Manufacturing method of lithium complex oxide comprising cobalt or nickel

Abstract: The invention provides a manufacturing method of a lithium complex oxide, comprising the steps of 1) atomizing and pyrolyzing an aqueous or alcohol solution of compounds containing metallic salts constituting a lithium cobalt complex oxide or a lithium nickel complex oxide, and 2) annealing said lithium cobalt complex oxide or said lithium nickel complex oxide to increase the average particle diameter thereof to between about 1 and 5 micrometers and adjust the specific surface area thereof to between 2 and 10m 2 /g. The lithium complex oxide provided by this method is homogeneous and enables a long cycle life to withstand repeated charging and discharging and a high level of storage stability when used as an cathode active material of a secondary lithium battery.

Description: This invention relates to a manufacturing method of a lithium complex oxide, especially a lithium cobalt complex oxide or a lithium nickel complex oxide both of which are useful as, for example, an cathode active material of a secondary lithium battery. As methods manufacturing a lithium cobalt complex oxide or a lithium nickel complex oxide both of which are used as an cathode active material of a secondary lithium battery, the following methods have been proposed so far. A lithium cobalt complex oxide: (a) A powder method in which, say, powders of lithium carbonate and cobalt oxide are mixed, and their mixture is fired at about 850°C. (b) A spray-pyrolysis method in which lithium nitrate and cobalt nitrate are dissolved in water, and their solution is ultrasonically atomized for pyrolysis. A lithium nickel complex oxide: (c) A solid-phase method (a powder method) in which powders of, say, lithium carbonate and nickel oxide are mixed, and their mixture is fired at about 750°C in an oxygen gas stream. (d) A method in which lithium nitrate or hydroxide and nickel hydroxide each of which has low-melting point are mixed each other, and their mixture is fired at a low temperature in an oxygen gas stream. (e) A spray-pyrolysis method in which lithium nitrate and nickel nitrate are dissolved in water, and their solution is ultrasonically atomized for pyrolysis. However, the above methods involved the following problems. The powders of carbonates and oxides used as the starting materials in the powder method (a) require firing at a relatively high temperature. As a result, the vaporization of lithium occurs heavily, and there is obtained a product having a molar Li/Co ratio deviating from the desired range. It is impossible to mix the powders uniformly on a molecular basis, resulting, for example, in the formation of Co 2 O 3 in addition to LiCoO 2 as desired, and in order to avoid it, it has been necessary to repeat a long time of firing several times. The spray-pyrolysis method (b) makes it possible to mix elements forming a lithium cobalt complex oxide uniformly on an ionic basis, and realize a drastically improved level of uniformity, as compared with the solid-phase method. It has also the advantage that, as it does not necessitate any step for crushing the raw materials, it can avoid the inclusion of impurities that would result from any crushing step. However, in this spray-pyrolysis method, a series of steps including vaporization of the solvent and pyrolysis are conducted within short period of time, and a complex oxide which is thereby synthesized tends, therefore, to be of low crystallinity, since it has a very short heat history as compared with the product of any conventional firing treatment. If it is used as an active material for a secondary battery, the repeated charging and discharging of the battery results in a broken crystal structure of the material and a lower battery capacity. Moreover, the complex oxide has a very large specific surface area in the order of several tens of square meters per gram, and the decomposition of an electrolyte contacting it brings about a serious lowering in the cycle life of the secondary battery and its storage stability. The powders of