To meet the current and future energy storage requirements, much effort has been undertaken to explore novel reaction mechanisms and feasible materials for constructing safer and better energy storage systems. Among the various new materials being suggested for electric vehicle (EV) and hybrid electric vehicle (HEV) applications, electrochemical conversion materials have emerged as likely candidates for significant breakthroughs in storage capacity. For example, commercial lithium batteries primarily use graphite-based anodes, which have a specific capacity of 372 mAh g−1 (LiC6). Alternative anodes based on lithium-metal alloys have been actively pursued in recent years. Among these lithium-metal alloys, an alloy with silicon (Li21Si5) has the highest theoretical specific capacity (nearly 4200 mAh g−1). However, very large volume changes (often more than 300 percent increase in volume) typically occur in the material when the lithium and silicon are alloyed. This large volume change can cause severe cracking and pulverization of an electrode, and lead to significant capacity loss.
In addition to Li—Si based alloys, a vast array of other lithium containing alloys (Li-A, where A represents Sn, Al, Bi, Ge, In, Sb, etc) and binary compounds (M-X, where M represent transition metal and X=F, O, S, and N) have been reported to exhibit superior reversible energy storage capacities that are several times higher than those observed by currently used cathode or anode materials. In particular, a large family of transition metal oxides, such as FeO, CoO, Cu2O, etc., can exhibit, through the conversion reaction, a reversible capacity that is two to four times higher than presently commercialized graphite anodes. Based on this improved performance, these materials appear to have the potential for use as safer and higher-capacity materials that could replace carbonaceous anodes. However, many of these transition metal oxides or lithium containing alloys, like Li—Si alloys, exhibit a large volume change during charge/discharge processes. The volumetric change in these materials can result in severe cracking and pulverization of the electrode, and lead to significant capacity loss. These materials may also exhibit undesirable capacity fading and low initial Coulombic efficiency from undesirable, often irreversible, conversion reactions. Therefore, there is an urgent need for an electrode material with high capacity and good reversibility that can be synthesized in a cost effective method.
This document describes a functional nanocomposite material, an electrode comprising the nanocomposite material, and energy storage systems having such electrodes, as well as methods for making these functional nanocomposite materials. The nanocomposite material is characterized by nanoparticles comprising an active material, a core particle comprising a comminution material, and a thin electronically conductive coating comprising an electronically conductive material. The nanoparticles are fixed between the core particle and the conductive coating. The comminution material has a Mohs hardness that is greater than that of the active material. In one embodiment, the ratio of the core particle average diameter to the nanoparticle average diameter is between 2 and 50. In another embodiment, the core particle has a diameter less than 5000 nm and the nanoparticles have diameters less than 500 nm.
The functional nanocomposite material can be arranged as an electrode. One example includes, but is not limited to, mixing the nanocomposite material with a binder and forming the mixture into an electrode.
As used herein, an active material can refer to a material exhibiting performance characteristics that are better than those of traditional electrode materials. Examples of performance characteristics include, but are not limited to, capacity, cyclability, safety, high temperature and low temperature stability, and power rate. For example, if the nanocomposite material were arranged as an anode in an energy storage system, a suitable active material might have a capacity greater than that of graphite (372 mAh·g−1). Often times, suitable active materials exhibit large volume expansion during physical, chemical, or electrochemical operation. The volume expansion can be caused by electrochemical reaction, chemical reaction, mechanical force, electromagnetic force, temperature, and/or humidity variation during operation as an electrode in an energy storage system.
In some embodiments, the active material of the nanoparticle can comprise tin and/or tin oxide, silicon and/or silicon oxide, germanium and/or germanium oxide, aluminium and/or aluminium oxide, or indium and/or indium oxide. In a particular embodiment, a nanocomposite material having nanoparticles comprising tin and/or tin oxide as the active material can have a reversible capacity of at least 400 mAh·g−1 based on whole electrode weight when operated over 100 cycles. In an embodiment wherein the nanoparticles comprises silicon and/or silicon oxide, the reversible capacity can be at least 550 mAh·g−1 based on whole electrode weight over 100 cycles. In preferred embodiments, the nanoparticles have diameters that are less than or equal to 50 nm.
