ULTRAFAST ELECTROPLATING OF CARBON AS A COATING AGENT FOR LITHIUM ION BATTERY APPLICATIONS

Abstract

A method of electroplating (or electrodeposition) carbon to coat anode and cathode active materials used in Li-ion batteries (LIBs) for improving their cycle life. The electroplating of the carbon coating from the carbon source is ultrafast, preferably taking less than 10 seconds. The carbon source can be comprised of an acetonitrile, methanol, ethanol, acetonitrile, nitromethane, nitroethane or N,N-dimethylformamide (DMF) solution. The protective carbon coating may be used also in gas sensors, biological cell sensors, supercapacitors, catalysts for fuel cells and metal air batteries, nano and optoelectronic devices, filtration devices, structural components, and energy storage devices.

Claims

1. A method of electrodepositing a protective carbon coating on to the surface of cathode or anode materials used in Li-ion batteries, using an organic solvent, the method comprising: (a) immersing a working electrode and a counter electrode into an organic solvent comprising a carbon source in an ambient atmosphere; (b) electrodepositing a carbon coating onto a surface of the working electrode from the organic solvent at a temperature ranging from about −5° C. to about 50° C.; (c) removing the carbon coated working electrode from the organic solvent; (d) rinsing the carbon coated working electrode with the organic solvent in which the carbon was electrodeposited; and (e) drying the carbon coated working electrode under vacuum.

2. The method of claim 1, wherein the carbon source is a solution selected from the group consisting of acetonitrile, methanol, ethanol, nitromethane, nitroethane and N,N-dimethylformamide (DMF) and mixtures thereof.

3. The method of claim 2, wherein the carbon source is an acetonitrile solution.

4. The method of claim 1, wherein the thickness of the protective carbon coating ranges from about 1 nm to about 5 um.

5. The method of claim 1, wherein the electrodepositing in step (b) is carried out at room temperature and under ambient atmosphere.

6. The method of claim 1, wherein the drying of the working electrode in step (e) is carried out under dynamic vacuum at a temperature of about 60° C.

7. The method of claim 1, wherein the working electrode used for electrodeposition is comprised of an anode active material used in Li-ion batteries and selected from the group consisting of silicon, graphite, graphene-based anodes, tin, and combinations thereof.

8. The method of claim 7, wherein the anode active material used in Li-ion batteries is silicon.

9. The method of claim 1, wherein the working electrode used for electrodeposition is comprised of a cathode active material used in Li-ion batteries selected from the group consisting of LiCoO.sub.2 (LCO), LiMn.sub.2O.sub.4 (LMO), LiMnNiCoO.sub.2 (NMC), LiFePO.sub.4 (LFP), LiNiCoAlO.sub.2 (NCA), Li-rich Li.sub.2MnO.sub.3.LMnNiCoO.sub.2 (LRNMC) electrodes and combinations thereof.

10. The method of claim 9, wherein the cathode active material used in Li-ion batteries is selected from the group consisting of LiCoO.sub.2 (LCO), LiMn.sub.2O.sub.4 (LMO), and combinations thereof.

11. The method of claim 1, wherein the counter electrode is selected from the group consisting of nickel, tungsten, copper, gold, platinum, titanium, carbon and mixtures thereof.

12. The method of claim 1, wherein the counter electrode is nickel.

13. The method of claim 1, wherein the electrodepositing of the carbon coating in step (b) takes less than 10 seconds.

14. The method of claim 1, wherein a voltage of from about 300 volts to about 2000 volts is applied to the counter electrode in step (b).

15. The method of claim 14, wherein about 1200 volts is applied to the counter electrode in step (b) for about 6 seconds.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0014] FIG. 1. Picture of experimental apparatus used to apply high voltage to the counter electrode to break down the acetonitrile and produce carbon film on working electrode.

[0015] FIG. 2. Picture of a depositional set up where the acetonitrile is filled up.

[0016] FIG. 3. Cycle life of NMC/Si full cells where Si was coated with carbon. Carbon coating treatment was done at 1200V, 6 s on, 300° C. 20 min heat treatment under Argon.