carbonates and oxides used as the starting materials in the powder method (c) require firing at a relatively high temperature. As a result, like the method (a), the vaporization of lithium occurs heavily, and there is obtained a product having a molar Li/Ni ratio deviating from the desired range. It is impossible to mix the powders uniformly on a molecular basis, resulting, for example, in the formation of Li 2 Ni 8 O 10 in addition to LiNiO 2 as desired, and in order to avoid it, it has been necessary to repeat a long time of firing several times. The method (d) gives a small deviation from the desired Li/Ni ratio, as compared with the solid-phase method, since it employs a lower temperature for synthesis. However, there is obtained a complex oxide of low crystallinity unless a long time of firing is employed. If it is used as an active material for a secondary battery, the repeated charging and discharging of the battery results in a broken crystal structure of the material and a lower battery capacity. In the event that cations having a radius close to Ni ions, such as of Fe, Co, Mn, Mg or Al, have been substituted for Ni in order to make a secondary battery having an improved cycle life to withstand repeated charging and discharging, it has been impossible to avoid the lack of uniformity in the distribution of Ni and substituted cations. The spray-pyrolysis method (e) makes it possible to mix elements forming a complex oxide of lithium and nickel uniformly on an ionic basis, and realize a drastically improved level of uniformity, as compared with the other methods. It has also the advantage that, like the method (b), as it does not necessitate any step for crushing the raw materials, it can avoid the inclusion of impurities that would result from any crushing step. However, this spray-pyrolysis method has same problems occurred in the method (b) described before. US-A-4 567 031 describes a method of manufacturing a lithium complex oxide comprising the steps of concentrating a solution of metallic salts constituting a lithium cobalt oxide or a lithium nickel complex oxide amongst others, co-crystallizing said concentrated mixed solution and calcining the co-crystallized mixed salt at about 400 to 500°C for about 1 to 4 hours in air to form a lithium complex oxide. It is, therefore, an object of this invention to solve the above problems and provide a manufacturing method of a lithium complex oxide comprising cobalt or nickel which is homogeneous, and enables a long cycle life to withstand repeated charging and discharging and a high level of storage stability when used as an cathode active material of a secondary lithium battery. The invention provides a manufacturing method of a lithium complex oxide, comprising the steps of 1) atomizing and pyrolyzing an aqueous or alcohol solution of compounds containing metallic salts constituting a lithium cobalt complex oxide or a lithium nickel complex oxide, and 2) annealing said lithium cobalt complex oxide or said lithium nickel complex oxide to increase the average particle diameter thereof to between about 1 and 5 micrometers and adjust the specific surface area thereof to between 2 and 10m 2 /g. In the above manufacturing method of a lithium complex oxide, the atomizing and pyrolyzing temperature is preferably between about 500 and 900°C. In the above manufacturing method of a lithium complex oxide, the annealing temperature is preferably between about 600 and 850°C. In the above manufacturing method of a lithium complex oxide, said lithium complex oxide may be LiCoO 2 . In the above manufacturing method of a lithium complex oxide, said lithium complex oxide may be LiNiO 2 . In the above manufacturing method of a lithium complex oxide, said compounds containing metallic salts may be inorganic acid salts. In the above manufacturing method of a lithium complex oxide, said compounds containing metallic salts may comprise a combination of at least one selected from the group of lithium nitrate, lithium acetate and lithium formate and at least one selected from the group of cobalt nitrate, cobalt