KR20110111056A - Process for preparing manganese composite oxide - Google Patents

Abstract

The present invention relates to a method for producing a manganese complex oxide based on the coprecipitation method, unlike the conventional coprecipitation method, without using an alkaline aqueous solution as a pH adjusting agent, manganese complex hydroxide is formed from the manganese complex aqueous solution The step is omitted and the manganese composite oxide ((Mn _1-x M _x ) ₃ O ₄ ) is formed immediately.

Description

Process for preparing manganese composite oxide

The present invention relates to a method for manufacturing a manganese composite oxide ([Mn _1-x M _x ] ₃ O ₄ ) that can be used as a cathode active material of a lithium secondary battery when further undergoing a firing procedure with lithium.

Manganese oxide used in the industry has been divided into the use of additives to improve properties in the manufacturing of steel, steel, and nonferrous metals, and as a cathode material for alkaline primary batteries. However, as the demand for hybrid and electric vehicles is expected to increase rapidly, Attention has been drawn to the use of secondary batteries.

Among lithium secondary batteries, a battery using lithium cobalt oxide as a cathode active material is the most used battery because of its excellent electrode life and high fast charge and discharge efficiency. However, such lithium cobalt-based oxides have a disadvantage in that the high temperature safety is low and the cobalt used as a raw material is an expensive material and thus the price competitiveness is limited. In order to use in electric vehicles, low cost, high stability, high power characteristics should be satisfied. Spinel type lithium manganese oxide (LiMn ₂ O ₄ ) manufactured using manganese oxide is an active researcher as an alternative to satisfy the above conditions. In progress.

Since the spinel type lithium manganese oxide has a three-dimensional crystal structure, it is possible to rapidly diffuse lithium ions, and thus has good output characteristics, and it is advantageous to realize low cost of a large capacity battery because low cost manganese is used. However, there is a disadvantage that the capacity is drastically reduced as manganese ions are eluted into the electrolyte at high temperatures and repeatedly charged and discharged. In order to solve this problem, the crystal structure of the positive electrode active material is controlled by the technology of controlling the specific surface area of the positive electrode material in direct contact with the electrolyte and by adding transition metals such as Al and Mg or adding anions such as F in lithium manganese oxide. Techniques to enhance this have been studied.

On the other hand, the conventional method for producing a composite metal oxide, such as the positive electrode active material of a lithium secondary battery is largely classified into three. The first is a high temperature solid phase method of calcination and sintering solid reactants at high temperature, the second is a solid phase reactant in a solvent to obtain a solution, and the solvent is evaporated to obtain a gel. The sol-gel method of heat-treating the gel, and the third is the hydrothermal method of wet heat treatment of the reactants in a high temperature and high pressure reactor. The solid phase method has a lot of problems to be applied to a lithium secondary battery because the whole process is complicated, the purity is not high, and the particle size distribution is not uniform, and the sol-gel method is a solvent or solvent as a raw material in addition to the essential chemical components to dissolve the reactants. As a result, more heat treatment process than necessary to remove them later is added, which not only generates a lot of energy loss, but also consumes materials other than essential chemicals, which is uneconomical. In the case of hydrothermal method, the type of composite metal oxide that can be manufactured is very limited, and since the high temperature and high pressure reactor must be sealed during the manufacturing process, continuous and mass production is impossible. In addition, wastewater from these processes causes water pollution.

In order to solve the problems of the conventional methods such as the solid phase method, the sol-gel method and the hydrothermal method, a number of techniques for producing manganese composite oxide based on the coprecipitation method have been proposed.

For example, Korean Patent Registration No. 815583 is a metal salt aqueous solution containing a first metal, optionally a second metal, including nickel, cobalt and manganese, a chelating agent and

A method for preparing a manganese composite oxide of the form Li _a Ni _x Co _y Mn _z M _1-xyz O _2-δ Q _δ characterized by mixing the basic aqueous solution is provided.

In addition, Korean Patent Registration No. 694567 provides a nickel-cobalt-manganese salt solution, an alkali metal hydroxide aqueous solution, and an ammonium ion supply to the reaction system continuously or intermittently to maintain a constant pH. Synthesis of nickel-cobalt-manganese composite hydroxide aggregated particles in which primary particles obtained by precipitation of hydroxides aggregated to form secondary particles, and synthesis of nickel-cobalt-manganese composite oxy hydroxide aggregated particles by acting an oxidizing agent on the composite hydroxide aggregated particles Lithium-nickel-cobalt represented by the general formula Li _p Ni _x Mn _{1 -x- y} Co _y O _{2 - q} F _q by dry mixing at least the composite oxyhydroxide and lithium salt and baking in an oxygen-containing atmosphere. A method for producing a manganese-containing composite oxide is proposed.

