WO2006009355A1 - Electrode active material for lithium secondary battery - Google Patents

Electrode active material for lithium secondary battery Download PDF

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Publication number
WO2006009355A1
WO2006009355A1 PCT/KR2005/002123 KR2005002123W WO2006009355A1 WO 2006009355 A1 WO2006009355 A1 WO 2006009355A1 KR 2005002123 W KR2005002123 W KR 2005002123W WO 2006009355 A1 WO2006009355 A1 WO 2006009355A1
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WO
WIPO (PCT)
Prior art keywords
active material
electrode active
limpo
transition metal
secondary battery
Prior art date
Application number
PCT/KR2005/002123
Other languages
French (fr)
Inventor
Sung-Kyun Chang
Jeong-Ju Cho
Original Assignee
Lg Chem, Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Lg Chem, Ltd. filed Critical Lg Chem, Ltd.
Priority to JP2007521392A priority Critical patent/JP4855399B2/en
Priority to CN2005800239878A priority patent/CN1985391B/en
Priority to CA2574042A priority patent/CA2574042C/en
Priority to EP05765876A priority patent/EP1776727B1/en
Publication of WO2006009355A1 publication Critical patent/WO2006009355A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/37Phosphates of heavy metals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/45Phosphates containing plural metal, or metal and ammonium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/5825Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the present invention relates to a novel electrode active material that can be used in a lithium secondary battery and has improved conductivity.
  • LiMPO as advanced cathode active material for a lithium secondary battery.
  • LiMPO has very low conductivity, con-
  • LiMPO 4 ductivity of LiMPO should be improved in order to commonly use it as electrode active material. Therefore, research and development are made intensively to improve the conductivity of LiMPO . [3] Typically, two types of methods are used to improve the conductivity of LiMPO 4.
  • One method that is used generally includes a step of adding carbon during a mixing step preceding heat treatment in preparing LiMPO 4. By doing so, carbon is coated on surfaces of active material particles formed of LiMPO 4 to provide LiMPO 4 having improved conductivity.
  • Another method that is used recently includes substituting Li or M sites of LiMPO 4 with a metal having a different oxidation number. JP
  • an electrode active material comprising a compound represented by the formula of Li x Fe 1-y M y PO 4 , wherein M is Mn, Cr, Co, Cu, Ni, V, Mo,
  • the present invention has been made in order to improve low con ⁇ ductivity of LiMPO . It is an object of the present invention to provide a novel electrode active material comprising LiMPO in which P atoms in the polyanionic PO
  • M is a transition metal
  • A is an element having an oxidation number of +4 or less and ⁇ x ⁇ l.
  • M is at least one transition metal selected from the group consisting of Fe, Co, Mn, Ni, V, Cu and Ti.
  • LiMPO into a multivalent oxidized state results in a significant increase in con-
  • LiMPO (wherein M is a transition metal with a valency of +2), P atoms (with an
  • the present invention is characterized in that the polyanionic PO 4 has a different element (A) that causes the transition metal (M) to have an oxidation number of between +2 and +3 (i.e., +3> M>+2). By doing so, it can be expected that the novel compound according to the present invention has improved conductivity in a similar manner to the prior art.
  • M is at least one transition metal selected from the group consisting of Fe
  • Non-limiting examples of the element with an oxidation number ⁇ +4 and capable of substituting P include Ti 4+ , Al 3+ ,B 3+ , Zr 4+ , Sn 4+ , V 4+ , Pb 4+ ' Ge 4+ , etc.
  • precursor of the transition metal (M) and precursor of the metal (A) for substitution for example, lithium metal oxides, hydroxides, nitrates, oxides, carbonates, acetates, oxalates, sulfates or chlorides of the transition metal or the metal for substitution
  • lithium precursor for example, lithium nitrate, lithium acetate, lithium hydroxide, lithium carbonate, lithium oxide, lithium sulfate or lithium chloride
  • precursor of PO for example, lithium metal oxides, hydroxides, nitrates, oxides, carbonates, acetates, oxalates, sulfates or chlorides of the transition metal or the metal for substitution
  • precursor of PO for example, lithium metal oxides, hydroxides, nitrates, oxides, carbonates, acetates, oxalates, sulfates or chlorides of the transition metal or the metal for substitution
  • precursor of PO for example, lithium metal oxides, hydroxides, nitrates, oxides, carbonates,
  • ammonium dihydrogen phosphate are mixed in a desired equivalent ratio.