acetate and cobalt formate. If the aqueous and/or alcoholic solution of compounds containing metal elements forming a lithium cobalt/nickel complex oxide is sprayed in a heated atmosphere, as stated above, it undergoes pyrolysis instantaneously and is finely divided by its own chemical decomposition to form a finely divided complex oxide of high surface activity. Then, the complex oxide is annealed to produce a complex oxide of high surface activity having a grown particle diameter of 1-5 micrometers and a specific surface area of 2-10 m 2 /g which is suitable as an cathode active material of a secondary lithium battery. The lithium cobalt complex oxide and the lithium nickel complex oxide according to this invention are not limited to LiCoO 2 and LiNiO 2 , respectively. The lithium cobalt/nickel complex oxide also includes any product obtained by substituting, for example, Cr, Mn, Fe, Ni/Co, Mg or Al for a part of Co/Ni to realize improved properties. Thus, the metal elements forming a lithium cobalt/nickel complex oxide according to this invention are not only Li and Co/Ni, but also include Cr, Mn, Fe, Ni/Co, Mg and Al. Typical water-soluble compounds thereof include acetates, formates, nitrates and chlorides. These compounds, such as acetates, formates, nitrates and chlorides, have an industrial advantage, since they are by far less expensive than organic compounds having metal ions substituted for hydrogen ions in the molecules, such as alkoxides, and make it possible to keep the cost of raw materials at a low level. A mode of carrying out this invention will now be described by way of examples in which LiCoO 2 was produced as a lithium cobalt complex oxide, and LiNiO 2 was produced as a lithium nickel complex oxide. BRIEF DESCRIPTION OF THE DRAWING Figure 1 is a sectional view showing a secondary lithium battery by way of examples. DESCRIPTIONS OF PREFERRED EMBODIMENTS 1. Examples of a lithium cobalt complex oxide Lithium nitrate, lithium acetate, lithium formate, cobalt nitrate, cobalt acetate and cobalt formate were prepared as compounds of metal elements forming LiCoO 2 . The compounds were used in combinations shown as raw materials in Table 1, and were weighed so accurately as to give a molar Li:Co ratio of 1:1, and put in a vessel, and 1000 ml of a mixture of water and alcohol having a ratio of 1:1 (by volume) was added to them, and stirred to dissolve them in a mixed solution. The mixed solution was sprayed into a vertical pyrolysis furnace having a controlled temperature between 400°C and 900°C through a nozzle at a rate of 1200 ml/h, whereby it was thermally decomposed to give a powder of a complex oxide. Then, the complex oxide was put in an alumina sagger, and annealed at an appropriate temperature between 500°C and 900°C for two hours, whereby samples of LiCoO 2 were obtained as shown at Nos. 1 to 16 in Table 1. LiCoO 2 was also made by another synthesizing method as a comparative example, and is shown as Sample No. *17 in Table 1. Lithium carbonate and cobalt oxide were prepared as the starting materials. They were weighed so accurately as to give a molar Li:Co ratio of 1:1, and were crushed and mixed in a ball mill, and their mixture was fired at 850°C for two hours to yield a complex oxide. A photograph was taken through a scanning electron microscope (SEM) of each sample of the complex oxide powder as obtained, and its particle diameter was determined therefrom. The specific surface area of the complex oxide was determined by nitrogen adsorption. The identification of the complex oxide was carried out by X-ray diffraction (XRD) analysis. The results are shown in Table 1. In Table 1, LC means LiCoO 2 , and CO means Co 2 O 3 . Sample No. Starting Material (Lithium) Starting Material (Cobalt) Atomizing Temp. (°C) Annealing Temp. (°C) Average Particle Diameter (micrometer) Specific Surface Area (m 2 /g) XRD Analysis Phase 1 lithium nitrate Cobalt nitrate 400 800 2.3 6.3 CO,LC 2 lithium nitrate Cobalt nitrate 500 800 2.4 2.7 LC 3 lithium nitrate Cobalt nitrate 600 800 2.6 2.9 LC 4 lithium nitrate Cobalt nitrate 800 800 