In addition, Korean Patent Registration No. 668050 forms a manganese complex hydroxide (Mn _1-x M _x (OH) ₂ ) to which a transition metal is added by coprecipitation, and oxidizes again to manganese complex oxide ((Mn _1-x M _x). ) ₃ O ₄₎ to be converted and to present a technique for producing a powder of a monodisperse spherical.

However, in the conventional method of manufacturing manganese composite oxide using the coprecipitation method, since the control of the reaction depends on the pH measured at the local region, it cannot be represented whether the input raw materials are uniformly distributed throughout, and the hydroxides and oxides in the reactor. Since it must be formed at the same time, there is a disadvantage that it is very difficult to obtain only the product that has been oxidized continuously. This problem is a part that must be solved in order to achieve mass production of the product. Therefore, a process control is needed more easily and stably to produce manganese composite oxide.

It is an object of the present invention to provide a method for producing a manganese composite oxide, which is easy to secure particle size and composition and has simple process control.

Still another object of the present invention is to provide a method capable of producing a manganese composite oxide, which is a final target material, without passing an intermediate of manganese composite hydroxide from manganese and transition metal raw materials.

In order to achieve the above object, the present invention provides a method for preparing a manganese composite oxide ((Mn _{1 - x} M _x ) ₃ O ₄ , wherein 0.01≤ x ≤ 0.1, M is a transition metal) without using an alkaline aqueous solution as a pH adjuster It provides a method for producing a manganese complex oxide, characterized in that the mixture is prepared by mixing a manganese solution, a transition metal solution, ammonia solution and air.

In particular, the aqueous solution of manganese is preferably an aqueous solution of at least one of manganese salts of manganese sulfide, manganese nitrate, manganese chloride and manganese fluoride.

In particular, the transition metal is preferably at least one selected from Al, Mg, Co, Ni, Cr, Mo, Fe, Zn and W.

In particular, the residence time of the reactants is preferably 4 hours to 12 hours.

In particular, the reaction temperature is preferably 40 to 60 ℃.

In the conventional coprecipitation method, since the control of the reaction depends on the pH measured at the local area, it is not possible to represent whether the input material is uniformly distributed throughout, and the manganese complex hydroxide in the reactor (Mn _{1 - x} M _x (OH) ₂ ) It is very difficult to obtain only manganese complex oxide continuously because it must be converted to manganese complex oxide ((Mn _1-x M _x ) ₃ O ₄ ) by oxidizing again, and the present invention does not use a pH adjuster. Therefore, there is an advantage that can solve the problems of the prior art at a time.

1 is a FE-SEM photograph of the manganese composite oxide prepared in Example 1.
Figure 2 is a FE-SEM photograph of the lithium manganese composite oxide prepared in Example 2.
3 is a FE-SEM measurement photograph of the manganese composite oxide prepared in Example 3.
Figure 4 is a FE-SEM photograph of the lithium manganese composite oxide prepared in Example 4.
5 is a FE-SEM photograph of the manganese composite oxide prepared in Example 5.
Figure 6 is a FE-SEM photograph of the lithium manganese composite oxide prepared in Example 6.
7 is a FE-SEM photograph of the manganese composite oxide prepared in Comparative Example 1.
8 is a FE-SEM photograph of the lithium manganese composite oxide prepared by Comparative Example 2.
9 is an XRD measurement result of the manganese composite oxide prepared in Examples 1, 3, 5 and Comparative Example 1.
10 shows XRD results of lithium manganese composite oxides prepared in Examples 2, 4, 6, and Comparative Example 2. FIG.

The present invention provides a method for preparing a manganese composite oxide ((Mn _{1 - x} M _x ) ₃ O ₄ , 0.01 ≦ x ≦ 0.1, M is a transition metal). In particular, the present invention provides a method for producing a composite manganese oxide using the coprecipitation method, characterized in that it is prepared directly from manganese complex oxide without passing through the intermediate of manganese complex hydroxide from the reactants, unlike the conventional coprecipitation method to provide.

The present invention provides a method for producing a manganese complex oxide, characterized in that prepared by supplying a fixed amount of aqueous solution of manganese, aqueous transition metal, ammonia solution and air.

As said manganese aqueous solution, all normal manganese aqueous solution is possible. For example, an aqueous solution in which manganese salts such as manganese sulfide, manganese nitrate, manganese chloride, and manganese fluoride are dissolved may be all used, and one or more kinds thereof may be mixed and used.

