Anode active material for lithium secondary battery and preparation thereof

09735418 · 2017-08-15

Assignee

Inventors

Cpc classification

International classification

Abstract

The present invention relates to an anode active material for a lithium secondary battery, comprising a carbon material, and a coating layer formed on the surface of particles of the carbon material and having a plurality of Sn-based domains having an average diameter of 1 μm or less. The inventive anode active material having a Sn-based domains coating layer on the surface of a carbon material can surprisingly prevent stress due to volume expansion which generates by an alloy of Sn and lithium. Also, the inventive method for preparing an anode active material can easily control the thickness of the coating layer.

Claims

1. A method for preparing an anode active material for a lithium secondary battery, the method comprising: dispersing a carbon material in an electroplating electrolyte of an electroplating bath, wherein the electroplating bath includes a main electrode and a counter electrode disposed therein; and then applying an electric current to form a coating layer having a plurality of Sn-based domains having an average diameter of 1 μm or less on the surface of particles of the carbon material, wherein the electric current is a pulse current ranging from 0.1 A to 10 A; and stirring the electrolyte at a speed ranging from 800 to 900 rpm while the electric current is applied, wherein the anode active material comprises the particles of the carbon material having the coating layer formed on the surface thereof, wherein the Sn-based domains have a hemisphere shape and/or agglomeration of several hemispheres, wherein the Sn-based domains are of an Sn alloy and wherein the Sn alloy is an alloy of Sn and a metal selected from the group consisting of Mg, Al, Ca, Ti, Cr, Mn, Fe, Co, Ni, Cu, Zn, Ga, Ge, Zr, Nb, Pd, Ag, Cd, In, Sb, Pt, Au, Hg, Pb and Bi, and wherein the coating layer has a density of 2.2 to 5.9 g.Math.cm .sup.−3.

2. The method according to claim 1, wherein the electroplating electrolyte is an acid-based Ni—Sn, Sn—Zn, Sn—Co or Sn—Pb plating solution; a sulfate-based Sn plating solution; hydrochloride-based Sn plating solution; a sulfonate-based Sn, Sn—Pb or Sn—Bi plating solution; a cyanide-based Sn—Cu or Sn—Ag plating solution; or a pyrophosphate-based Sn, Sn—Cu, Sn—Pb or Sn—Zn plating solution.

3. The method according to claim 1, wherein the carbon material is selected from the group consisting of natural graphite, artificial graphite, mesocarbon microbeads (MCMB), carbon fibers, carbon black and a mixture thereof.

4. The method according to claim 1, wherein the carbon material has a specific surface area 10 m.sup.2/g or less.

5. The method according to claim 1, wherein the carbon material has an average particle size of 5 to 100 μm.

Description

DESCRIPTION OF THE DRAWINGS

(1) The accompanying drawings illustrate preferred embodiments of the present invention and, together with the foregoing disclosure, serve to provide further understanding of the technical spirit of the present invention. However, the present invention is not to be construed as being limited to the drawings.

(2) FIG. 1 shows a method for preparing an anode active material in accordance with one embodiment of the present invention.

(3) FIG. 2 is a scanning electron microscope (SEM) photograph of the surface of spherical natural graphite particles having no coating of a Ni—Sn alloy.

(4) FIG. 3 is a SEM photograph of the surface of spherical natural graphite particles coated with a Ni—Sn alloy, which is an anode active material prepared in Example 1.

(5) FIG. 4 is a graph showing results evaluating the life characteristics of batteries prepared in Example 2 and Comparative Example 1.

BEST MODE

(6) Hereinafter, preferred embodiments of the present invention will be described in detail. Prior to the description, it should be understood that the terms used in the specification and the appended claims should not be construed as limited to general and dictionary meanings, but interpreted based on the meanings and concepts corresponding to technical aspects of the present invention on the basis of the principle that the inventor is allowed to define terms appropriately for the best explanation.

(7) FIG. 1 shows a method for preparing an anode active material in accordance with one embodiment of the present invention. However, the configurations illustrated in the embodiments and the drawings are just preferable examples for the purpose of illustrations only, not intended to limit the scope of the disclosure, so it should be understood that other equivalents and modifications could be made thereto without departing from the spirit and scope of the disclosure.