2.5 3.5 LC 5 lithium nitrate Cobalt nitrate 900 800 2.8 2.5 LC 6 lithium nitrate Cobalt nitrate 800 500 1.6 33.2 LC 7 lithium nitrate Cobalt nitrate 800 600 2.3 9.6 LC 8 lithium nitrate Cobalt nitrate 800 850 2.6 2.6 LC 9 lithium nitrate Cobalt nitrate 800 900 7.9 0.6 LC,CO 10 lithium acetate Cobalt acetate 800 800 1.1 4.3 LC 11 lithium formate Cobalt formate 800 800 1.7 4.2 LC 12 lithium nitrate Cobalt formate 500 800 1.8 2.9 LC 13 lithium nitrate Cobalt formate 600 800 2.0 3.1 LC 14 lithium nitrate Cobalt formate 800 800 1.9 3.7 LC 15 lithium nitrate Cobalt formate 900 800 2.2 2.7 LC 16 lithium nitrate Cobalt formate 800 600 1.7 9.8 LC 17 lithium carbonate Cobalt oxide 850 (Solid-phase method) 9.6 0.4 LC A secondary battery was made by using each complex oxide sample as its active cathode material. The complex oxide powder was kneaded with acetylene black as an electric conducting agent and polytetrafluoroethylene as a binder, and a sheet was formed from their mixture, and bonded under pressure to a stainless steel mesh to make the cathode. The cathode 3 and metallic lithium as an anode 4 were put together with a polypropylene separator 5 interposed therebetween and with the stainless steel mesh of the cathode 3 positioned outwardly, and were placed in a stainless steel cathode can 1 with the cathode 3 down, as shown in Figure 1. The separator 5 was impregnated with an electrolyte. The electrolyte was a solution of lithium perchlorate in a mixed solvent composed of propylene carbonate and 1, 1-dimethoxyethane. Then, the opening of the cathode can 1 was closed with a stainless steel anode plate 2 and an insulating packing 6, whereby a secondary lithium battery as shown in Table 2 was made. Each secondary lithium battery as obtained was subjected to 100 cycles of charging and discharging tests by employing a current density of 0.5 mA/cm 2 for charging and discharging it, and ending its charging at a voltage of 4.2 V and its discharging at a voltage of 3.0 V. After the tests, the secondary battery was disassembled, and its cathode was visually inspected for any peeling. The results are shown in Table 2. Sample No. Initial discharge capacity(mAh/g) Discharge capacity (mAh/g) after 100 cycles Peeling of cathode 1 96 72 Yes (a little) 2 131 127 No 3 135 133 No 4 140 134 No 5 135 131 No 6 136 104 Yes 7 133 126 No 8 131 129 No 9 116 110 No 10 125 117 No 11 126 117 No 12 130 126 No 13 134 132 No 14 139 133 No 15 134 130 No 16 132 125 No 17 114 103 No As is obvious from the results shown in Table 1, the spray pyrolysis of a solution containing metal elements forming a lithium cobalt complex oxide and the annealing of its product yield a complex oxide having a grown particle diameter of 1-5 micrometers and a specific surface area of 2-10 m 2 /g. This complex oxide is a single phase of LiCoO 2 . The use of any such complex oxide as an active cathode material makes it possible to obtain a secondary lithium battery having a long cycle life and free from any deterioration, such as electrode peeling, as shown in Table 2. A specific range of preferred spray-pyrolysis temperatures is 500-900°C. A single phase of a lithium cobalt complex oxide can be produced at a temperature of 500°C or above. Its upper limit is defined by the temperature below which the lithium cobalt complex oxide as produced is not decomposed by heat. A specific range of preferred annealing temperatures is 600-850°C. At any temperature below 600°C, it is impossible to cause the lithium cobalt complex oxide as produced by pyrolysis to grow satisfactorily in crystallinity and particle diameter to give an improved cycle life and an improved storage stability to a secondary battery. If the annealing temperature exceeds 850°C, however, a particle diameter of the lithium cobalt complex oxide become too large for an active cathode material for a secondary battery, causing a low capacity. Although the foregoing description of the examples has been of the cases where the compounds of metal elements forming LiCoO 2 are their nitrates, acetates or formates, it is not intended for limiting the