METHOD FOR THE PRODUCTION OF MSNX NANOPARTICLES AS ANODE MATERIALS FOR A RECHARGEABLE BATTERY

Abstract

A method for the production of MSn.sub.x nanoparticles, wherein M is an element selected from the group consisting of Co, Mn, Fe, Ni, Cu, In, Al, Ge, Pb, Bi, Ga, and 0<x10, the said method including synthesizing Sn nanoparticles by reducing a tin salt with a solution of a hydride in an anhydrous polar solvent, separating the solid Sn nanoparticles formed from the solution, and washing the Sn nanoparticles, synthesizing M nanoparticles by reducing a metal salt with a solution of a hydride in an anhydrous polar solvent, separating the solid M nanoparticles formed from the solution, and washing the M nanoparticles, mechanical mixing the Sn nanoparticles and the M nanoparticles to convert them into MSn.sub.x nanoparticles.

Claims

1. A method for the production of MSnx nanoparticles, wherein M is an element selected from the group consisting of Co, Mn, Fe, Ni, Cu, In, Al, Ge, Pb, Bi, Ga, and
0<x10 said method comprising the steps of: synthesizing Sn nanoparticles by reducing a tin salt with a solution of a hydride in an anhydrous polar solvent, separating the solid Sn nanoparticles formed from the solution, and washing the Sn nanoparticles, synthesizing M nanoparticles by reducing a metal salt with a solution of a hydride in an anhydrous polar solvent, separating the solid M nanoparticles formed from the solution, and washing the M nanoparticles, mechanical mixing said Sn nanoparticles and said M nanoparticles to convert them into MSnx nanoparticles.

2. The method according to claim 1, wherein the molar ratio of M nanoparticles and Sn nanoparticles for the mechanical mixing step is comprised between 1:1 and 1:3.

3. The method according to claim 1, wherein the mechanical mixing is obtained by ball-milling.

4. The method according to claim 3, wherein the ball-milling is performed in inert gas.

5. The method according to claim 4, wherein the ball-milling is performed under nitrogen.

6. The method according to claim 3, wherein the ball-milling is performed in air.

7. The method according to claim 1, wherein M is Co.

8. The method according to claim 1, wherein the reduction reaction of the tin salt is performed at a temperature comprised between 50 C. and 70 C.

9. The method according to claim 1, wherein the reduction reaction of the metal salt is performed at a temperature comprised between 60 C. and 180 C.

10. The method according to claim 1, wherein the hydride is selected from the group consisting of NaBH4, lithium hydride, sodium hydride, potassium hydride, magnesium hydride, calcium hydride, tributyltinhydride, diisobutyl aluminum hydride, lithium aluminum hydride, lithium triethylborohydride and mixtures thereof.

11. The method according to claim 10, wherein the hydride is NaBH4.

12. The method according to claim 1, wherein the anhydrous polar solvent is selected from the group consisting of 1-methyl-2-pyrrolidone (NMP), hexamethylphosphoramide, 1,3-dimethyl-2-imidazolidinone, 1,3-dimethyl-3,4,5,6-tetrahydro-2(1H)-pyrimidinone, dimethylsulfoxide, sulfolane, glyme, diglyme, triethylene glycol dimethylether, and mixtures thereof.

13. The method according to claim 12, wherein the anhydrous polar solvent is 1-methyl-2-pyrrolidone (NMP).

14. The method according to claim 1, wherein the tin salt is selected from the group consisting of tin chloride, tin fluoride, tin bromide, tin iodide, tin oxide, tin sulfide, sodium stannate trihydrate, tetrabutyltin, and mixtures thereof.

15. The method according to claim 14, wherein the tin salt is tin chloride.

16. The method according to claim 1, wherein the metal salt is selected from the group consisting of M chlorides and mixtures thereof.

