume particle size distribution shown in Fig. From this, it was found that the crystallization progressed as the firing temperature was increased in LiFePO 4 .
    Further, the BET specific surface area of LiFePO 4 synthesized in Samples 1 to 5 was measured. The measurement results of the BET specific surface area are shown in Fig. Further, the stage was in a measurement with regard to Figure 10, the Samples 1 to 5. In addition, LiFePO 4 in which more accurately change the firing temperature.
    From FIG. 10, it can be seen that the BET specific surface area monotonously changes as the firing temperature of LiFePO 4 increases, and the variation width is very large, from 20 m 2 / g or more to 0.5 m 2 / g or less.
    And, 10 and there is shown showing the relationship between the sintering temperature of LiFePO 4 and the discharge capacity compared to 3, BET specific surface area of the positive electrode active material is LiFePO 4 is 0.5 ㎡ / g or more, more preferably 2 ㎡ / g, when more than It has been found that LiFePO 4 has a high practical capacity close to the theoretical capacity.
    Next, in order to examine the optimum firing temperature of the cathode active material, a cathode active material was synthesized at a lower firing temperature than that of the prior art, and a test battery was prepared as Sample 6 using the cathode active material.
    Sample 6
    LiFePO 4 was synthesized in the same manner as in Sample 1 except that the firing temperature was changed to 320 ° C, and a test battery was fabricated using the obtained LiFePO 4 as a cathode active material.
    First, the powder X-ray diffraction pattern was measured on the cathode active material synthesized in Sample 6 and LiFePO 4 as a cathode active material synthesized in Samples 1 and 5. The measurement results are shown in Fig. In both Fig. 11 from the sample 1, 5, 6 LiFePO 4 synthesized in the presence of other than LiFePO 4 is not an impurity in the product was not identified it was found that a single phase LiFePO 4 was obtained.
    Then, the test batteries produced in Samples 1, 5, and 6 were subjected to a charge-discharge test.
    Charge-discharge characteristics of the sample 1 cell are shown in Fig. From FIG. 12, it was found that the battery of Sample 1 using LiFePO 4 baked at 600 ° C as the precursor had a flat potential near 3.4 V. In addition, this battery produced a reversible charge / discharge capacity of 163 mAh / g. The value of 163 mAh / g was close to the theoretical capacity of 170 mAh / g of LiFePO 4 .
    The relationship between the number of cycles and the charge / discharge capacity of the battery of Sample 1 is shown in Fig. From FIG. 13, it was found that the cycle deterioration of the charge / discharge capacity was relatively low at 0.1% / cycle, and stable battery characteristics were obtained.
    On the other hand, in the battery of Sample 5, as shown in Fig. 14, it was found that the obtained charge / discharge capacity was extremely small. This is considered to be because the crystallization is excessively advanced because the firing temperature of LiFePO 4 is as high as 800 캜 and the diffusion of lithium in the LiFePO 4 particles does not sufficiently take place.
    In the battery of Sample 6, as shown in Fig. 15, it was found that a sufficient charge-discharge capacity was not obtained. It is considered that if the firing temperature is as low as 320 ℃, discard it, etc. present in the trivalent iron compound impurities, that is different from LiFePO 4 containing Fe 3+.
    From the above results, it was found that the LiFePO 4 serving as the cathode active material can realize a high capacity by setting the firing temperature in the range of 400 ° C. to 700 ° C.
    It was also found that a high actual capacity exceeding 120 mAh / g of the conventional non-aqueous electrolyte secondary battery was realized by firing LiFePO 4 in the range of 400 ° C to 600 ° C.
    Further, MnCO 3 was added to the raw material and fired in the same manner to produce Li (Mn 0.6 Fe 0.4 ) PO 4 . The X-ray diffraction diagram of Li (Mn 0.6 Fe 0.4 ) PO 4 obtained in FIG. 16 was shown. From Fig. 16, it can be seen that Li (Mn 0.6 Fe 0.4 ) PO 4 has a single-phase olivine structure containing no impurities.