(8) An anode active material for a lithium secondary battery according to the present invention comprises a carbon material, and a coating layer formed on the surface of particles of the carbon material and having a plurality of Sn-based domains having an average diameter of 1 μm or less.

(9) The anode active material functions to absorb lithium ions contained in a cathode active material during charging and then generate electric energy along the concentration gradient of lithium ions during the deintercalation of the absorbed lithium ions. If the anode active material is Sn having high charging/discharging capacity, Sn forms an alloy with lithium ions during the absorption of lithium ions to cause volume expansion.

(10) In order to solve such a volume expansion problem due to Sn, the inventors have introduced a coating layer comprising Sn-based materials on the surface of a carbon material.

(11) The coating layer comprising Sn-based materials according to the present invention is characterized by a plurality of Sn-based domains having an average diameter of 1 μm or less. Here, the domains have boundaries, and each of the domains means the assembly of particles which can be separated by at least one domain boundary. The Sn-based domains of the present invention refer to Sn or a Sn-based alloy. The Sn-based alloy may be an alloy of Sn and a metal selected from the group consisting of Mg, Al, Ca, Ti, Cr, Mn, Fe, Co, Ni, Cu, Zn, Ga, Ge, Zr, Nb, Pd, Ag, Cd, In, Sb, Pt, Au, Hg, Pb and Bi.

(12) The Sn-based domains are formed on the surface of the carbon material to make a coating layer. The Sn-based domains formed on the surface of the carbon material may have a hemisphere shape or a porous structure obtained from the agglomeration of several hemispheres. The coating layer of the Sn-based domains is uniformly formed on the whole surface of the carbon material. Preferably, the Sn-based domains have an average diameter of 1 μm or less so as to minimize mechanical stress due to contraction or expansion which is generated in the formation of an alloy with lithium during charging and discharging. That is, when the domains of Sn or Sn-based alloy components have a smaller size, the anode active material can be recovered to its initial size even though the contraction and expansion is generated during charging and discharging.

(13) The lower limit of an average diameter of Sn-based domains is not particularly limited. However, Sn-based domains having an average diameter less than 0.01 μm may be difficult to form physically and thus may have an average diameter of 0.01 μm or higher.

(14) Also, if the coating layer of Sn or Sn-based alloy having a domain form or a porous structure according to the connection of domains has a thickness of several to tens of μm, the coating layer deposited on the surface of the carbon-based anode active material may be delaminated or broken during alloying (intercalation) with lithium to deteriorate life characteristics.

(15) Accordingly, the coating layer has a density of 2.2 (corresponding to a porosity rate of 80%) to 5.9 g.Math.cm.sup.−3 (corresponding to a porosity rate of 20%), preferably 2.3 to 3.2 g.Math.cm.sup.—3, more preferably 3.3 to 4.5 g.Math.cm.sup.−3, and such a density is higher than that of a Sn-based coating layer obtained by an electroless (autocatalytic) plating method which reduces metallic ions in the presence of a reducing agent in an aqueous metal salt solution to deposit metals on the surface of a material to be treated without the external provision of electric energy. The Sn-based domains are uniformly formed on the surface of the carbon material. Thus, the uniform Sn-based domains coating having a high density can provide superior battery characteristics to an anode active material according to one embodiment of the present invention.

(16) The carbon material used in the present invention may include any carbon material which is known as an anode active material in the art, without particular limitation, for example, natural graphite, artificial graphite, mesocarbon microbeads (MCMB), carbon fiber and carbon black. Such a carbon material may be used alone or in a mixture of at least two materials, but is not limited thereto.

(17) In addition, it is preferred that the carbon material has a specific surface area of 10 m.sup.2/g or less. If the carbon material has a specific surface area larger than 10 m.sup.2/g, the initial efficiency of the anode may decrease. In the present invention, the lower limit of the specific surface area for the carbon material is not particularly limited. A preferred lower limit of the specific surface area may be 2 m.sup.2/g, which is just for illustration purposes and the present invention is not limited thereto.

(18) Also, the carbon material may have an average particle size of 5 to 100 μm, preferably 5 to 40 μm. If the carbon material has an average particle size less than 5 μm, the initial efficiency of the anode may decrease due to the fine powders of the carbon material. If the carbon material has an average particle size larger than 100 μm, the processibility for coating an anode slurry may decrease and scratches on an electrode may increase.

(19) The anode active material of the present invention may be prepared by a method as follows.