17. The method according to claim 16, wherein the metal salt is Co chloride.

18. The method according to claim 1, wherein the reduction reaction is performed in inert gas.

19. The method according to claim 18, wherein the reduction reaction is performed under nitrogen.

20. The method according to claim 1, wherein the reduction reaction is performed in air.

21. The method according to claim 1, wherein the step of synthesizing the Sn nanoparticles comprises the steps of: preparing a solution of hydride in anhydrous solvent and at least one solution of tin salt in anhydrous solvent, heating the solution of hydride to the reaction temperature of the reduction reaction of the tin salt, and starting the reduction reaction when the reaction temperature of the reduction reaction of the tin salt is reached by quick injection of the one or more tin salt solutions into the solution of hydride to generate a reaction mixture.

22. The method according to claim 1, wherein the step of synthesizing the Sn nanoparticles comprises the steps of: preparing a solution of one or more tin salts in anhydrous solvent and at least one solution of hydride in anhydrous solvent, heating the solution of tin salts to the reaction temperature of the reduction reaction of the tin salt, and starting the reduction reaction when the reaction temperature of the reduction reaction of the tin salt is reached by quick injection of the hydride solution into the solution of one or more tin salts to generate a reaction mixture.

23. The method according to claim 1, wherein the step of synthesizing the M nanoparticles comprises the steps of: preparing a solution of hydride in anhydrous solvent and at least one solution of metal salt in anhydrous solvent, heating the solution of hydride to the reaction temperature of the reduction reaction of the metal salt, and starting the reduction reaction when the reaction temperature of the reduction reaction of the metal salt is reached by quick injection of the one or more metal salt solutions into the solution of hydride to generate a reaction mixture.

24. The method according to claim 1, wherein the step of synthesizing the M nanoparticles comprises the steps of: preparing a solution of one or more metal salts in anhydrous solvent and at least one solution of hydride in anhydrous solvent, heating the solution of metal salts to the reaction temperature of the reduction reaction of the metal salt, and starting the reduction reaction when the reaction temperature of the reduction reaction of the metal salt is reached by quick injection of the hydride solution into the solution of one or more metal salts to generate a reaction mixture.

25. The method according to claim 21, wherein the reaction mixture is cooled to room temperature immediately after injection.

26. A method for producing an anode comprising performing the method of claim 1 for producing MSnx nanoparticles, mixing such obtained MSnx nanoparticles, carbon black, carboxy methyl cellulose (CMC) and water, coating the aqueous slurry obtained on a current collector and drying.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0047] The invention will be better understood and objects other than those set forth above will become apparent when consideration is given to the following detailed description thereof. This description makes reference to the annexed drawings which show:

[0048] FIG. 1. X-ray diffraction (XRD) patterns of Co NPs, Sn NCs, CoSn.sub.x NPs prepared by ball-milling in air and CoSn.sub.2 NCs prepared by ball-milling under nitrogen atmosphere by the method of the invention

[0049] FIG. 2. EDX-spectrum of amorphous Co NPs

[0050] FIGS. 3A-3D. Transmission electron microscopy (TEM) images of Co NPs (FIG. 3A), Sn NCs (FIG. 3B), CoSn.sub.x NPs (FIG. 3C) and CoSn.sub.2 NCs (FIG. 3D)

[0051] FIG. 4. Capacity retention for Sn NCs, CoSn.sub.2 NCs and CoSn.sub.x NPs in lithium-ion half-cells at a current of 1984 mAg.sup.1 within the potential range 0.005-1.0 V

[0052] FIGS. 5A-5C. Galvanic charge/discharge curves for Sn NCs (FIG. 5A), CoSn.sub.2 NCs (FIG. 5B) and CoSn.sub.x NPs (FIG. 5C) corresponding to FIG. 4.