scope of this invention to such cases. This invention does not preclude the use of other water- or alcohol-soluble compounds, such as chlorides. When lithium nitrate is used as a lithium compound, or one of the compounds of metal elements forming LiCoO 2 , and cobalt formate as the other, or a cobalt compound, as in the case of Sample No. 14, it is possible to obtain a higher discharge capacity than when lithium acetate and cobalt acetate are used as in the case of Sample No. 10, and when lithium formate and cobalt formate are used as in the case of Sample No. 11, and a high discharge capacity which is comparable to what is obtained when lithium nitrate and cobalt nitrate are used as in the case of Sample No. 4. Further, when lithium nitrate and cobalt formate are used, a reaction as shown by formula (1) takes place, and produces exhaust gases which contain only 1/3 of the amount of NO 2 produced by the reaction of lithium nitrate and cobalt nitrate as shown by formula (2). Therefore, it is easier to dispose of the gases. Thus, the most preferable combination of compounds of metal elements forming LiCoO 2 is of lithium nitrate and cobalt formate. LiNO 3 + Co(HCOO) 2 + O 2 → LiCoO 2 + 2CO 2 + NO 2 + H 2 O LiNO 3 + Co(NO 3 ) 2 → LiCoO 2 + 3NO 2 + 0.5O 2 Similar results can be obtained from cases employing a lithium cobalt complex oxide other than LiCoO 2 , as obtained by substituting, for example, Cr, Mn, Fe, Ni, Mg or Al for a part of the Co sites in LiCoO 2 . 2. Examples of a lithium nickel complex oxide Lithium nitrate, lithium acetate, lithium formate, nickel nitrate, nickel acetate and nickel formate were prepared as compounds of metal elements forming LiNiO 2 . The compounds were used in combinations shown as raw materials in Table 1, and were weighed so accurately as to give a molar Li:Ni ratio of 1:1, and put in a vessel, and 1000 ml of a mixture of water and alcohol having a ratio of 1:1 (by volume) was added to them, and stirred to dissolve them in a mixed solution. The mixed solution was sprayed into a vertical pyrolysis furnace having a controlled temperature between 400°C and 900°C through a nozzle at a rate of 1200 ml/h, whereby it was thermally decomposed to give a powder of a complex oxide. Then, the complex oxide was put in an alumina sagger, and annealed at an appropriate temperature between 500°C and 900°C for two hours, whereby samples of LiNiO 2 were obtained as shown at Nos. 1 to 16 in Table 1. LiNiO 2 was also made by another synthesizing method as a comparative example, and is shown as Sample No. *117 in Table 1. Lithium hydroxide and nickel hydroxide were prepared as the starting materials. They were weighed so accurately as to give a molar Li:Ni ratio of 1:1, and were crushed and mixed in a ball mill, and their mixture was fired at 750°C for two hours in an oxygen gas stream to yield a complex oxide. A photograph was taken through a scanning electron microscope (SEM) of each sample of the complex oxide powder as obtained, and its particle diameter was determined therefrom. The specific surface area of the complex oxide was determined by nitrogen adsorption. The identification of the complex oxide was carried out by X-ray diffraction (XRD) analysis. The results are shown in Table 3. In Table 3, LN means LiNiO 2 , and NO means Li 2 Ni 8 O 10 . Sample No. Starting Materal (Lithium) Starting Material (Nickel) Atomizing Temp. (°C) Annealing Temp. (°C) Average Particle Diameter (micrometer) Specific Surface Area (m 2 /g) XRD Analysis Phase 101 lithium nitrate nickel nitrate 400 800 2.4 5.4 NO, LN 102 lithium nitrate nickel nitrate 500 800 2.4 2.8 LN 103 lithium nitrate nickel nitrate 600 800 2.5 3.1 LN 104 lithium nitrate nickel nitrate 800 800 2.3 3.2 LN 105 lithium nitrate nickel nitrate 900 800 2.8 2.6 LN 106 lithium nitrate nickel nitrate 800 500 1.8 27.3 LN 107 lithium nitrate nickel nitrate 800 600 2.2 9.4 LN 108 lithium nitrate nickel nitrate 800 850 2.5 2.4 LN 109 lithium nitrate nickel nitrate 800 900 7.4 0.7 LN, LO 110 lithium acetate nickel acetate 800 800 1.2 4.2 LN 111 lithium formate nickel formate 800 800 