(20) First, a main electrode and a counter electrode are disposed in an electroplating bath and the electroplating bath is filled with an electroplating electrolyte.

(21) More specifically, as shown in FIG. 1, a Sn-based counter electrode for providing Sn ions and a main electrode to which Sn is deposited are disposed in an electroplating bath, and then the electroplating bath is filled with an electroplating electrolyte. The electroplating electrolyte which may be used in the present invention includes, but is not limited to, an acidic-based Ni—Sn, Sn—Zn, Sn—Co or Sn—Pb plating solution; a sulfuric acid-based Sn plating solution; hydrochloric acid-based Sn plating solution; sulfonic acid-based Sn, Sn—Pb or Sn—Bi plating solution; cyanide-based Sn—Cu or Sn—Ag plating solution; or pyrophosphate-based Sn, Sn—Cu, Sn—Pb or Sn—Zn plating solution. The Sn-based counter electrode for providing Sn ions may be a Sn-based electrode or an electrode made of a Sn-based alloy. The main electrode for the deposition of Sn-based domains may be an electrode made of SuS or Ni, but its type is not particularly limited.

(22) Next, a carbon material is dispersed in the electroplating electrolyte and then applied to an electric current to form a coating layer having a plurality of Sn-based domains on the surface of particles of the carbon material.

(23) More specifically, as shown in FIG. 1, the bath is provided with a stirrer to uniformly disperse the carbon material in the electrolyte. The electric current used for electroplating, which flows through the counter electrode and the main electrode, may be 0.1 to 10 A, and may be used as a pulse current by controlling the time difference and current values of an applied electric current. Preferably, electrodeposition may be conducted for 10 minutes to 5 hours. As shown in FIG. 1, Sn.sup.2+ ions accept electrons from the main electrode to be deposited on the surface of the carbon material.

(24) Such dispersive electrodeposition may be conducted by using a semibath-type reactor which can calculate the maximum value of theoretical quantities of electrodeposition for Sn or a metal such as Ni, Cu, Co, Zn and Pb, used in the formation of a Sn-alloy, in a plating solution and can easily recover an active material having Sn and a Sn-based alloy plated on the surface of the carbon material and the plating solution after dispersive electrodeposition. The recovered plating solution may be reused.

(25) The anode active material thus prepared according to the present invention may be used to prepare an anode by a conventional method known in the art. Also, a cathode used in the present invention may be prepared by a conventional method known in the art, similar to the anode. For example, the electrode active material of the present invention is mixed with a binder, a solvent, and optionally a conducting material and a dispersing agent to produce a slurry, which is applied to a current collector, followed by compression molding, to prepare an electrode.

(26) The binder which may be used in the present invention includes various kinds of binder polymers, for example, styrene-butadiene rubber (SBR), vinylidenefluoride-hexafluoropropylene copolymer (PVDF-co-HFP), polyvinylidenefluoride, polyacrylonitrile, polymethylmethacrylate, and the like.

(27) The cathode active material which may be used in the present invention preferably includes a lithium-containing transition metal oxide, for example, any one selected from the group consisting of Li.sub.xCoO.sub.2 (0.5<x<1.3), Li.sub.xNiO.sub.2 (0.5<x<1.3), Li.sub.xMnO.sub.2 (0.5<x<1.3), Li.sub.xMn.sub.2O.sub.4 (0.5<x<1.3), Li.sub.x(Ni.sub.aCo.sub.bMn.sub.c)O.sub.2 (0.5<x<1.3, 0<a<1, 0<b<1, 0<c<1, a+b+c=1), Li.sub.xNi.sub.1-yCo.sub.yO.sub.2 (0.5<x<1.3, 0<y<1), Li.sub.xCo.sub.1-yMn.sub.yO.sub.2 (0.5<x<1.3, 0≦y<1), Li.sub.xNi.sub.1-yMn.sub.yO.sub.2 (0.5<x<1.3, O≦y<1), Li.sub.x(Ni.sub.aCo.sub.bMn.sub.c)O.sub.4 (0.5<x<1.3, 0<a<2, 0<b<2, 0<c<2, a+b+c=2), Li.sub.xMn.sub.2-zNi.sub.zO.sub.4 (0.5<x<1.3, 0<z<2), Li.sub.xMn.sub.2-zCo.sub.zO.sub.4 (0.5<x<1.3, 0<z<2), Li.sub.xCoPO.sub.4 (0.5<x<1.3), Li.sub.xFePO.sub.4 (0.5<x<1.3), and a mixture thereof. The lithium-containing transition metal oxide may be coated with a metal such as Al or a metal oxide. In addition, lithium-containing transition metal sulfide, selenide, or halide may also be used.