    FIG. 17 shows charge / discharge characteristics of a battery similarly manufactured using Li (Mn 0.6 Fe 0.4 ) PO 4 obtained by firing at 600 ° C. From Fig. 17, a high capacity of 150 mAh / g was obtained, and a capacity at around 4 V was newly observed, and thus the energy density could be improved.
    The results of measurement of the particle size distribution of Li (Mn 0.6 Fe 0.4 ) PO 4 obtained by firing at 600 ° C are shown in Fig. From Fig. 18, it was found that Li (Mn 0.6 Fe 0.4 ) PO 4 had a particle diameter of 10 탆 or less and a 10% volume cumulative diameter of 1 탆 or less.
    <Experiment 2>
    In Experiment 2, Sample 6 having a sintering temperature of 320 ° C, Sample 2 having a sintering temperature of 400 ° C, and Sample 1 having a sintering temperature of 600 ° C, which contained Fe, in which the Mossbauer effect was observed, among the cathode active materials prepared in Experiment 1 described above Of LiFePO 4 was measured by using Mössbauer spectroscopy.
    In measuring the Mossbauer spectrum, 50 mg of LiFePO 4 as a sample was filled in the hole portion of a lead plate having a hole with a thickness of 0.5 mm and a diameter of 15 mm, and both sides of the hole portion were sealed with a tape. 57 Co of GBq were investigated.
    FIG. 19 shows the results of spectrum measurement of LiFePO 4 of Sample 6 obtained by Mossbauer spectroscopy, FIG. 20 shows the results of spectrum measurement of LiFePO 4 of Sample 2, and FIG. 21 shows the results of spectral measurement of LiFePO 4 of Sample 1.
    The spectrum of Fe 2+ obtained by fitting the Mössbauer spectrum of LiFePO 4 of Sample 6 shown in Fig. 19 is shown in Fig. 22, and the spectrum of Fe 3+ is shown in Fig.
    The spectrum of Fe 2+ obtained by fitting the Mössbauer spectrum of LiFePO 4 of Sample 2 shown in Fig. 20 is shown in Fig. 24, and the spectrum of Fe 3+ is shown in Fig.
    The spectrum of Fe 2+ obtained by fitting the Mössbauer spectrum of LiFePO 4 of Sample 1 shown in FIG. 21 is shown in FIG. 26, and the spectrum of Fe 3+ is shown in FIG.
    The original spectrum of LiFePO 4 was a double line having an isomer shift corresponding to Fe 2+ of about 1.2 mm / sec and a quadrupole splitting of about 2.9 mm / sec, as shown in Figs. 22, 24 and 26.
    On the other hand, LiFePO 4 of Sample 6 having a firing temperature of 320 ° C had a broad double line of about 0.4 mm / sec corresponding to Fe 3+ and a quadrupole splitting of about 0.8 mm / sec, Respectively.
    Here, the area intensity, that is, isomer shift value of the doublet corresponding to Fe 3+ La the area strength of the spectrum in the range between 0.1 ㎜ / sec 0.7 ㎜ / sec A, and the doublet corresponding to Fe 2+ The area strength, that is, the area strength of the spectrum in which the isomer shift value is in the range of 0.8 mm / sec to 1.5 mm / sec is represented by B, and A / B is shown in Table 1.
    Firing temperature A / B 320 ° CSample 60.77 400 ° CSample 20.34 600 ℃Sample 10.15
    In Experiment 1, when X-ray diffraction was performed on Samples 1, 2 and 6, as shown in Fig. 2, the spectrum of Fe 3+ -containing phase, for example, a trivalent iron compound was not detected. However, when the Mössbauer spectroscopic measurement for Samples 1, 2 and 6 was carried out as described above, it was confirmed that an image containing Fe 3+ was present. This is because the X-ray diffraction is caused by the long-distance interference of crystals for the first time, whereas the Mössbauer spectroscopy is by directly detecting the information near the nucleus.
    It can be seen from Table 1 that there are relatively many phases containing Fe 3+ not having a long-range order in Sample 6 having a low firing temperature of 320 ° C.
    From Table 1, it can be seen that A / B depends on the calcination temperature of LiFePO 4 , and that the lower the calcination temperature is, the more Fe 3+ contained in LiFePO 4 is.