As the transition metal aqueous solution, an aqueous solution in which salts of at least one transition metal selected from Al, Mg, Ni, Co, Cr, Mo, Fe, Zn, and W, for example, aluminum sulfide and aluminum chloride, are dissolved It is possible.

Unlike the conventional coprecipitation method, an aqueous alkali solution, for example, an aqueous sodium hydroxide solution, is not used as the pH adjusting agent. In the present invention, unlike the conventional coprecipitation technique, the manganese complex hydroxide is formed without forming manganese complex hydroxide, and thus, such as sodium hydroxide required for the preparation of manganese complex hydroxide in the intermediate stage of the reaction. No aqueous alkali solution is required. In other words, the pH control was not performed because the alkaline solution used in the existing coprecipitation method was not used. Instead, the reaction rate can be adjusted by checking the accuracy of the raw material supply pump periodically during the reaction. have.

The reaction is put in a constant amount of water and an aqueous ammonia solution in a constant temperature reactor that can maintain a constant temperature, the desired temperature is maintained and stirred at a constant rpm, supplying a manganese solution, a transition metal solution and an aqueous ammonia solution at a constant rate. . At the same time, air is introduced at a constant rate to form an oxidizing atmosphere to form manganese composite oxide ([Mn _{1 - x} M _x ] ₃ O ₄ ). As for the said reaction temperature, about 40-60 degreeC is preferable. The residence time of the reactants in the present invention preferably has 4 to 12 hours. Within the residence time of the reactants, the size of the reaction vessel and the rate of injection of the reactants can be controlled.

The manganese composite oxide prepared by the method of the present invention is characterized in that primary particles of about 0.1 μm to 1 μm are collected to form secondary particles of 5 μm to 15 μm.

In addition, using a manganese composite oxide prepared by the method of the present invention Li _{1 + α} M _x Mn _{2 -α- x} O ₄ which is a cathode active material for a lithium secondary battery (where 0.01 ≦ x ≦ 0.1, 0 ≦ α ≦ 0.1 ) Can be prepared.

For example, the composite manganese oxide powder prepared by the method of the present invention and lithium carbonate were measured at a predetermined ratio, mixed, put in an alumina container, placed in a calcination furnace, and heated up to about 700 ° C. at a constant rate, followed by 8 hours in an air atmosphere. Li _{1 + α} [M _x Mn _{2 -α-x} ] O ₄ may be prepared by the above heat treatment. The method of preparing Li _{1 + α} [M _x Mn _{2 -α-x} ] O ₄ powder from the [Mn _{1 - x} M _x ] ₃ O ₄ powder by firing with Li is very well known. Will be omitted.

Hereinafter, the present invention will be described through examples.

Example 1

Manganese sulfate and aluminum sulfate were weighed in a molar ratio of 0.975: 0.025 to prepare a manganese sulfide complex aqueous solution of 2M concentration, and then maintained at 50 ° C. Into a constant temperature reactor (capacity 5L) capable of maintaining a constant temperature, 4.7L of water and 0.3L of ammonia solution were added and maintained at 50 ° C., followed by stirring at 900 rpm to quantify the manganese sulfide complex solution and ammonia solution at a constant speed. Supplied. At the same time, air was introduced at a rate of 2 L / Min to form an oxidizing atmosphere to form manganese composite oxide.

The aqueous ammonia solution was used 28wt% concentration, and after the initial 0.3L input was continuously quantitatively supplied to the reactor at a rate of 0.04L / min, the manganese sulfide complex aqueous solution was quantitatively supplied at a rate of 0.56L / min. In order to oxidize manganese and aluminum complexes to form manganese composite oxides, only high-purity air was used without any additional materials, and the average residence rate of the total solution added was about 8.3 hours. In the above process, since the alkali solution used in the existing coprecipitation method was not used, no separate pH adjustment was performed. During the reaction, the reaction rate was determined by periodically checking the accuracy of the raw material supply pump. I tried to fit it. After about 8 hours after the start of the reaction, manganese composite oxides were obtained from the outlet located at the top of the reactor and washed with water. The washed manganese composite oxide powder was filtered through water using a vacuum filter and dried in a dryer at 120 ° C. for 12 hours to remove residual water. Final powder prepared Manganese composite oxide _{(Mn 0 .975 Al 0 .025)} 3 FE-SEM picture of the measured O ₄ was like that of FIG.