[0053] FIGS. 6A-6C. Cyclic voltammogram of Sn NCs (FIG. 6A), CoSn.sub.2 NCs (FIG. 6B) and CoSn.sub.x NPs (FIG. 6C) tested in a lithium-ion half-cell using a scan rate of 0.1 Vs.sup.1 in the potential range 0.005-1.0 V

[0054] FIG. 7. Rate capability measurements for Sn NCs, CoSn.sub.2 NCs and CoSn.sub.x NPs in Lithium-ion half-cells within the potential range 0.005-1.0 V

[0055] FIGS. 8A-8B. (FIG. 8A) Capacity retention for a CoSn.sub.x NPs lithium-ion full-cell with LiCoO.sub.2 as cathode material at a current of 500 mAg.sup.1 and (FIG. 8B) galvanic charge/discharge curves for the CoSn.sub.x/LiCoO.sub.2 full cell corresponding to (FIG. 8A) with the average discharge voltage as inset.

MODES FOR CARRYING OUT THE INVENTION

[0056] According to the process of the invention, first Sn nanoparticles (NPs) and M NPs are synthesized separately by reducing the respective metal chloride with a solution of hydride in an anhydrous polar solvent.

[0057] In a typical synthesis of Sn or M NPs, in particular Co NPs, a suitable amount of a hydride such as NaBH.sub.4 is dissolved in an appropriate amount of anhydrous polar solvent such as 1-methyl-2-pyrrolidone (NMP) and heated while stirred. For the synthesis of Sn NPs, upon reaching the desired temperature, such as 60 C., a solution of a tin salt, such as SnCl.sub.2, in anhydrous solvent, such as NMP, is injected quickly. For the synthesis of M NPs, upon reaching the desired temperature, such as 150 C. for MCo or 120 C. for MMn, Fe, Ni, a solution of a metal salt, such as CoCl.sub.2, MnCl.sub.2, FeCl.sub.2, NiCl.sub.2, in anhydrous solvent, such as NMP, is injected quickly.

[0058] Solid Sn NPs or M NPs are formed immediately. After the injection the respective suspensions are cooled to room temperature, e.g. with a water-ice bath. The respective obtained materials are separated from their solution by centrifugation and washed once with dimethyl sulfoxide (DMSO) and two times with water to remove unreacted NaBH.sub.4 and water-soluble side-products such as NaCl. The respective reaction products can be finally dried in the vacuum oven at room temperature. Typically the reaction yields the desired product in amounts of 67% for Sn NPs, 98% for Co NPs, 36% for Fe NPs, 16% for Mn NPs and 34% for Ni NPs.

[0059] In the above indicated methods the following chemicals in general are suitably applied to obtain Sn NPs or M NPs. However, to account for the different reactivity of MCl.sub.2 and SnCl.sub.2 different reaction temperatures and precursor concentrations are used:

I. As Anhydrous Solvent Other Than NMP

[0060] Any amide such as hexamethylphosphoramide, 1,3-dimethyl-2-imidazolidinone or 1,3-dimethyl-3,4,5,6-tetrahydro-2(1H)-pyrimidinone.

II. As Substitution for NaBH.SUB.4

[0061] Any alkali or earth alkali hydride such as lithium hydride, sodium hydride, potassium hydride, magnesium hydride, calcium hydride or other metal hydrides such as tributyltinhydride, diisobutyl aluminum hydride, lithium aluminum hydride or lithium triethylborohydride.

III. As Substitution for SnCl.SUB.2

[0062] Any tin halide such as tin fluoride, tin bromide, tin iodide; any tin oxide, tin sulfide, sodium stannate trihydrate, or tetrabutyltin.

IV. As Substitution for MCl.SUB.2

[0063] Any metal halide such as metal fluoride, metal bromide, metal iodide; any metal oxide, metal sulfide or metal sulfate.

[0064] The above indicated chemicals may be used alone or in combination with one or more other members of their respective group I to IV.

[0065] The particles sizes may be influenced by several characteristics such as amount of hydride, reaction temperature and cooling speed.