1.8 4.1 LN 112 lithium nitrate nickel formate 500 800 1.9 2.8 LN 113 lithium nitrate nickel formate 600 800 2.0 3.0 LN 114 lithium nitrate nickel formate 800 800 1.9 3.7 LN 115 lithium nitrate nickel formate 900 800 2.3 2.4 LN 116 lithium nitrate nickel formate 800 600 1.8 9.3 LN 117 lithium carbonate nickel oxide 850 (Solid-phase method) 8.9 0.5 LN A secondary battery was made by using each complex oxide sample as its active cathode material. The complex oxide powder was kneaded with acetylene black as an electric conducting agent and polytetrafluoroethylene as a binder, and a sheet was formed from their mixture, and bonded under pressure to a stainless steel mesh to make the cathode. The cathode 3 and metallic lithium as an anode 4 were put together with a polypropylene separator 5 interposed therebetween and with the stainless steel mesh of the cathode 3 positioned outwardly, and were placed in a stainless steel cathode can 1 with the cathode 3 down, as shown in Figure 1. (The same Figure 1 and the same reference numerals described in the example using the lithium cobalt complex oxide are used here again.) The separator 5 was impregnated with an electrolyte. The electrolyte was a solution of lithium perchlorate in a mixed solvent composed of propylene carbonate and 1, 1-dimethoxyethane. Then, the opening of the cathode can 1 was closed with a stainless steel anode plate 2 and an insulating packing 6, whereby a secondary lithium battery as shown in Table 4 was made. Each secondary lithium battery as obtained was subjected to 100 cycles of charging and discharging tests by employing a current density of 0.5 mA/cm 2 for charging and discharging it, and ending its charging at a voltage of 4.2 V and its discharging at a voltage of 3.0 V. After the tests, the secondary battery was disassembled, and its cathode was visually inspected for any peeling. The results are shown in Table 4. Sample No. Initial discharge capacity (mAh/g) Discharge capacity (mAh/g) after 100 cycles Peeling of cathode 101 120 90 Yes (a little) 102 164 159 No 103 169 166 No 104 173 168 No 105 168 164 No 106 168 130 Yes 107 166 157 No 108 169 167 No 109 146 138 No 110 155 145 No 111 156 145 No 112 163 158 No 113 168 165 No 114 172 167 No 115 167 163 No 116 165 156 No 117 142 129 No As is obvious from the results shown in Table 3, the spray pyrolysis of a solution containing metal elements forming a lithium nickel complex oxide and the annealing of its product yield a complex oxide having a grown particle diameter of 1-5 micrometers and a specific surface area of 2-10 m 2 /g. This complex oxide is a single phase of LiNiO 2 . The use of any such complex oxide as an active cathode material makes it possible to obtain a secondary lithium battery having a long cycle life and free from any deterioration, such as electrode peeling, as shown in Table 4. A specific range of preferred spray-pyrolysis temperatures is 500-900°C. A single phase of a lithium nickel complex oxide can be produced at a temperature of 500°C or above. Its upper limit is defined by the temperature below which the lithium nickel complex oxide as produced is not decomposed by heat. A specific range of preferred annealing temperatures is 600-850°C. At any temperature below 600°C, it is impossible to cause the lithium nickel complex oxide as produced by pyrolysis to grow satisfactorily in crystallinity and particle diameter to give an improved cycle life and an improved storage stability to a secondary battery. If the annealing temperature exceeds 850°C, however, a particle diameter of the lithium nickel complex oxide become too large for an active cathode material for a secondary battery, causing a low capacity. Although the foregoing description of the examples has been of the cases where the compounds of metal elements forming LiNiO 2 are their nitrates, acetates or formates, it is not intended for limiting the scope of this invention to such cases. This invention does not preclude the use of other water- or alcohol-soluble compounds, such as chlorides. When lithium nitrate is used as a lithium compound, or one