  • a mortar grinder mixing technique is used to form a mixture containing precursor of the transition metal (M), lithium precursor, precursor of PO and precursor of the metal (A) for substitution in a desired equivalent ratio.
  • a dry mixing process or wet mixing process may be used. A dry mixing process is performed with no solvent, while a wet mixing process is performed by adding a suitable solvent such as ethanol, methanol, water, acetone, etc., and mixing to a solvent-free state.
  • the mixture is preferably palletized. However, such palletizing may be omitted.
  • the heat treating process is performed under the atmosphere of dry air, nitrogen or oxygen at a heating/cooling rate of 0.5-10 0 C /min.
  • the mixture is maintained in each heat treating temperature for a predetermined time as described above.
  • An electrode for a battery is manufactured by using the compound of formula 1 obtained as described above as electrode active material.
  • a conductive agent for imparting electroconductivity and a binder for making adhesion between an electrode active material and a collector are necessary in addition to the electrode active material.
  • 1-30 wt% of a conductive agent and 1-20 wt% of a binder are mixed with an electrode active material based on the weight of the electrode active material to form a mixture, and then a dispersing agent is added thereto with stirring to provide paste. Finally, the paste is applied to a collector made of metal, followed by compressing and drying, to provide a laminate- shaped electrode.
  • carbon black is used as the conductive agent.
  • conductive agents include acetylene black (available from Chevron Chemical Company or Gulf Oil Company), Ketjen Black EC series (available from Armak Company), Vulcan XC-72(available from Cabot Company) and Super P (3M Co.).
  • Typical examples of the binder include polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVdF) or copolymers thereof, cellulose, etc.
  • Typical examples of the dispersing agent include isopropyl alcohol, N-methylpyrrolidone (NMP), acetone, etc.
  • the metal forming the collector is a metal with high conductivity. There is no particular limitation in selection of the metal, as long as the metal has no reactivity in the range of drive voltage of the battery and permits the electrode active material paste to be adhered with ease.
  • Typical examples of the metal collector include mesh or foil made of aluminum or stainless steel.
  • the method of applying the electrode active material paste onto the metal collector can be selected among known methods depending on characteristics of particular materials. Otherwise, the method can be suitably designed. For example, the paste is distributed onto the collector and then dispersed thereon uniformly by using a doctor blade, etc. If necessary, the distribution step and dispersion step may be carried out in one step. In addition to the above method, other methods such as die casting, comma coating or screen printing may be used. Otherwise, the paste may be formed on a separate substrate and then is bonded with a collector by a pressing or lamination process.
  • the paste applied on the collector as described above may be dried, for example, in a vacuum oven at a temperature of between 50 and 200 0 C for 1 to 3 days.
  • a method for manufacturing a lithium secondary battery by using the electrode obtained as described above may be exemplified as follows.
  • the electrode is used as cathode.
  • anode active materials used are carbonaceous materials such as hard carbon or graphitized carbon; metal composite oxides such as Li Fe O (0 ⁇ x ⁇ 1), Li
  • WO 2 (0 ⁇ x ⁇ 1) or Sn x Me 1-x Me' y O z
  • Me Mn, Fe, Pb, Ge; Me': Al, B, P, Si, Group 1, 2 or 3 element in the Periodic Table, halogen; 0 ⁇ x ⁇ l; l ⁇ y ⁇ 3; l ⁇ z ⁇ 8); lithium metal; lithium alloys; silicon-containing alloys; tin-containing alloys; metal oxides such as SnO, SnO , PbO, PbO , PbO , Pb O , Pb O , Sb O , Sb O , Sb O , GeO, GeO , Bi O ,
  • Bi O or Bi O conductive polymers such as polyacetylene; Li-Co-Ni based materials,
  • a separator is interposed between the cathode and anode.
  • the separator serves to interrupt internal short circuit between both electrodes and to receive an electrolyte infiltrated therein.
  • Typical examples of the separator that may be used include polymers, glass fiber mats, kraft paper, etc.
  • Commercially available separators include the Celgard series available from Hoechest Celanese Corp. (for example, Celgard 2400 and 2300) and polypropylene membranes available from Ube Industries Ltd. or Pall RAI Co.
  • the electrolyte is a system comprising a lithium salt dissolved in an organic solvent.