[0066] Depending on the amount of NaBH.sub.4 employed the size of the NPs can be varied, i.e. the higher the amount of NaBH.sub.4 the smaller the particles. In addition, to produce NPs of small sizes with high yield an excess of NaBH.sub.4 is necessary.

[0067] Sn NPs or M NPs can also be produced at room temperature, however, the formation of smaller NPs is likely to be favored at elevated temperatures.

[0068] Sn NPs with a diameter of approximately 5-10 nm can be obtained by employing about a 96 fold excess of NaBH.sub.4 as reducing agent and fast cooling down directly after the injection of the SnCl.sub.2.

[0069] M NPs with a diameter of approximately 4-10 nm can be obtained by employing about a 4-8 fold excess of NaBH.sub.4 as reducing agent and fast cooling down directly after the injection of the MCl.sub.2.

[0070] The fast cooling down can be achieved by any adequate cooling technique known to the person skilled in the art.

[0071] In addition, it has been found that such syntheses of Sn or M NPs may be performed in air which significantly reduces the costs (material as well as working hours).

[0072] Besides of being easy to perform and comparatively cheap the method for preparing the Sn NPs and M NPs used in the present invention has several advantages compared with methods described in literature. The advantages of this synthetic procedure are the following: [0073] I. No surfactant needs to be used. [0074] II. Reaction can also be done in air. [0075] III. Inexpensive and safe chemicals: the herein preferably used NaBH.sub.4 is the least expensive metal hydride, [0076] IV. Washing procedure: the obtained Sn or M NPs are simply washed with water in air. [0077] V. Depending on the excess of NaBH.sub.4 used and the reaction temperature, the size of the particles can be tuned.

[0078] After the synthesis of the Sn NPs and of the M NPs, mixtures of Sn NPs and M NPs are prepared. The molar ratio of M nanoparticles and Sn nanoparticles in these mixtures is comprised between 1:1 and 1:3.

[0079] The mixtures of Sn NPs and M NPs are ball-milled either in air or under nitrogen with the goal to alloy the materials and obtain MSn.sub.x nanoparticles. Advantageously, the M nanoparticles and Sn nanoparticles are ball-milled for 2 to 4 hours, at a frequency of 1800 to 2400 rpm.

[0080] An anode may be prepared by mixing MSn.sub.x NPs, carbon black, CMC and water, preferably by using a ball-mill for e.g. 1 h. The aqueous slurry obtained is then coated on a current collector like a Cu current collector, and subsequently dried, e.g. overnight at 80 C. under vacuum prior to battery assembly.

Experimental Art

I. Materials Used

[0081] Chemicals and solvents: Tin chloride SnCl.sub.2 (99.9%, Alfa Aesar), CoCl.sub.2 (98%, Sigma-Aldrich), 1-methyl-2-pyrrolidone (NMP, anhydrous, 99.5%, Fisher BioReagents).

[0082] Battery components: Carbon black (CB, Super C65, provided by TIMCAL), carboxymethylcellulose (CMC, Grade: 2200, Daicel Fine Chem Ltd.); fluoroethylene carbonate (FEC, Solvay, battery grade), 1 M solution of LiPF.sub.6 in ethylene carbonate/dimethyl carbonate (EC:DMC:1:1, Merck, battery grade), glass microfiber separator (GF/D, Whatman, Cu foil (9 m, MTI Corporation)

II. Methods

[0083] Synthesis of CoSn.sub.x NPs

EXAMPLE 1

Synthesis of CoSn.SUB.2 .Nanocrystals (NCs)

[0084] According to the invention, the synthesis of CoSn.sub.2 NCs comprises the synthesis of Sn NCs, the synthesis of Co NPs, and the synthesis of CoSn.sub.2 NCs by ball-milling of the Sn NCs and Co NPs:

[0085] Synthesis of Sn NCs:

[0086] In a typical synthesis of Sn NCs, 96 mmol of NaBH.sub.4 were dissolved in 85 mL anhydrous NMP and heated to 60 C. under nitrogen, while stirred mechanically. Upon reaching 60 C. a solution of 1 mmol SnCl.sub.2 previously dissolved in anhydrous NMP was injected quickly and the reaction mixture was immediately cooled to room temperature using a water-ice bath. The reaction product was separated from the solution by centrifugation and washed once with dimethyl sulfoxide and then two times with water. Sn NCs were obtained.