In some embodiments, the comminution material is electrically conductive. For example, the comminution material can have a conductivity that is greater than 1 S/m. Particular examples of comminution materials (some of which are conductive) can include, but are not limited to boron carbide, tungsten carbide, titanium carbide, silicon carbide, and combinations thereof. The core particle, in some embodiments, is less than or equal to 1000 nm in diameter.
In some embodiments the conductive material comprises a carbonaceous material. Examples of carbonaceous materials can include, but are not limited to, graphene, few-layer graphene, graphite, ketjenblack, carbon black, Super P carbon black, carbon fibers, carbon whiskers, soft carbon, other carbonaceous material, and combinations thereof. Alternatively, the conductive material can comprise a conductive polymer. In still another embodiment, the conductive material can comprise a powder having metal particles. Preferably, the conductive coating is less than or equal to 50 nm thick.
The overall composition of the nanocomposite material can comprise 10-90 wt % active material, 5-85 wt % comminution material, and 5-85 wt % conductive material. The weight ratio of active material to the comminution material and to the conductive material can range from 18:1:1 to 2:17:1 or 2:1:17, respectively. Referring to these three weight ratios (18:1:1, 2:17:1, or 2:1:17), since there are three components (active, comminution, and conductive materials), the latter two compositions (2:17:1 and 2:1:17) have relatively small amounts of active material. Preferred embodiments have compositions in which the active material in the ternary composite is approximately 40 wt %. Furthermore, in preferred embodiments the comminution material and the conductive material have a weight ratio that is approximately 1:1. In one example, the weight ratio is 4:3:3, respectively.
One embodiment of an electrode can comprise a nanocomposite material characterized by nanoparticles comprising an active material, a core particle comprising a comminution material having an electrical conductivity greater than 1 S/m, and a thin electronically conductive coating comprising a carbon material. The nanoparticles are fixed between the core particle and the conductive coating, wherein the comminution material has a Mohs hardness greater than that of the active material. The core particles have an average diameter less than 1000 nm, and the nanoparticles have average diameters less than 200 nm. The electrode, when operated in a cell, has a capacity greater than 400 mAh·g−1 based on whole electrode weight after 100 cycles. Preferably, the capacity is greater than 550 mAh·g−1 based on whole electrode weight after 100 cycles.
In one embodiment of an energy storage device having a cathode and an anode, the anode comprises a nanocomposite material. The nanocomposite material is characterized by nanoparticles comprising an active material, a core particle comprising a comminution material, and a thin electronically conductive coating comprising an electronically conductive material. The nanoparticles are fixed between the core particle and the conductive coating, wherein the comminution material has a Mohs hardness greater than that of the active material. The core particle has a diameter less than 5000 nm, and the nanoparticles have diameters less than 500 nm. In some instances, the cathode can comprise lithium, lithium intercalation materials, lithium conversion materials, or combinations thereof.
One method of making the nanocomposite material comprises comminuting a first mixture comprising an active material and a comminution material until particles of the active material are less than 500 nm in average diameter and particles of the comminution material are less than 5000 nm in average diameter. The comminution material has a Mohs hardness greater than the active material. Particles of the active material can become fixed on the particles of the comminution material while performing said comminuting step, thereby yielding an intermediate nanocomposite. Mixing an amount of an electronically conductive material with the first mixture can result in coating the intermediate nanocomposite with the electronically conductive material to yield the final nanocomposite material. In some instances, the mixing step can also involve additional comminution.
In various embodiments, the first mixture can comprise 10-95 wt % active material. In other embodiments, the first mixture can comprise 5-90 wt % comminution material. In still other embodiments, the amount of the electronically conductive material is 5-85 wt % of the conductive material and first mixture total weight.
In some embodiments, the comminuting can proceed until the particles of the active material are less than 200 nm in diameter and particles of the comminution material are less than 2000 nm in diameter. In other embodiments, comminuting proceeds until the particles of the active material are less than 100 nm in diameter and particles of the comminution material are less than 1000 nm in diameter. One example of comminuting includes, but is not limited to ball milling.