[0017] FIG. 4. Raman spectra of pristine Si and carbon deposited Si electrodes at different deposition potential

[0018] FIG. 5A. SEM image of pristine Si on Ni scaffold

[0019] FIG. 5B. SEM image of after carbon deposition of Si on Ni scaffold

[0020] FIG. 6. SEM images showing the homogeneity of carbon deposition across the Si electrode

[0021] FIGS. 7A-F. SEM images showing application of carbon coating to other conventional cathode and anode chemistries

[0022] FIGS. 8A & 8B. Raman spectra of pristine Si and carbon coating applied to other conventional cathode and anode chemistries

[0023] FIG. 9A. XPS analysis on ultrafast carbon coated Si on 80 um Xerion Ni foam showing spectrum of Si 2p core level emission.

[0024] FIG. 9B. XPS analysis on ultrafast carbon coated Si on 80 um Xerion Ni foam showing spectrum of C 1S core level emission.

[0025] FIG. 10A. SEM image of carbon deposition of Si on Ni scaffold when there was a 0.5 inch distance between the working electrode (W.E.) and the counter electrode (C.E).

[0026] FIG. 10B. SEM image of carbon deposition of Si on Ni scaffold when there was a 1 inch distance between the working electrode (W.E.) and the counter electrode (C.E).

[0027] FIG. 11A. SEM image of carbon deposition of Si on in-house produced Ni foam that has paired with commercial Ni scaffold having a low surface area as counter electrode.

[0028] FIG. 11B. SEM image of carbon deposition of Si on in-house produced Ni foam that has paired with in house produced Ni scaffold having a high surface area as counter electrode.

[0029] FIG. 12. The graph shows cycle life of two different electroplating potentials of carbon. The NMC/Si full cell with square symbol where Si was coated at 1200V and NMC/Si with round symbol where Si was coated at 2000V.

DETAILED DESCRIPTION OF THE INVENTION

[0030] As illustrated in FIG. 1, a high voltage (i.e., 1200V) was applied to the counter electrode to break down the acetonitrile and produce a carbon film on the working electrode which can be anode or cathode active materials for LIBs. Note that although 1200V was used for this particular experimental set up, other voltages work and give different attractive properties. For example, voltages in the range of from about 300V to about 2000V should also work.

[0031] Total deposition time can vary to modify the thickness of the carbon coating. Wave form of deposition can also change, constant voltage, constant current, pulse voltage or current and combination thereof. Currently, Applicants use 1200V 6s on time for coating. The higher potential gives thicker carbon deposition while also the longer deposition gives thicker carbon deposits.

[0032] Traditionally carbon coating on Si anode takes several hours (see e.g., Nonfilling Carbon Coating of Porous Silicon Micrometer-Sized Particles for High-Performance Lithium Battery Anodes, Zhenda Lu, Nian Liu, Hyun-Wook Lee, Jie Zhao, Weiyang Li, Yuzhang Li, and Yi Cui, C S Nano, 2015, 9 (3), pp 2540-2547).

[0033] As illustrated in FIG. 2, electroplating of a carbon coating was carried out by

[0034] immersing a working electrode and two counter electrodes into an acetonitrile solution in ambient atmosphere; electrodepositing carbon onto the surface of the working electrode at room temperature; removing the working electrode from the bath; drying the working electrode under dynamic vacuum at 60° C. and if desired and appropriate heat the sample up to 300° C. for 15 minutes to increase silicon carbon adhesion.

[0035] As illustrated in FIG. 3, application of the ultrafast carbon coating process results in the enhancement of cycle life in a real battery system. In particular, a carbon coating treatment 1200V, 6 s on, 300° C. 20 min heat treatment under Argon was carried out by full cell with 4.2 mAh/cm2 cathode-4.6 mAh/cm2 anode, cycled between 4.15-2.5V @C/2 charge and discharge. Both cells contain same metal scaffold plated with Si from organic solvents. Both cells also contain the same commercial electrolyte from SoulBrain. The electrolyte consists of 1.2M LiPF6 salt dissolved in organic solvent which is also a mixture of ethylmethyl carbonate, ethylene carbonate, diethyl carbonate, dimethyl carbonate solvents. The ultrafast carbon coated Si showed superior cycle life as compared to the bare Si electrode.