[0087] The reaction yield was 80 mg (67%). The XRD pattern of the obtained product showed only peaks corresponding to crystalline Sn (FIG. 1, indexed to tetragonal Sn, space group l41/amd (141), a=5.831 , c=3.182 , ICDD PDF entry No.: 00-004-0673). Analysis of the reaction product by TEM showed that particles were polydisperse with sizes of 5-10 nm (FIG. 3B).

[0088] Synthesis of Co NPs:

[0089] In a typical synthesis of Co NPs, a similar procedure was used as for Sn NCs with modifications, in particular reaction temperature and precursor concentrations): 32 mmol of NaBH.sub.4 were dissolved in 15 mL anhydrous NMP and heated to 150 C. under nitrogen, while stirred mechanically. Upon reaching 150 C. a solution of 8 mmol CoCl.sub.2 previously dissolved in anhydrous NMP was injected quickly and the reaction mixture was immediately cooled to room temperature using a water-ice bath. The reaction product was separated from the solution by centrifugation and washed once with dimethyl sulfoxide and then two times with water. Co NPs were obtained.

[0090] The reaction yield was 460 mg (98%). The XRD pattern of the obtained product showed that amorphous Co NPs were obtained. FIG. 2 shows the EDX-spectrum of amorphous Co NPs. The peak corresponding to S (about 1 wt % of the sample) might be attributed to residual DMSO. Analysis of the reaction product by TEM showed that particles were polydisperse with sizes of 4-7 nm range (FIG. 3A).

[0091] Synthesis of CoSn.sub.2 Nanocrystals (NCs):

[0092] For the preparation of CoSn based NCs, 1.4 mmol of Sn NCs prepared as above were ball-milled for 4 hours with 0.7 mmol of Co NPs prepared as above, at a frequency of 30 s.sup.1. The beaker for ball-milling was loaded under nitrogen atmosphere and sealed.

[0093] The reaction yield was 200 mg (96%). The XRD pattern of the obtained product showed that ball-milling under inert conditions resulted in the formation of crystalline CoSn.sub.2 nanoalloys (reference patterns: tetragonal SnO.sub.2, space group P42/mnm (136), a=4.7391 , c=3.1869 , ICDD PDF entry 00-077-0448; tetragonal CoSn.sub.2, space group l4/mcm (140), a=6.363 , c=5.456 , ICDD PDF entry 00-025-0256). Analysis of the reaction product by TEM showed that particles were polydisperse with sizes of 6-20 nm (FIG. 3D).

EXAMPLE 2

Synthesis of CoSn.SUB.x .Nanoparticles (NPs)

[0094] For the preparation of CoSn based NPs, 1.4 mmol of Sn NCs prepared as above were ball-milled for 4 hours with 0.7 mmol of Co NPs prepared as above, at a frequency of 30 s.sup.1. The beaker for ball-milling was loaded in air.

[0095] The reaction yield was 200 mg (96%). The XRD pattern of the obtained product showed that ball-milling in air resulted in the formation of amorphous CoSn.sub.x NPs. The major fraction of the samples amorphizes, with only small features corresponding to SnO.sub.2 at 34 and CoSn.sub.2 at 35.5. Analysis of the reaction product by TEM showed that particles were polydisperse with sizes of 6-20 nm (FIG. 3C).