of the compounds of metal elements forming LiNiO 2 , and nickel formate as the other, or a nickel compound, as in the case of Sample No. 114, it is possible to obtain a higher discharge capacity than when lithium acetate and nickel acetate are used as in the case of Sample No. 110, and when lithium formate and nickel formate are used as in the case of Sample No. 111, and a high discharge capacity which is comparable to what is obtained when lithium nitrate and nickel nitrate are used as in the case of Sample No. 104. Further, when lithium nitrate and nickel formate are used, moreover, a reaction as shown by formula (1) takes place, and produces exhaust gases which contain only 1/3 of the amount of NO 2 produced by the reaction of lithium nitrate and nickel nitrate as shown by formula (2). Therefore, it is easier to dispose of the gases. Thus, the most preferable combination of compounds of metal elements forming LiNiO 2 is of lithium nitrate and nickel formate. LiNO 3 + Ni(HCOO) 2 + O 2 → LiNiO 2 + 2CO 2 + NO 2 + H 2 O LiNO 3 + Ni(NO 3 ) 2 → LiNiO 2 + 3NO 2 + 0.5O 2 Similar results can be obtained from cases employing a lithium nickel complex oxide other than LiNiO 2 , as obtained by substituting, for example, Cr, Mn, Fe, Co, Mg or Al for a part of the Ni sites in LiNiO 2 . As is obvious from the foregoing description, the manufacturing method of this invention makes it possible to obtain a lithium cobalt complex oxide and a lithium nickel complex oxide each of which is homogeneous and has a particle diameter of 1-5 micrometers and a specific surface area of 2-10 m 2 /g. The use of this complex oxide as an cathode active material of a secondary battery makes it possible to obtain a secondary lithium battery having a long cycle life to withstand repeated charging and discharging and a high level of storage stability.

Claims: A manufacturing method of a lithium complex oxide, comprising the steps of: 1) atomizing and pyrolyzing an aqueous or alcohol solution of compounds containing metallic salts constituting a lithium cobalt complex oxide or a lithium nickel complex oxide, and 2) annealing said lithium cobalt complex oxide or said lithium nickel complexoxide to increase the average particle diameter thereof to between about 1 and 5 micrometers and adjust the specific surface area thereof to between 2 and 10m 2 /g. A manufacturing method of a lithium complex oxide according to Claim 1, characterized in that the atomizing and pyrolyzing temperature is between about 500 and 900°C. A manufacturing method of a lithium complex oxide according to Claim 2, characterized in that the annealing temperature is between about 600 and 850° C. A manufacturing method of a lithium complex oxide according to one of Claims 1 to 3, characterized in that said lithium complex oxide is LiCoO 2 . A manufacturing method of a lithium complex oxide according to one of Claims 1 to 3, characterized in that said lithium complex oxide is LiNiO 2 . A manufacturing method of a lithium complex oxide according to one of Claims 1 to 5, characterized in that said compounds containing metallic salts are inorganic acid salts. A manufacturing method of a lithium complex oxide according to Claim 4, characterized in that said compounds containing metallic salts comprises a combination of at least one selected from the group of lithium nitrate, lithium acetate and lithium formate and at least one selected from the group of cobalt nitrate, cobalt acetate and cobalt formate. A manufacturing method of a lithium complex oxide according to Claim 5, characterized in that said compounds containing metallic salts comprises a combination of at least one selected from the group of lithium nitrate, lithium acetate and lithium formate and at least one selected from the group of nickel nitrate, nickel acetate and nickel formate.

Inventors: HATTORI KOJI, SAKABE YUKIO, YAMASHITA YASUHISA, HATTORI, KOJI, SAKABE, YUKIO, YAMASHITA, YASUHISA
Applicants: MURATA MANUFACTURING CO, MURATA MANUFACTURING CO., LTD.
Application year: 1997
Main classification: C01G51
IPC codes: C01G53, H01M4, C01G51, C01B13