The purpose of the foregoing abstract is to enable the United States Patent and Trademark Office and the public generally, especially the scientists, engineers, and practitioners in the art who are not familiar with patent or legal terms or phraseology, to determine quickly from a cursory inspection the nature and essence of the technical disclosure of the application. The summary is neither intended to define the invention of the application, which is measured by the claims, nor is it intended to be limiting as to the scope of the invention in any way.
Various advantages and novel features of the present invention are described herein and will become further readily apparent to those skilled in this art from the following detailed description. In the preceding and following descriptions, the various embodiments, including the preferred embodiments, have been shown and described. Included herein is a description of the best mode contemplated for carrying out the invention. As will be realized, the invention is capable of modification in various respects without departing from the invention. Accordingly, the drawings and description of the preferred embodiments set forth hereafter are to be regarded as illustrative in nature, and not as restrictive.
Embodiments of the invention are described below with reference to the following accompanying drawings.
a-2e includes transmission electron microscope (TEM) micrographs of a nanocomposite material according to embodiments of the present invention.
d is an illustration depicting the formation and structure of a nanocomposite material according to embodiments of the present invention.
a includes cyclic voltammetry curves of a nanocomposite material according to embodiments of the present invention.
b-d include graphs illustrating the electrochemical performance of nanocomposite materials described herein and applied as anodes.
a includes an X-ray photoelectron spectroscopy (XPS) spectrum acquired from nanocomposite materials described herein.
b is a TEM micrograph of a nanocomposite material described herein.
a-c include diagrams and TEM micrographs depicting the formation and structure of a nanocomposite material described elsewhere herein.
a includes XRD patterns of various nanocomposite materials described elsewhere herein.
b-d include CV data for various nanocomposite materials described elsewhere herein.
The following description includes the preferred best mode of one embodiment of the present invention. It will be clear from this description of the invention that the invention is not limited to these illustrated embodiments but that the invention also includes a variety of modifications and embodiments thereto. Therefore the present description should be seen as illustrative and not limiting. While the invention is susceptible of various modifications and alternative constructions, it should be understood, that there is no intention to limit the invention to the specific form disclosed, but, on the contrary, the invention is to cover all modifications, alternative constructions, and equivalents falling within the spirit and scope of the invention as defined in the claims.
In one example, a nanocomposite material was synthesized and characterized for use as an electrode in an energy storage system. The nanocomposite of the instant example comprised SnO2 as the active material, SiC as the comminution material, and graphite (G) as the conductive material. SnO2 (99.5% purity, ˜200 mesh National medicine Co., Ltd, China Shanghai, hereafter called m-SnO2), nano-SnO2 (99.9% purity, ˜40 nm Alfa Aesar, hereafter called n-SnO2), sphere-like SiC (99.5% purity, ten to a few hundred nanometers in diameter), and graphite (99% purity) were used as received. The SnO2—SiC/G nanocomposites (SiC: SnO2: C=20:70:10 wt %) were prepared by high-energy ball milling of the mixture of SiC and m-SnO2 powders (8000M Mixer/Mill, SPEX, USA) for 20 h at 1725 rpm and then by ball milling the SnO2—SiC composites with graphite by a planetary mill (QM-1SP04, Nanjing, China) at a rotation speed of 240 rpm for 6 h. The weight ratio of milling balls to the powder materials was maintained at 20 to 1.
The crystalline structure of the as-prepared nanocomposites was characterized by XRD on a Shimadzu x-ray diffractometer using Cu Ka radiation. XRD data were obtained at 2θ=10-80°, with a step size of 0.02°. From the XRD data, the lattice parameters were calculated based on the Scherrer equation (d=0.9λ/(β cos θ). XPS measurements were carried out with a Kratos XSAM800 Ultra spectrometer. The morphologies of the composite particles were characterized by TEM (JEOL 2010).