[0036] FIG. 4 illustrates the Raman spectra of pristine Si and carbon deposited Si electrodes at different deposition potential. The conventional peaks for carbon can be seen at 1360 and 1600 cm−1 wavelength, which indicates that the ultrafast carbon coating process has formed a carbon coating on the silicon electrode. At all deposition potentials the carbon peaks are formed. The Si characteristic peak (around 500 cm−1) is getting less intense suggesting the carbon film formation. The width of D band in carbon peak usually signifies disordered nature of carbon which might indicate graphitic carbon is preferentially formed at 1200V compared to other deposition potentials which do not show that much of a wide D band peak.

[0037] FIG. 5A is an SEM image of pristine Si on Ni scaffold and

[0038] FIG. 5B is an SEM image after Carbon Deposition of Si on Ni scaffold demonstrating the actual carbon particles. The arrows in FIG. 5B indicate where the carbon films formed on the surface of the Si anode electrode.

[0039] FIG. 6 contains 3 SEM images taken along the length of the Si electrode. The 3 SEM images show the homogeneity of carbon deposition across the Si electrode.

[0040] FIGS. 7A-F are all SEM images showing application of carbon coating to other conventional cathode and anode chemistries. It is clear from these images that carbon coating can be applied to other conventional cathode and anode chemistries, which will enhance their electrochemical properties like cycle life, power, and charge time.

[0041] FIGS. 8A & 8B illustrate Raman spectra of pristine Si and carbon coating applied to other conventional cathode and anode chemistries. Since slurry based commercial electrodes have carbon source blended with active material, it is hard to distinguish carbon peaks due to the carbon that is already incorporated in the electrode. For this reason a XABC LCO electrode, which does not contain carbon, was selected to demonstrate the ability of this method to coat cathode materials. It should be interpreted from this demonstration that carbon can also be coated on conventional cathode materials.

[0042] FIG. 9A is an XPS analysis on ultrafast carbon coated Si on 80 um Xerion Ni foam showing spectrum of Si 2p core level emission. It was coated from acetonitrile at various voltages using a 6 second voltage pulse. The peak at ˜100 eV corresponds to metallic silicon while the peak at ˜104 eV corresponds to SiO.sub.2. The energies between 100 eV and 104 eV correspond to the silicon sub-oxides, such as, Si.sub.2O, SiO, and Si.sub.2O.sub.3. XPS is extremely surface sensitive (˜10 nm penetration depth—typical), and as a result the intensity of the silicon emissions diminish as the deposition voltage is increased. The carbon film becomes thicker with higher deposition voltages. In addition, there is a slight shift towards lower binding energy for the films coated at 1200V and 1500 V possibly because a small amount of silicon carbide is formed. The formation of silicon carbide is beneficial because the adhesion of the carbon film is chemically bound to the silicon.

[0043] FIG. 9B is an XPS analysis on ultrafast carbon coated Si on 80 um Xerion Ni foam showing spectrum of C 1S core level emission. It was coated from acetonitrile at various voltages using a 6 second voltage pulse. The peak at ˜285 eV corresponds to c—c bonds while the broad shoulders at higher eV correspond to oxidized forms of carbon, such as, carbon connected to ether, carbonyl, and carboxylic groups. The shoulder of 1200 eV at lower binding energy corresponds to sp2-forms of carbon. Most materials analyzed by XPS will show sp3 carbon emission, which is call the adventitious carbon signal—even on materials that are not carbon coated. The carbon signal in FIG. 9B shows a high degree of sp2, sp3 and oxidized carbon, and therefore indicates the presence of a carbonaceous film which was applied from the electrochemical deposition.

[0044] Analysis of both spectra simultaneously, combined with the Raman spectroscopy data proves unequivocally the presence of electrodeposited carbon.

[0045] As illustrated in FIGS. 10A and 10B, the distance between the working electrode (W.E.) and counter electrode (C.E.) greatly affects the homogeneity of the carbon coating. FIG. 10A, with a 0.5 inch distance between the W.E. and C.E., shows a thick carbon coating on the surface versus the 1 inch distance between the W.E. and C.E. in FIG. 10B which shows less agglomeration on the surface. Both FIGS. 10A and 10B show the Si deposited Ni foam.

[0046] As illustrated in FIGS. 11A and 11B, finding the right surface area of the counter electrode is important for obtaining a conformal carbon coating. FIG. 11A, with a commercial Ni foam having a low surface area, does not produce the uniform deposition of carbon particles shown in FIG. 11B obtained by using an in-house produced Ni foam having a high surface area.