  • Particular examples of the lithium salt that may be used include LiClO , LiCF SO , LiAsF , LiBF , LiN(CF SO ) , LiPF , LiSCN and LiC(CF SO ) .
  • Particular examples of the lithium salt that may be used include LiClO , LiCF SO , LiAsF , LiBF , LiN(CF SO
  • organic solvent examples include ethylene Carbonate (EC), propylene carbonate (PC), diethylcarbonate (DEC), dimethylcarbonate (DMC), 1,2-dimethoxyethane, 1,2-diethoxyethane, gamma-butyrolactone, tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxolane, 4-methyl-l,3-dioxolane, diethylether and sulfolane.
  • EC ethylene Carbonate
  • PC propylene carbonate
  • DEC diethylcarbonate
  • DMC dimethylcarbonate
  • 1,2-dimethoxyethane 1,2-diethoxyethane
  • gamma-butyrolactone 1,2-dimethoxyethane
  • 1,2-diethoxyethane 1,2-diethoxyethane
  • gamma-butyrolactone 1,2-dimethoxyethane
  • 1,2-diethoxyethane 1,2-diethoxyethane
  • FIG. 1 is a graph showing charge/discharge characteristics of the battery according to Comparative Example 1.
  • FIG. 2 is a graph showing charge/discharge characteristics of the battery according to Example 1.
  • FIG. 3 is a graph showing charge/discharge characteristics of the battery according to Comparative Example 2.
  • FIG. 4 is a graph showing charge/discharge characteristics of the battery according to Example 2.
  • Co-acetate, Li-carbonate and ammonium dihydrogen phosphate were introduced into a mortar mixer in a desired equivalent ratio and then mixed to obtain a mixture.
  • the resultant powder was introduced into an electric furnace under nitrogen atmosphere and reacted at 300 0 C for 12 hours to remove impurities.
  • the powder free from impurities was mixed again in a mortar mixer. Then, the mixed powder was introduced into an electric furnace under nitrogen atmosphere and reacted at 700 0 C for 24 hours to obtain a final product (LiCoPO ).
  • LiCoPO was used as cathode active material.
  • Slurry was formed by mixing the cathode active material, a conductive agent and binder in the ratio of 90:5:5 and the resultant slurry was applied onto Al foil to provide an electrode.
  • As counter electrode lithium metal was used.
  • An electrolyte containing EC:EMC (1:2) in which IM LiPF was dissolved was used along with the cathode and anode to provide
  • Comparative Example 1 was repeated to obtain a final product (LiCoP Ti O ), except that Co-acetate, Li-carbonate, ammonium dihydrogen phosphate and Li TiO were used in a desired equivalent ratio. Additionally, a coin type battery was man ⁇ ufactured in the same manner as Comparative Example 1, except that the final product, LiCoP 0 98 Ti 0 02 O 4 was used as cathode active material.
  • Comparative Example 1 was repeated to obtain a final product (LiFePO 4 ), except that Fe-acetate was used instead of Co-acetate. Additionally, a coin type battery was manufactured in the same manner as Comparative Example 1, except that the final product, LiFePO was used as cathode active material. [46] Examp r le 2: Synthesis of LiFeP 0.98 Ti 0.02 O 4 and Manufacture of Battery J
  • Example 1 was repeated to obtain a final product (LiFeP Ti O ), except that Fe-
  • the battery according to Example 1 showed a significant drop in the gap between charge profile and discharge profile, as compared to the battery according to Comparative Example 1. This indicates that the cathode active material according to the present invention shows an increased conductivity and decreased resistance. Further, the battery according to Example 1 showed an increase in charge/discharge capacity. When conductivity of an electrode active material increases, the gap between charge profile and discharge profile of the battery using the same material decreases. This results from a drop in overvoltage appearing in charge/discharge cycles, wherein the overvoltage increases in proportion to the resistance of an electrode active material.
  • Example 2 was subjected to a charge/discharge cycle in a voltage range of 3-4V under constant current (CC) conditions of 0.1C. The results are shown in FIGs. 3 and 4.
  • Example 2 the battery according to Example 2 showed a significant drop in the gap between charge profile and discharge profile, as compared to the battery according to Comparative Example 2. This indicates that the cathode active material according to the present invention shows an increased conductivity and decreased resistance. Further, the battery according to Example 2 showed an increase in charge/discharge capacity. [53] Therefore, it can be seen from FIGs. 2 and 4 that each of the batteries using the cathode active materials according to Examples 1 and 2 operates as a battery and provides excellent battery quality compared to the batteries using the cathode active materials according to Comparative Examples 1 and 2.