The electrochemical evaluation of the prepared functional nanocomposite materials were carried out with a half-cell configuration using 2016-type coin cells. Stainless steel was used as the current collector, and Li foil was used as the counter and reference electrode. The electrolyte was 1-M LiPF6 dissolved in a mixture of ethylene carbonate (EC), dimethyl carbonate (DMC), and ethylene methyl carbonate (EMC) (1:1:1 by weight, Shinestar Battery Materials Company Ltd, China), and the separator was a microporous membrane (Celgard® 2400). The composite anode was prepared by mixing 70 wt % composite powder, 22 wt % acetylene black, 4 wt % carboxymethyl cellulose (CMC) and 4 wt % styrene butadiene rubber (SBR), and dissolving the electrode mixture into distilled water to form a slurry. Then, the electrode slurry was coated on a nickel foam, pressed, and dried at 80° C. for 10 hours under vacuum. The cells were assembled in an argon-filled glove box and galvanostatically charged and discharged using a battery tester (Land CT2001A, Wuhan, China) at room temperature. The electrochemical capacity was calculated based on the SnO2 mass and on the whole electrode weight (e.g., active material, comminution material, conductive material and binder). CV measurements also were carried out with the three-electrode cell at a scan rate of 0.1 mV s−1.
The crystalline structures of the SnO2—SiC/G nanocomposite materials were characterized using x-ray powder diffraction (XRD). The diffraction peaks of SnO2 in the nanocomposite materials appeared much weaker and broader compared to the XRD patterns of the pure m-SnO2 sample shown in
The morphology of the as-prepared nanocomposite was studied using transmission electron microscopy (TEM) (
SiC particles can play a role as a comminution material in obtaining the structure shown in the TEM images. The SiC can be introduced into the ball-milling process as an abrasive for its high rigidity (9.3 on the Mohs' scale of hardness) to reduce bulk SnO2 grains to nanometer-sized particles and to function as a support, with its abundant surface area (90 m2/g), for the SnO2 nanoparticles. The illustration in
The properties of SnO2—SiC/G material were studied using a voltage window of 1.5 to 0.01 V for the following alloying reaction.
SnO2+4Li++4e−→Sn+2Li2O (1)
Sn+xLi++xe−⇄LixSn (0<x<4.4) (2)
a shows the cycling performance of SnO2—SiC/G at a constant current density of 0.1 A·g−1. The initial charge (i.e., Li extraction) capacity in the potential range between 1.5 and 0.01 V obtained is 810 mAh·g−1 (based on the SnO2 mass calculated: CSnO2=[Ctotal1−0.1*Cgraphite]/0.7, assuming that graphite has a theoretical capacity [Cgraphite] of 372 mAh·g−1), which corresponds to a fully reversible alloying/dealloying reaction. A high reversible capacity of 670 mAh·g−1 can be retained over 150 cycles, which corresponds to 83% capacity retention. For comparison, the cycling performance of the n-SnO2 and m-SnO2 electrodes is provided in
The effect on the Li-storage properties of the as-prepared SnO2—SiC/G nanocomposite electrode, including the alloying and conversion reactions, can be demonstrated by the following series of electrochemical measurements performed at the wider voltage window of 3.0 to 0.01 V.
The lithium lithiation/delithiation profiles of the SnO2—SiC/G electrode at a current density of 0.1 A·g−1 in a voltage range of 3.0 to 0.01 V are shown in
d shows the cycling performance and rate capability comparison of the SnO2—SiC/G nanocomposite material and the pure SnO2 electrodes. The cells were charged and discharged between 3.0 and 0.01 V under current densities ranging from 0.1 A·g−1 to 2 A·g−1. As shown in
X-ray photoelectron spectroscopy (XPS) and TEM analyses were used to characterize the structural and morphological changes of the electrode.
The reversible conversion to SnO2 also is supported by the TEM analysis of the cycled SnO2—SiC/G sample. As shown in
In another example, a nanocomposite material was synthesized comprising silicon as the active material, B4C as the comminution material, and micro-sized graphite as the conductive material. As shown in
The Si:B4C:graphite nanocomposites were characterized by XRD (Philips X'Pert X-ray diffractometer), TEM (JEOL-2010) and BET (QUANTACHROME AUTOSORB 6-B). An electrode sheet was prepared by casting a slurry of the Si:B4C:graphite nanocomposite, conductive carbon black (SUPER P®, from TIMCAL), and carboxymethyl cellulose sodium salt (Na-CMC, Kynar HSV900,®, from Arkema Inc.) solution (2.5 wt. %) in distilled water onto copper foil. The weight ratio of Si:B4C:graphite, SP, and CMC was 70:10:20, respectively. After water was evaporated, the electrode sheet was die cut into disks with a diameter of approximately 1.27 cm and dried overnight under vacuum at 110° C.