[Example 2]

The manganese composite oxide of Example 1 and lithium carbonate (Li 2 CO 3) were weighed in a molar ratio of 1: 0.7875, mixed, put in an alumina container, put into a calcination furnace, and heated up to 730 ° C. at a rate of 3 ° C./min. After that, the FE-SEM measurement photograph of the powder Li _1..05 Al _0.05 Mn _1.9 O ₄ obtained by heat treatment at 8 hours under an air atmosphere was as shown in FIG. 2.

Example 3

Manganese sulfate and magnesium sulfate were mixed in a molar ratio of 0.975: 0.025 to prepare manganese composite oxide (Mn _0.975 Mg _0.025 ) ₃ O ₄ in the same manner as in Example 1, except that a composite manganese sulfate solution was prepared. The FE-SEM measurement photograph of the powder prepared in Example 3 was as shown in FIG. 3.

Example 4

The manganese composite oxide of Example 3 was reacted with lithium carbonate as in Example 2 to prepare Li _1.05 Mg _0.05 Mn _1.9 O ₄ , and the FE-SEM measurement photograph was shown in FIG. 4.

Example 5

Manganese sulfate and cobalt sulfate were mixed in a molar ratio of 0.975: 0.025 to prepare a composite manganese tetraoxide (Mn _0.975 Co _0.025 ) ₃ O ₄ in the same manner as in Example 1 except for preparing a composite manganese sulfate solution. The FE-SEM measurement photograph of the powder prepared in Example 3 was as shown in FIG. 5.

Example 6

Example 5 was prepared as the manganese complex oxide as in Example 2 was prepared in the lithium carbonate to yield _{Li 1 .05 Co 0 .05 Mn 1} .9 O 4, FE-SEM picture measurement was as Fig.

Comparative Example 1

Mn ₃ O _{4 in the} same manner as in Example 1, except that a pure manganese sulfate solution was prepared without mixing other metal salts. Particles were prepared, and the FE-SEM photographs were as shown in FIG. 7.

Comparative Example 2

A lithium manganese oxide LiMn ₂ O ₄ was prepared in the same manner as in Example 2 using the manganese composite oxide of Comparative Example 1, and the FE-SEM measurement photo was shown in FIG. 8.

Experimental Example 1

Table 1 shows the results of the component analysis for each of the manganese composite oxide prepared in Example 1, Example 3, Example 5. Total metals (total manganese and transition metals) The content ratios of Al, Mg and Co added by mixing at a molar ratio of 0.025 were close to the theoretical values, indicating that the method for preparing manganese composite oxide was an effective method for impregnating additives.

Additional metal component
Theoretical value Measured value Metal ratio
Of all metals Content ratio
(wt%) Content ratio
(wt%) Example 1 Al 0.025 0.89 0.82 Example 3 Mg 0.025 0.80 0.78 Example 5 Co 0.025 1.93 1.95

Experimental Example 2

Figure 9 shows the results of the XRD pattern analysis for the composite trimanganese tetraoxide prepared in Example 1, Example 3, Example 5 and the comparative trimanganese tetramanganese prepared in Comparative Example 1. The XRD patterns of trimanganese tetraoxide without manganese tetraoxide and manganese composite oxide with Al, Mg, and Co were similar, and impurity phase was not detected.

[Experimental Example 3]

FIG. 10 shows the results of XRD pattern analysis of the lithium manganese composite oxides prepared in Examples 2, 4, and 6 and the lithium manganese composite oxides prepared in Comparative Example 2. FIG. It was confirmed that the spinel-type lithium complex manganese oxide was easily prepared from the trimanganese tetraoxide prepared by the above method by showing the same pattern of lithium manganese oxide and lithium manganese oxide to which Al, Mg, and Co were added.

Claims (5)

Manganese composite oxide ((Mn _{1 - x} M _x ) ₃ O ₄ , 0.01 ≤ x ≤ 0.1, M is a transition metal) without using an alkaline aqueous solution as a pH adjuster, manganese solution, transition metal solution, ammonia solution And a method of producing manganese composite oxides by mixing and reacting air.
The method of claim 1, wherein the manganese aqueous solution is at least one aqueous solution of manganese sulfide, manganese nitrate, manganese chloride, and manganese fluoride solution.
The method of claim 1, wherein the transition metal is one or more selected from Al, Mg, Co, Ni, Cr, Mo, Fe, Zn, and W.
The method of claim 1, wherein the residence time of the reactants is 4 hours to 12 hours.
The method of claim 1, wherein the reaction temperature is 40 to 60 ℃ manufacturing method of manganese composite oxide.

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