  • the electrode active material comprising LiMP
  • a O according to the present invention shows improved conductivity and charge/ discharge capacity compared to LiMPO 4.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
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Abstract

Disclosed is a compound represented by the following formula 1. A lithium secondary battery using the same compound as electrode active material, preferably as cathode active material, is also disclosed. [Formula 1] LiMP1-xAxO4 wherein M is a transition metal, A is an element having an oxidation number of +4 or less and 0<x<l. The electrode active material comprising a compound represented by the formula of LiMPl-xAxO4 shows excellent conductivity and charge/discharge capacity compared to LiMPO4.

Description

Description ELECTRODE ACTIVE MATERIAL FOR LITHIUM
SECONDARY BATTERY
Technical Field
[1] The present invention relates to a novel electrode active material that can be used in a lithium secondary battery and has improved conductivity.
Background Art [2] Due to the structural stability of LiMPO resulting from covalent bonds therein,
4 many attempts are made to develop LiMPO as advanced cathode active material for a lithium secondary battery. However, because LiMPO has very low conductivity, con-
4 ductivity of LiMPO should be improved in order to commonly use it as electrode active material. Therefore, research and development are made intensively to improve the conductivity of LiMPO . [3] Typically, two types of methods are used to improve the conductivity of LiMPO 4.
One method that is used generally includes a step of adding carbon during a mixing step preceding heat treatment in preparing LiMPO 4. By doing so, carbon is coated on surfaces of active material particles formed of LiMPO 4 to provide LiMPO 4 having improved conductivity. Another method that is used recently includes substituting Li or M sites of LiMPO 4 with a metal having a different oxidation number. JP
2002-117903 discloses an electrode active material comprising a compound represented by the formula of Li x Fe 1-y M y PO 4 , wherein M is Mn, Cr, Co, Cu, Ni, V, Mo,
Ti, Zn, Al, Ga, Mg, B or Nb; x is a number of between 0.05 and 1.2; and y is a number of between 0 and 0.8.
Disclosure
[4] Therefore, the present invention has been made in order to improve low con¬ ductivity of LiMPO . It is an object of the present invention to provide a novel electrode active material comprising LiMPO in which P atoms in the polyanionic PO
3 sites are partially substituted with a differen 4t element instead of substituting Li or M 4 sites with a different element. [5] According to an aspect of the present invention, there is provided a compound represented by the following formula 1. There is also provided a lithium secondary battery using the same compound as electrode active material, preferably as cathode active material. [6] [Formula 1]
[7] LiMP A O l-x x 4
[8] wherein M is a transition metal, A is an element having an oxidation number of +4 or less and θ<x<l. [9] Preferably, in the above formula 1, M is at least one transition metal selected from the group consisting of Fe, Co, Mn, Ni, V, Cu and Ti.
[10] Hereinafter, the present invention will be explained in more detail.
[11] It is reported by MIT Yet- Ming Chiang et al. that when a transition metal is converted into its multi-valent oxidized state, its conductivity increases significantly compared to its single- valent state (Nature materials 1, 123-128 (2002)/ nature materials 1, 81-82). [12] The present invention is based on the fact that conversion of a transition metal M in
LiMPO into a multivalent oxidized state results in a significant increase in con-
4 ductivity compared to its single-valent state.
[13] According to the present invention, in order to improve low conductivity of
LiMPO (wherein M is a transition metal with a valency of +2), P atoms (with an
4 3 oxidation number of +5) of the polyanionic PO 4 sites in LiMPO 4 are partially substituted with a different element (A) with a oxidation number of +4 or less, thereby providing a novel compound in which the transition metal M has a total oxidation number of between +2 and +3.
[14] In order to convert the transition metal (M) of LiMPO into a multivalent state, P should be substituted with a different element with an oxidation number other than +5. When P is substituted with an element (A) with an oxidation number of +4, the total average oxidation number of M is more than +2. In other words, the present invention is characterized in that the polyanionic PO 4 has a different element (A) that causes the transition metal (M) to have an oxidation number of between +2 and +3 (i.e., +3> M>+2). By doing so, it can be expected that the novel compound according to the present invention has improved conductivity in a similar manner to the prior art.