(28) After the electrode is made, a conventional lithium secondary battery including the cathode, the anode, a separator interposed between the cathode and the anode, and an electrolyte may be prepared.

(29) In the present invention, a lithium salt used as a solute of the electrolyte is not particularly limited if it is conventionally used in an electrolyte for a lithium secondary battery. For example, an anion of the lithium salt may include any one selected from the group consisting of F.sup.−, Cl.sup.−, Br.sup.−, I.sup.−, NO.sub.3.sup.−, N(CN).sub.2.sup.−, BF.sub.4.sup.−, ClO.sub.4.sup.−, PF.sub.6.sup.−, (CF.sub.3).sub.2PF.sub.4.sup.−, (CF.sub.3).sub.3PF.sub.3.sup.−, (CF.sub.3).sub.4PF.sub.2.sup.−, (CF.sub.3).sub.5PF.sup.−, (CF.sub.3).sub.6P.sup.−, CF.sub.3SO.sub.3.sup.−, CF.sub.3CF.sub.2SO.sub.3.sup.−, (CF.sub.3SO.sub.2).sub.2N.sup.−, (FSO.sub.2).sub.2N.sup.−, CF.sub.3CF.sub.2(CF.sub.3).sub.2CO.sup.−, (CF.sub.3 SO.sub.2).sub.2CH.sup.−, (SF.sub.5).sub.3C.sup.−, (CF.sub.3SO.sub.2).sub.3C.sup.−, CF.sub.3(CF.sub.2).sub.7SO.sub.3.sup.−, CF.sub.3CO.sub.2.sup.−, CH.sub.3CO.sub.2.sup.−, SCN.sup.− and (CF.sub.3CF.sub.2SO.sub.2).sub.2N.sup.−.

(30) In the electrolyte used in the present invention, an organic solvent contained in the electrolyte is not particularly limited if it is conventionally used in an electrolyte for a lithium secondary battery. For example, the organic solvent may include propylene carbonate (PC), ethylene carbonate (EC), diethyl carbonate (DEC), dimethyl carbonate (DMC), ethylmethyl carbonate (EMC), methylpropyl carbonate, dipropyl carbonate, dimethylsulfoxide, acetonitrile, dimethoxyethane, diethoxyethane, vinylene carbonate, sulforane, γ-buryrolactone, propylene sulfite, and tetrahydrofuran and or a mixture thereof. In particular, among the above carbonate-based organic solvents, ethylene carbonate and propylene carbonate that are cyclic carbonates are preferred, since they have high viscosity and consequently a high dielectric constant to easily dissociate the lithium salt in the electrolyte. More preferably, such a cyclic carbonate is used in a mixture with a linear carbonate having a low viscosity and a low dielectric constant, such as dimethyl carbonate and diethyl carbonate in a suitable ratio, to provide an electrolyte having a high electric conductivity.

(31) Optionally, the electrolyte stored according to the present invention may further include an additive such as an overcharge inhibitor which is conventionally used in an electrolyte.

(32) Also, the separator which may be used in the present invention includes, but is not limited to, a single-layered or multi-layered porous polymer film conventionally used as a separator, and a porous non-woven fabric conventionally used as a separator, and the like. The porous polymer film may be made of polyolefin-based polymer, for example, ethylene homopolymer, propylene homopolymer, ethylene/butene copolymer, ethylene/hexene copolymer, and ethylene/methacrylate copolymer, and the porous non-woven fabric may be made of, for example, high-melting glass fibers, polyethylene terephthalate fibers, and the like. However, the present invention is not limited thereto.

(33) A battery casing used in the present invention may be any one conventionally used in the art, and the appearance of the battery casing is not limited to a specific shape based on the purpose of use of the battery. For example, the battery casing may have a cylindrical shape, a prismatic shape, a pouch shape, or a coin shape.

(34) Hereinafter, the present invention will be described in detail through specific examples. However, the description proposed herein is just a preferable example for the purpose of illustrations only, not intended to limit the scope of the invention, so it should be understood that the examples are provided for a more definite explanation to an ordinary person skilled in the art.