III. Preparation of CoSn-Based Electrodes, Cell Assembly and Electrochemical Measurements

[0096] For electrode preparation, aqueous slurries were prepared by mixing the respective NPs (64 wt. %) with CB (21 wt. %), CMC (15 wt. %) and water as solvent by ball-milling at 500 rpm for 1 hour. The resulting slurries were coated onto copper current collectors, which were dried at 80 C. under vacuum for 12 hours prior to battery assembly. Electrochemical measurements were conducted in air tight coin-type cells assembled in an Ar-filled glove box (O.sub.2<0.1 ppm, H.sub.2O<0.1 ppm) using either elemental lithium for lithium-ion half-cell tests or LiCoO.sub.2 on aluminium foil (MTI) for lithium-ion full-cell tests. A piece of glass microfiber was used as separator. As electrolyte 1M LiPF.sub.6 in EC:DMC with 3% FEC was used. FEC is added to the electrolyte to improve cycling stability. Galvanostatic cycling tests were carried out at room temperature on MPG2 multi-channel workstation (BioLogic). Capacities were normalized by the mass of Co-Sn nanoparticles for both half and full-cell tests, excluding CB and the binder.

IV. Characterization

[0097] Transmission Electron Microscopy (TEM) images were obtained with a Philips CM30 TEM microscope at 300 kV using carbon-coated Cu grids as substrates (Ted-Pella). Energy-dispersive X-ray spectroscopy (EDX) measurements were carried out using a NanoSEM 230. Powder X-ray diffraction (XRD) was measured on a STOE STADI P powder X-ray diffractometer.

V. Electrochemical Results

[0098] FIG. 4 shows the capacity retention of CoSn based NPs over 1500 cycles at a high current of 1984 mAg.sup.1 in the potential range 0.005-1.0 V. The current of 1984 mAg.sup.1 corresponds to a rate of 2C for Sn based on the theoretical capacity of 992 mAhg.sup.1 for the formation of Li.sub.4.4Sn. Assuming that Co does not contribute to the capacity, the theoretical capacity of CoSn.sub.x NPs and CoSn.sub.2 NCs is with 795 mAhg.sup.1 accordingly lower compared to pure Sn. For galvanostatic cycling tests the upper cut-off potential was limited to 1.0 V in order to only include processes corresponding to high energy density in full-cells. As can be seen in FIG. 4 for galvanostatic cycling at 1984 mAg.sup.1 Sn NCs as well as CoSn.sub.x NPs and CoSn.sub.2 NCs show capacities of 570 mAhg.sup.1, after rapid increase of the capacity during the first 100 cycles. Whereas Sn NCs show significant capacity fading after 400 cycles, CoSn based NPs show much better capacity retention. In particular, for CoSn.sub.2 NCs after 1500 cycles still 462 mAhg.sup.1 are retained. For CoSn.sub.x NPs capacity retention is even better with 525 mAhg.sup.1 corresponding to only 8% fading over 1500 cycles at a current of 1984 mAg.sup.1. Therefore the CoSn.sub.x NPs obtained by the method of the invention have an ultrahigh cycling stability. The superior cycling stability of CoSn.sub.x NPs involving Co compared to pure Sn NCs might be attributed to two effects. Due to the fact that Co does not form lithium-alloys it can serve as inactive matrix during cycling and therefore buffer the volume changes caused by the lithiation/delithiation of Sn. Moreover, the presence of Co can prevent Sn NCs from aggregation and therefore further improve cycling stability. The difference between CoSn.sub.2 NCs and CoSn.sub.x NPs in terms of cycling stability might be attributed to the fact that CoSn.sub.x NPs are more oxidized due to their preparation by ball-milling in air. The higher content of oxides possibly results in the formation of a more effective Li.sub.2O matrix to buffer volume changes and inhibit sintering of Sn domains during cycling. It should be noted that for all three systems the average coulombic efficiency is 99.6% during cycling, after values of 30% were obtained for the first discharge cycle due to the solid electrolyte formation. The average delithiation potential for Sn NCs, CoSn.sub.2 NCs and CoSn.sub.x NPs are equally low with a stable value of 0.5 V vs. Li.sup.+/Li during cycling (FIGS. 5A-5C and FIGS. 6A-6C).