[15] Such conversion of the transition metal M of LiMPO into a multivalent state may be exemplified as follows.
[16] LiMPO 4 (M= 2+) => LiM2+ (1-x) M3+ x P (1-x) Ti x O 4 (M= 2+ or 3+)
[17] wherein M is at least one transition metal selected from the group consisting of Fe,
Co, Mn, Ni, V, Cu, Ti, etc., and O<X<1.
[18] Additionally, according to the prior art, substitution of Li and transition metal sites with other elements having a different oxidation number is followed by a drop in amount of Li and a structural change including generation of oxygen defects so as to balance the total oxidation valence. However, substitution in the polyanion according to the present invention results in improvement of conductivity without any structural changes.
[19] Non-limiting examples of the element with an oxidation number < +4 and capable of substituting P include Ti4+, Al3+ ,B3+, Zr4+, Sn4+, V4+ , Pb4+' Ge4+ , etc. [20] In order to synthesize the compound represented by the above formula 1, precursor of the transition metal (M) and precursor of the metal (A) for substitution (for example, lithium metal oxides, hydroxides, nitrates, oxides, carbonates, acetates, oxalates, sulfates or chlorides of the transition metal or the metal for substitution), lithium precursor (for example, lithium nitrate, lithium acetate, lithium hydroxide, lithium carbonate, lithium oxide, lithium sulfate or lithium chloride) and precursor of PO (for
4 example, ammonium dihydrogen phosphate) are mixed in a desired equivalent ratio.
[21] In this mixing step, a mortar grinder mixing technique is used to form a mixture containing precursor of the transition metal (M), lithium precursor, precursor of PO and precursor of the metal (A) for substitution in a desired equivalent ratio. To accomplish this, a dry mixing process or wet mixing process may be used. A dry mixing process is performed with no solvent, while a wet mixing process is performed by adding a suitable solvent such as ethanol, methanol, water, acetone, etc., and mixing to a solvent-free state. Before heat treating the mixture formed as described above, the mixture is preferably palletized. However, such palletizing may be omitted.
[22] The mixture formed as described above is heat treated at a temperature of between
350 and 550 0C for 1-12 hours and then further heat treated at a temperature of between 700 and 950 0C for 4-24 hours to provide crystalline powder of the compound represented by the above formula 1. The heat treating process is performed under the atmosphere of dry air, nitrogen or oxygen at a heating/cooling rate of 0.5-10 0C /min. The mixture is maintained in each heat treating temperature for a predetermined time as described above.
[23] Then, the powder of the compound represented by formula 1 is pulverized by mortar grinding.
[24] An electrode for a battery is manufactured by using the compound of formula 1 obtained as described above as electrode active material. To manufacture an electrode, a conductive agent for imparting electroconductivity and a binder for making adhesion between an electrode active material and a collector are necessary in addition to the electrode active material. 1-30 wt% of a conductive agent and 1-20 wt% of a binder are mixed with an electrode active material based on the weight of the electrode active material to form a mixture, and then a dispersing agent is added thereto with stirring to provide paste. Finally, the paste is applied to a collector made of metal, followed by compressing and drying, to provide a laminate- shaped electrode.
[25] In general, carbon black is used as the conductive agent. Particular examples of commercially available conductive agents include acetylene black (available from Chevron Chemical Company or Gulf Oil Company), Ketjen Black EC series (available from Armak Company), Vulcan XC-72(available from Cabot Company) and Super P (3M Co.). [26] Typical examples of the binder include polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVdF) or copolymers thereof, cellulose, etc. Typical examples of the dispersing agent include isopropyl alcohol, N-methylpyrrolidone (NMP), acetone, etc.
[27] The metal forming the collector is a metal with high conductivity. There is no particular limitation in selection of the metal, as long as the metal has no reactivity in the range of drive voltage of the battery and permits the electrode active material paste to be adhered with ease. Typical examples of the metal collector include mesh or foil made of aluminum or stainless steel.
[28] The method of applying the electrode active material paste onto the metal collector can be selected among known methods depending on characteristics of particular materials. Otherwise, the method can be suitably designed. For example, the paste is distributed onto the collector and then dispersed thereon uniformly by using a doctor blade, etc. If necessary, the distribution step and dispersion step may be carried out in one step. In addition to the above method, other methods such as die casting, comma coating or screen printing may be used. Otherwise, the paste may be formed on a separate substrate and then is bonded with a collector by a pressing or lamination process.