Half cells were assembled in an argon-filled glove box using Li metal for the counter electrode, CELGARD K1640® as a polyethylene-based electrolyte separator, and 1-M LiPF6 in EC/DMC (1:2 ratio in volume) as the electrolyte with 10 wt % FEC additive. The electrochemical performance of the coin cells was measured at room temperature using an ARBIN® BT-2000 battery tester. The cells were cycled between 0.02 and 1.5 V. Cyclic voltammetry (CV) scans were conducted on a CHI 1000A® impedance analyzer at a scan rate of 0.05 mVs−1 measured between 0 and 1.5 V using a two-electrode cell configuration.
The morphology of the as-prepared intermediate and final products were studied by transmission electron microscopy (TEM).
The crystalline structures of the precursors and Si:B4C:graphite composites with different compositions were characterized by X-ray diffraction (not shown). Regarding the SBG415, SBG433 and SBG451 samples, the intensity of the graphite peaks decreases when the graphite content decreases from 50% to 10% while the peak intensity of B4C increases when the B4C content increases from 10% to 50%. The peak intensity of the silicon increases even though the silicon ratio doesn't change. The increase of the silicon peak intensity is likely due to the decreasing thickness of graphite in the series. This phenomenon also corroborates the core-shell-shell structure in which the silicon (i.e., active material) shell is mostly, if not fully, covered by the graphite (i.e., conductive material) shell. The clear and sharp silicon characteristic peaks indicate some of the silicon keeps its crystalline structure after the comminution (e.g., ball-milling) processes. The characteristic peaks for silicon become broader after ball-milling likely due to the significant particle size decrease and the silicon becoming more amorphous. However, there is no visible change for the characteristic peaks for B4C particle even though a decrease in size has been observed in the TEM images.
The long-term stabilities of SBG415, SBG433 and SBG451 under similar ball milling time (8 hours) were compared in
The first-cycle Coulombic efficiency increases in the order SBG415 (78.1%)<SBG433 (82.3%)<SBG451 (84.6%). The higher graphite content can lead to a larger surface area, which can result in more SEI film formation and a higher irreversible capacity. The BET results show the composites have surface areas that increase in the following order SBG415 (151.8 m2 g−1)>SBG433 (88.2 m2 g−1)>SBG451 (44.5 m2 g−1). Even the SBG415 still shows capacity retention of 88.0% after 75 cycles and a first-cycle efficiency of 78.1%.
b-c shows the effects of different ball-milling time on stability of SBG433 samples. The time for high energy ball-milling was varied from 4 hours, to 8 hours and to 12 hours, while the time for planetary ball-milling was fixed at 8 hours. As shown in
c shows results obtained while the high energy ball-milling time was fixed at 8 hours and the planetary ball-milling time was changed from 4 hours, to 8 hours, to 12 hours. The capacity retention after 30 cycles is 90.9% for 4-hour sample, 100% for 8-hour sample and 93.1% for 12-hour sample. The shorter planetary ball-milling appears to be too short to establish higher graphite coverage on the B4C/Si particles. Accordingly, for certain materials and in some embodiments, comminution occurs for at least 8 hours.
A SBG433 nanocomposite was prepared by 8-hour high-energy ball-milling followed by 8-hour planetary ball-milling.
While a number of embodiments of the present invention have been shown and described, it will be apparent to those skilled in the art that many changes and modifications may be made without departing from the invention in its broader aspects. The appended claims, therefore, are intended to cover all such changes and modifications as they fall within the true spirit and scope of the invention.
This invention claims priority from U.S. Provisional Patent Application No. 61/521,188, filed on Aug. 8, 2011 (Attorney Docket No 17156-E PROV), which is incorporated herein by reference.
This invention was made with Government support under Contract DE-AC0576RLO1830 awarded by the U.S. Department of Energy. The Government has certain rights in the invention.
Number | Date | Country | |
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61521188 | Aug 2011 | US |