[0099] To evaluate the rate capability of the CoSn based NPs, galvanostatic cycling tests at current rates between 0.2C to 10C were carried out (FIG. 7, 1C=992 mAg.sup.1). Due to the small size of the NPs and therefore enhanced reaction kinetics in all cases similarly good rate capability was observed, though for currents of 0.5C-2C Sn NCs showed by 50 mAhg.sup.1 lower capacities compared to CoSn.sub.2 NCs. For rates as high as 10C all three materials still retain a capacity of 350 mAhg.sup.1. Interestingly, it can be observed that at such high current capacities increase during cycling, resulting in same or even higher capacities were obtained during stepwise decrease of the rate back to 0.2C. Especially for CoSn.sub.x NPs the slight difference in capacity to CoSn.sub.2 NCs observed initially at the rates of 0.5C-2C diminishes fully during cycling.

[0100] In order to test the applicability of CoSn based NPs under more practical conditions, anode-limited full-cell tests using LiCoO.sub.2 as cathode were carried out. CoSn.sub.x NPs were chosen as anode material, because of their superior capacity retention compared to Sn and CoSn.sub.2 NCs. Herein, all capacities and currents are related to the mass of CoSn.sub.x NPs. Full-cells of CoSn.sub.x NPs/LiCoO.sub.2 were initially charged to 2000 mAhg.sup.1 to account for the irreversible charge loss in the first cycle. For subsequent cycling charge and discharge were limited to 500 mAhg.sup.1. Cycled under these conditions at a current of 500 mAg.sup.1 CoSn.sub.x NPs show stable capacities with an average discharge voltage of 3.2 V for 50 cycles. Based on the anode capacity and discharge voltage one roughly estimates the specific energy density of CoSn.sub.x NPs to be comparable to graphite (372 mAhg.sup.1, 3.6 V vs. LiCoO.sub.2). However, given the much higher density of bulk Sn (7.3 gcm.sup.3) and Co (8.9 gcm.sup.3) compared to graphite (2.2 gcm.sup.3) using CoSn.sub.x NPs can potentially improve the volumetric energy density by up to factor 4.

[0101] FIGS. 8A-8B show the electrochemical performance of a CoSn.sub.x NPs lithium-ion full-cell with LiCoO.sub.2 as cathode material: FIG. 8A: Capacity retention at a current of 500 mAg.sup.1. FIG. 8B: Galvanostatic charge/discharge curves for the SnSb/LiCoO.sub.2 full cell corresponding to (FIG. 8A) with the average discharge voltage as inset. Cells were cycled with limitation of charge and discharge capacity to 500 mAhg.sup.1. Displayed capacities and currents are related to the mass of CoSn.sub.x NPs.

[0102] In conclusion, the method of the invention allows to synthesize Co NPs and Sn NCs with diameters nm via simple reduction of the respective metal chlorides with NaBH.sub.4 in NMP and subsequently converted them into intermetallic crystalline and amorphous CoSn nanoalloys by ball-milling. Though CoSn.sub.2 NCs show good cycling stability for several hundred cycles, amorphous CoSn.sub.x NPs show outstanding capacity retention with only 8% fading over 1500 cycles at 1984 mAg.sup.1. In addition, tested in lithium-ion full-cells with LiCoO.sub.2 as cathode material CoSn.sub.x NPs provide stable capacities of 500 mAhg.sup.1 with an average discharge voltage of 3.2 V. Given the inexpensive and easily upscalable preparation method and their excellent electrochemical properties characterized by high cyclability as well as high volumetric and specific energy densities, the herein presented CoSn.sub.x NPs have a great potential as high-performance anode materials for Li-ion and Na-ion batteries

[0103] While there are shown and described presently preferred embodiments of the invention, it is to be distinctly understood that the invention is not limited thereto but may be otherwise variously embodied and practiced within the scope of the following claims.

REFERENCES

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