[29] The paste applied on the collector as described above may be dried, for example, in a vacuum oven at a temperature of between 50 and 200 0C for 1 to 3 days.
[30] A method for manufacturing a lithium secondary battery by using the electrode obtained as described above may be exemplified as follows. The electrode is used as cathode. As anode active materials, used are carbonaceous materials such as hard carbon or graphitized carbon; metal composite oxides such as Li Fe O (0 < x < 1), Li
2 3
WO 2 (0 < x < 1) or Sn x Me 1-x Me' y O z (Me: Mn, Fe, Pb, Ge; Me': Al, B, P, Si, Group 1, 2 or 3 element in the Periodic Table, halogen; 0<x < l; l ≤ y < 3; l ≤ z < 8); lithium metal; lithium alloys; silicon-containing alloys; tin-containing alloys; metal oxides such as SnO, SnO , PbO, PbO , Pb O , Pb O , Sb O , Sb O , Sb O , GeO, GeO , Bi O ,
2 2 2 3 3 4 2 3 2 4 2 5 2 2 3
Bi O or Bi O ; conductive polymers such as polyacetylene; Li-Co-Ni based materials,
2 4 2 5 or the like. A separator is interposed between the cathode and anode. The separator serves to interrupt internal short circuit between both electrodes and to receive an electrolyte infiltrated therein. Typical examples of the separator that may be used include polymers, glass fiber mats, kraft paper, etc. Commercially available separators include the Celgard series available from Hoechest Celanese Corp. (for example, Celgard 2400 and 2300) and polypropylene membranes available from Ube Industries Ltd. or Pall RAI Co. [31] The electrolyte is a system comprising a lithium salt dissolved in an organic solvent. Particular examples of the lithium salt that may be used include LiClO , LiCF SO , LiAsF , LiBF , LiN(CF SO ) , LiPF , LiSCN and LiC(CF SO ) . Particular
3 6 4 3 2 2 6 3 2 3 examples of the organic solvent that may be used include ethylene Carbonate (EC), propylene carbonate (PC), diethylcarbonate (DEC), dimethylcarbonate (DMC), 1,2-dimethoxyethane, 1,2-diethoxyethane, gamma-butyrolactone, tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxolane, 4-methyl-l,3-dioxolane, diethylether and sulfolane. Such organic solvents may be used alone or in combination.
Description of Drawings
[32] FIG. 1 is a graph showing charge/discharge characteristics of the battery according to Comparative Example 1.
[33] FIG. 2 is a graph showing charge/discharge characteristics of the battery according to Example 1.
[34] FIG. 3 is a graph showing charge/discharge characteristics of the battery according to Comparative Example 2.
[35] FIG. 4 is a graph showing charge/discharge characteristics of the battery according to Example 2.
Best Mode
[36] Reference will now be made in detail to the preferred embodiments of the present invention. It is to be understood that the following examples are illustrative only and the present invention is not limited thereto.
[37] Comparative Example 1
[38] <Synthesis of LiCoPO 4 >
[39] Co-acetate, Li-carbonate and ammonium dihydrogen phosphate were introduced into a mortar mixer in a desired equivalent ratio and then mixed to obtain a mixture. The resultant powder was introduced into an electric furnace under nitrogen atmosphere and reacted at 300 0C for 12 hours to remove impurities. The powder free from impurities was mixed again in a mortar mixer. Then, the mixed powder was introduced into an electric furnace under nitrogen atmosphere and reacted at 700 0C for 24 hours to obtain a final product (LiCoPO ).
[40] <Manufacture of Battery >
[41] The final product, LiCoPO was used as cathode active material. Slurry was formed by mixing the cathode active material, a conductive agent and binder in the ratio of 90:5:5 and the resultant slurry was applied onto Al foil to provide an electrode. As counter electrode, lithium metal was used. An electrolyte containing EC:EMC (1:2) in which IM LiPF was dissolved was used along with the cathode and anode to provide
6 a coin type battery. [42] Example 1: Synthesis of LiCoP Ti O and Manufacture of Battery
[43] Comparative Example 1 was repeated to obtain a final product (LiCoP Ti O ), except that Co-acetate, Li-carbonate, ammonium dihydrogen phosphate and Li TiO were used in a desired equivalent ratio. Additionally, a coin type battery was man¬ ufactured in the same manner as Comparative Example 1, except that the final product, LiCoP 0 98 Ti 0 02 O 4 was used as cathode active material.