    3, which shows the relationship between the sintering temperature and the discharge capacity of A / B and LiFePO 4 shown in Table 1, the smaller the A / B ratio, the more the ferric compound such as Fe 3+ in the LiFePO 4 And the like, the lithium ion secondary battery exhibits a high capacity. Further, it was found that when LiFePO 4 was synthesized at a calcination temperature of 400 ° C or higher, A / B was less than 0.3, realizing a high capacity.
    Therefore, it was found that a high capacity is realized by using LiFePO 4 having A / B of 0.3 as a cathode active material in a lithium ion secondary battery.
    As can be seen from the above description, the cathode active material of the present invention has the formula Li x M y PO 4 (where x is in the range of O <x 2, y is in the range of 0.8 Y 1.2, M is the 3d transition metal ), Li x M y PO 4 has a particle diameter of 10 탆 or less and a BET specific surface area of 0.5 m 2 / g or more. Accordingly, when this positive electrode active material is used in a nonaqueous electrolyte secondary battery, excellent cycle characteristics and high capacity can be realized.
    In addition, the cathode active material of the present invention has a chemical formula Li x (Fe y M 1-y ) PO 4 wherein x is in the range of 0.9 X 1.1, y is in the range of 0 <y And Li x (Fe y M 1-y ) PO 4 has a ratio A / B of less than 0.3 to the area intensity A of the spectrum obtained by the Mössbauer spectroscopy. Accordingly, when the positive electrode active material is used in a nonaqueous electrolyte secondary battery, a high capacity can be realized.
    Further, in the non-aqueous electrolyte secondary battery of the present invention, by using LiFePO 4 obtained by specifying the firing temperature and the particle shape, it has a large capacity and excellent cycle characteristics.
    Also, in the non-aqueous electrolyte secondary battery of the present invention, LiFePO 4 having A / B less than 0.3 is used as a positive electrode active material, so that it has a large capacity.
    Further, in the method for producing a positive electrode active material of the present invention, a single phase Li x M y PO 4 free of impurities is obtained, and thus it is possible to realize a high capacity exceeding 120 mAh / g in the conventional non-aqueous electrolyte secondary battery.
    权利要求:
    Claims (15)
    [1" claim-type="Currently amended] A compound represented by the formula Li x M y PO 4 wherein x is in the range of O <x 2, y is in the range of 0.8 Y 1.2, and M contains the 3d transition metal,
    Wherein said Li x M y PO 4 has a particle diameter of 10 m or less.
    [2" claim-type="Currently amended] The positive electrode active material according to claim 1, wherein the 10% volume cumulative diameter of Li x M y PO 4 is 1 μm or less.
    [3" claim-type="Currently amended] The positive electrode active material according to claim 1, wherein the Li x M y PO 4 has a Bronewight-Mmetw-Teller specific surface area of at least 0.5 m 2 / g.
    [4" claim-type="Currently amended] The positive electrode active material according to claim 1, wherein the Li x M y PO 4 is LiFePO 4 .
    [5" claim-type="Currently amended] A compound represented by the general formula Li x (Fe y M 1 -y ) PO 4 wherein x is in the range of 0.9 X 1.1, y is in the range of 0 <y 1, and M contains a 3d transition metal &Lt; / RTI &
    The above-mentioned Li x (Fe y M 1-y ) PO 4 is defined as the area intensity of the spectrum in which the isomer shift value is in the range of 0.1 mm / sec to 0.7 mm / sec in the spectrum obtained by the Mössbauer spectroscopy, Wherein A / B is less than 0.3, where B is the area strength of the spectrum in which the isomer shift value is in the range of 0.8 mm / sec to 1.5 mm / sec.
    [6" claim-type="Currently amended] The positive electrode active material according to claim 5, wherein Li x (Fe y M 1-y ) PO 4 is LiFePO 4 .
    [7" claim-type="Currently amended] (Li x M y PO 4 wherein x is in the range of O <x 2, y is in the range of 0.8 Y 1.2, and M contains the 3d transition metal) capable of reversibly doping / dedoping lithium ), A negative electrode having a negative electrode active material capable of reversibly doping / undoping lithium, and a non-aqueous electrolyte, wherein the positive electrode active material comprises a compound represented by the following formula
    Wherein the Li x M y PO 4 has a particle diameter of 10 탆 or less.