[0047] FIG. 12 shows how the deposition potential affects the cycle life performance of Si based LIB. In particular, FIG. 12 shows a carbon coating treatment at 1200V and 2000V, in an NMC/Si full cell treatment under Argon. FIG. 12 shows the superiority of 1200V as compared to 2000V.

[0048] In general, the present invention discloses a method of electrodepositing a carbon coating onto the surface of a working electrode, i.e. cathode or anode materials used in LIBs, comprising the steps of:

[0049] a) immersing a working electrode and counter electrode into an organic solvent comprising a carbon source (e.g., acetonitrile solution) in ambient atmosphere;

[0050] b) electrodepositing a carbon coating onto a surface of the working electrode from the organic solvent at room temperature;

[0051] c) removing the working electrode from the organic solvent;

[0052] d) rinsing the electroplated carbon coated working electrode; and

[0053] e) drying the working electrode under dynamic vacuum at 60° C.

[0054] The carbon source can be comprised of an acetonitrile, methanol, ethanol, nitromethane, nitroethane, or N,N-dimethylformamide (DMF) solutions or other carbon bond containing solvents and mixtures thereof. These organic solvents have carbon bonds where DC potentials are applied to break them and deposit carbon on working electrode.

[0055] The thickness of the carbon coating ranges from 1 nm to 5 um.

[0056] The electroplating is carried out in a wide range of temperature ranging from −5° C. up to 50° C. Preferably, the electroplating is carried out at room temperature and under ambient atmosphere.

[0057] The electroplating of the carbon coating is ultrafast, typically taking less than 10 seconds. In a preferred embodiment, 1200 volts is applied to the counter electrode in step (b) for about 6 seconds.

[0058] The working electrode is preferably rinsed with the organic solvent in which the carbon is plated from. For example, if the electrodeposition of carbon is carried out in acetonitrile the working electrode is rinsed with acetonitrile after carbon coating.

[0059] The working electrode is preferably dried under dynamic vacuum at a temperature of about 60° C.

[0060] The conductive counter electrode substrate used for electrodeposition preferably comprises at least one of nickel, tungsten, copper, gold, platinum, titanium, and carbon. In a preferred embodiment, the counter electrode is nickel. Fiber or foam version of these electrodes can be used if higher current densities are desired.

[0061] The working electrode during electroplating of carbon can be an either cathode or anode active materials for LIBs. The cathode materials can be LiCoO.sub.2 (LCO), LiMn.sub.2O.sub.4 (LMO), LiMnNiCoO.sub.2 (NMC), LiFePO.sub.4 (LFP), LiNiCoAlO.sub.2 (NCA), Li-rich Li.sub.2MnO.sub.3.LMnNiCoO.sub.2 (LRNMC) electrodes and combinations thereof. It can also be doped with different transition metals of LCO, LMO, NMC, NCA, LFP and LRNMC. The anode materials can be silicon, graphite, graphene based anodes, tin, and other anode materials that can be used in Li-ion or other energy storage systems. Both cathode and anode materials may consist of composite electrode which contain binder and conductive additives.

[0062] In a preferred embodiment, the anode active material is silicon.

[0063] In another preferred embodiment, the cathode active material is selected from the group consisting of LiCoO.sub.2 (LCO), LiMn.sub.2O.sub.4 (LMO), and combinations thereof.

[0064] The invention described here can be applied to cathodes and anodes of other battery and energy storage technologies like next generation Li-ion, Na-ion, Na-air, Li-air, Li—S batteries, supercapacitors etc.

[0065] In addition, this invention can be applied to battery components that are used to make solid state batteries. For example, it can be used as an engineered interface between cathodes or anodes and a solid state electrolyte to decrease the interfacial resistance. The carbon coating could be applied on a densely formed cathode or anode that may have been formed by sputtering, electrodeposition, or traditional methods.

[0066] Additionally, to meet the requirement of non-electrical conductivity, a thin non-conductive layer would be applied between the cathode or anode and solid-state electrolyte interface. This coating could consist of precisely electrodeposited silicon that is converted into electronically resistive silicon carbide through a post anneal treatment. Carbon is well known to be a good ionic conductor for Li-ions.