EXAMPLES

Example 1

Preparation of Anode Active Material

(35) In order to coat Ni—Sn on a carbon-based active material, an electroplating solution (Ni—Sn electrolyte) was prepared. Specifically, 0.075 M nichel chloride hexahydrate (NiCl.sub.2.6H.sub.2O), 0.175 M tin chloride dehydrate (SnCl.sub.2.2H.sub.2O) and 0.125 M glycine (NH.sub.2CH.sub.2COOH) were added to 0.5 M potassium pyrophosphate (K.sub.2P.sub.2O.sub.7) aqueous solution, to which 26% ammonia solution (NH.sub.4OH) was added to control pH of the solution.

(36) In 177 g of Ni—Sn plating solution thus prepared, 135 g of spherical natural graphite was dispersed to obtain an electroplating electrolyte (pH 8.02) having a solid content of 43.3%.

(37) As shown in FIG. 1, a Sn-plate (counter electrode) and a SuS mesh (main electrode) were disposed in 100 ml beaker containing the electroplating electrolyte prepared above, which was used as an electroplating equipment, followed by dispersive Ni—Sn electroplating for 1 hour in the condition of an electric current of 1.0 A and a stiffing speed of 800 to 900 rpm.

(38) The resultant obtained from electroplating was washed with distilled water at a pH range of 7.0 to 7.51, and dried at 130° C. for 24 hours, to obtain natural graphite particles coated with a Ni—Sn alloy (yield: about 90% or more) as an anode active material.

Example 2

Preparation of Lithium Secondary Battery

(39) The anode active material prepared in Example 1, SBR (styrene-butadiene rubber) as a binder, CMC (carboxy methyl cellulose) as a thickener and acetylene black as a conducting material were mixed at a ratio of 95:2:2:1 (wt %), and added to water (H.sub.2O) as a solvent to obtain a uniform anode slurry. The anode slurry obtained was coated on one surface of a copper current collector at a thickness of 65 μm, dried and compressed, followed by punching to the desired size, to obtain an anode.

(40) Ethylene carbonate (EC) and diethyl carbonate (DEC) as a solvent were mixed at a ratio of 30:70 (vol %), and LiPF.sub.6 was added thereto, to obtain 1M LiPF.sub.6 non-aqueous electrolyte.

(41) Also, lithium metal foil was used as a counter electrode, i.e., cathode, and then a polyolefin separator was interposed between both electrodes and the electrolyte obtained was introduced, to obtain a coin-type lithium secondary battery.

Comparative Example 1

Preparation of Lithium Secondary Battery

(42) The procedure of Example 2 was repeated except that spherical natural graphite particles having no coating of a Ni—Sn alloy were used, to obtain a coin-shaped lithium secondary battery.

Experimental Example 1

Evaluation for the Surface of Anode Active Material

(43) The anode active material prepared in Example 1, i.e., the natural graphite particles coated with a Ni—Sn alloy on the surface thereof, and the spherical natural graphite particles having no coating of a Ni—Sn alloy were analyzed for their surface by means of scanning electron microscope (SEM). The results are shown in FIGS. 2 and 3.

Experimental Example 2

Evaluation for the Cycle Characteristics of Coin-type Battery using Anode Active Material

(44) The batteries prepared in Example 2 and Comparative Example 1 were evaluated for charge/discharge characteristics.

(45) Specifically, battery charging was made with a current density of 0.1C up to 5 mV at constant current (CC)—constant voltage (CV) mode, kept at 5 mV at CC mode, and completed when the current density reached 0.005C, and battery discharging was made with a current density of 0.1C up to 1V at CC mode. The charging/discharging was repeated 50 times under the same conditions.

(46) The results of the measured charge/discharge characteristics are shown in FIG. 4.

(47) As can be seen in FIG. 4, the battery of Example 2 using natural graphite particles coated with a Ni—Sn alloy as an anode active material represents an increased capacity and equivalent cycle characteristics due to the Ni—Sn coating, compared to the battery of Comparative Example 1 using simple natural graphite particles as an anode active material, and also the battery of Example 2 represents substantially equivalent coulombic efficiency in the presence of the Ni—Sn alloy coating, compared to the battery of Comparative Example 1.