    [8" claim-type="Currently amended] The nonaqueous electrolyte secondary battery according to claim 7, wherein the 10% volume cumulative diameter of Li x M y PO 4 is 1 탆 or less.
    [9" claim-type="Currently amended] The non-aqueous electrolyte secondary battery according to claim 7, wherein the Li x M y PO 4 has a Bronewight-Emmet-Teller specific surface area of 0.5 m 2 / g or more.
    [10" claim-type="Currently amended] The nonaqueous electrolyte secondary battery according to claim 7, wherein the Li x M y PO 4 is LiFePO 4 .
    [11" claim-type="Currently amended] (Li x (Fe y M 1-y ) PO 4 wherein x is in the range of 0.9 X 1.1, y is in the range of 0 &lt; y 1, and M can be reversibly doped / A transition metal, and a transition metal), a negative electrode having a negative electrode active material capable of reversibly doping / undoping lithium, and a nonaqueous electrolyte,
    The above-mentioned Li x (Fe y M 1-y ) PO 4 is defined as the area intensity of the spectrum in which the isomer shift value is in the range of 0.1 mm / sec to 0.7 mm / sec in the spectrum obtained by the Mössbauer spectroscopy, Wherein A / B is less than 0.3, where B is the area strength of the spectrum in which the isomer shift value is in the range of 0.8 mm / sec to 1.5 mm / sec.
    [12" claim-type="Currently amended] The nonaqueous electrolyte secondary battery according to claim 11, wherein Li x (Fe y M 1-y ) PO 4 is LiFePO 4 .
    [13" claim-type="Currently amended] A compound represented by the formula Li x M y PO 4 wherein x is in the range of O <x 2, y is in the range of 0.8 Y 1.2 and M is the 3d transition metal, A mixing process for producing
    And a firing step of firing the precursor obtained in the mixing step to perform the reaction,
    Wherein the precursor is fired at a temperature in the range of 400 ° C to 700 ° C in the firing step.
    [14" claim-type="Currently amended] 14. The method for producing a cathode active material according to claim 13, wherein the precursor is calcined at a temperature in the range of 400 DEG C to 600 DEG C in the calcination step.
    [15" claim-type="Currently amended] 14. The method for producing a cathode active material according to claim 13, wherein the Li x M y PO 4 is LiFePO 4 .
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    同族专利:
    公开号 | 公开日
    CN1174509C|2004-11-03|
    JP4985640B2|2012-07-25|
    KR100672879B1|2007-01-23|
    US20040002003A1|2004-01-01|
    JP4749551B2|2011-08-17|
    CN1549366A|2004-11-24|
    CA2334003A1|2000-10-12|
    US7217474B2|2007-05-15|
    CN1323447C|2007-06-27|
    WO2000060680A1|2000-10-12|
    US6632566B1|2003-10-14|
    US20060188782A1|2006-08-24|
    CN1302460A|2001-07-04|
    JP2009120479A|2009-06-04|
    TW447162B|2001-07-21|
    EP1094533A1|2001-04-25|
    US7147969B2|2006-12-12|
    JP2011054574A|2011-03-17|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    法律状态:
    1999-04-06|Priority to JP9940899
    1999-04-06|Priority to JP99-99408
    1999-09-28|Priority to JP99-274380
    1999-09-28|Priority to JP27438099
    2000-01-19|Priority to JP2000014131
    2000-01-19|Priority to JP00-14131
    2000-03-28|Application filed by 이데이 노부유끼, 소니 가부시끼 가이샤
    2001-03-26|Publication of KR20010025117A
    2007-01-23|Application granted
    2007-01-23|Publication of KR100672879B1
    优先权:
    申请号 | 申请日 | 专利标题
    JP9940899|1999-04-06|
    JP99-99408|1999-04-06|
    JP99-274380|1999-09-28|
    JP27438099|1999-09-28|
    JP2000014131|2000-01-19|
    JP00-14131|2000-01-19|
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