[44] Comparative Example 2: Synthesis of LiFePO 4 and Manufacture of Battery
[45] Comparative Example 1 was repeated to obtain a final product (LiFePO 4 ), except that Fe-acetate was used instead of Co-acetate. Additionally, a coin type battery was manufactured in the same manner as Comparative Example 1, except that the final product, LiFePO was used as cathode active material. [46] Examp rle 2: Synthesis of LiFeP 0.98 Ti 0.02 O 4 and Manufacture of Battery J
[47] Example 1 was repeated to obtain a final product (LiFeP Ti O ), except that Fe-
0 98 0 02 4 acetate was used instead of Co-acetate. Additionally, a coin type battery was man¬ ufactured in the same manner as Comparative Example 1, except that the final product, LiFeP 0 98 Ti 0 02 O 4 was used as cathode active material.
[48] Experimental Example 1: Electrochemical Test
[49] Each of the batteries obtained from Comparative Example 1 and Example 1 was subjected to a charge/discharge cycle in a voltage range of 3-5.2V under constant current (CC) conditions of 0.1C (15 niAh/g). The results are shown in FIGs. 1 and 2.
[50] As can be seen from FIG. 1 (Comparative Example 1) and FIG. 2 (Example 1), the battery according to Example 1 showed a significant drop in the gap between charge profile and discharge profile, as compared to the battery according to Comparative Example 1. This indicates that the cathode active material according to the present invention shows an increased conductivity and decreased resistance. Further, the battery according to Example 1 showed an increase in charge/discharge capacity. When conductivity of an electrode active material increases, the gap between charge profile and discharge profile of the battery using the same material decreases. This results from a drop in overvoltage appearing in charge/discharge cycles, wherein the overvoltage increases in proportion to the resistance of an electrode active material.
[51] Meanwhile, each of the batteries obtained from Comparative Example 2 and
Example 2 was subjected to a charge/discharge cycle in a voltage range of 3-4V under constant current (CC) conditions of 0.1C. The results are shown in FIGs. 3 and 4.
[52] Similarly, as can be seen from FIG. 3 (Comparative Example 2) and FIG. 4
(Example 2), the battery according to Example 2 showed a significant drop in the gap between charge profile and discharge profile, as compared to the battery according to Comparative Example 2. This indicates that the cathode active material according to the present invention shows an increased conductivity and decreased resistance. Further, the battery according to Example 2 showed an increase in charge/discharge capacity. [53] Therefore, it can be seen from FIGs. 2 and 4 that each of the batteries using the cathode active materials according to Examples 1 and 2 operates as a battery and provides excellent battery quality compared to the batteries using the cathode active materials according to Comparative Examples 1 and 2.
Industrial Applicability [54] As can be seen from the foregoing, the electrode active material comprising LiMP
A O according to the present invention shows improved conductivity and charge/ discharge capacity compared to LiMPO 4.
[55] While this invention has been described in connection with what is presently considered to be the most practical and preferred embodiment, it is to be understood that the invention is not limited to the disclosed embodiment and the drawings. On the contrary, it is intended to cover various modifications and variations within the spirit and scope of the appended claims.

Claims

Claims[1] A compound represented by the following formula 1:
[Formula 1] LiMP A O l-x x 4 wherein M is a transition metal, A is an element having an oxidation number of
+4 or less and 0<x<l. [2] The compound according to claim 1, wherein M is at least one transition metal selected from the group consisting of Fe, Co, Mn, Ni, V, Cu and Ti. [3] The compound according to claim 1, wherein A substituting for P is at least one element selected from the group consisting of Ti(4+), Al(3+) ,B(3+), Zr(4+),
Sn(4+), V(4+), Pb(4+) and Ge(4+). [4] An electrode active material comprising the compound as defined in any one of claims 1 to 3. [5] A lithium secondary battery using the electrode active material as defined in claim 4 as cathode active material.
PCT/KR2005/002123 2004-07-16 2005-07-05 Electrode active material for lithium secondary battery WO2006009355A1 (en)

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CA2574042A CA2574042C (en) 2004-07-16 2005-07-05 Electrode active material for lithium secondary battery
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