Lithium ion batteries (LIBs) are based on intercalation reaction mechanisms. The lithium intercalation and de-intercalation may occur during discharge and charge process. For the intercalation mechanism using for example LiCoO2 or LiFePO4, there may be one (1) electron transfer occurrence per one transition metal (e.g., 3d transition metal). In other words, one electron may be transferred by one redox center.
In the present disclosure, multiple electron redox reactions may be utilized for reversible or rechargeable LIBs. In one embodiment Cu—V—O systems may allow multiple electrons to be transferred during an electrochemical process. A copper displacement reaction may allow for a transfer of two (2) electrons (e−) during an electrochemical cycle. Thus, the Cu—V—O system may deliver a higher capacity for a lithium ion battery due to its higher gravimetric capacity and energy density than other vanadium oxides (e.g., Ag—V—O). An energy density of up to 850 Wh/kg, specific capacity of up to at least 350 mAh/g and working potentials (above 2.4 V) may be achieved.
The present α-phase of Cu—V—O may have a crystal structure in space group R-3 (No. 148) and lattice parameters of a=12.8560 Å and c=7.1939 Å when x=0.1. This phase herein may be referred to as α-CVO. α-CVO has been reported to have a variable composition of Cu7−xV6O19−x where 0≤x<0.5, due to the presence of two different redox-active cations and due to the difficulty of probing oxygen vacancies using X-ray diffraction techniques.
Based on the results of structural analysis, the present α-CVO may be used as a cathode. The present cathode with α-CVO may be used in rechargeable lithium ion battery systems. The present α-CVO may have “wide” open channels for Cu-ion and Li-ion transport, where vanadium ions are clusters that are separated from each other by intervening Cu and/or Li ions. The present α-CVO may result in displacement reaction chemistry where one divalent Cu cation may be replaced by two monovalent Li cations.
The invention relates to a lithium ion battery having a cathode including an α-copper vanadium oxide with a stoichiometry of Cu7−xV6O19−X, wherein 0≤x≤0.5, and the discharge capacity is at least 250 mAh/g after 20 cycles. Preferably, the discharge capacity is at least 289 mAh/g after 20 cycles.
The battery may have an energy density of between 650 and 850 Wh/kg or an energy density of up to about 850 Wh/kg.
The copper vanadium oxide has open channels for lithium ion transfer during an electrochemical cycling process.
The invention also relates to solid state method of making a cathode material of an alpha phase of copper vanadium oxide comprising grinding a copper oxide precursor and a vanadium oxide precursor to form a powder mixture, pressing the powder mixture to form a first pellet, and heating the first (i.e., pristine) pellet under inert gas at a temperature of at least about 250° C., cooling the first pellet to room temperature, ball milling the first pellet to form a milled pellet, pressing the milled pellet to form a second (i.e., solid) pellet, heating the second pellet under inert gas at a temperature of at most about 495° C., and cooling the solid pellet to room temperature to form the cathode material. Preferably, the cathode material is composed of nanoparticles and the inert gas is argon. In one embodiment, the solid state method may further include assembling the cathode material into a coin cell. Preferably, the copper oxide precursor is Cu2O and the vanadium oxide precursor is V2O5. Most preferably, the cathode material is Cu7−xV6O19−X, wherein 0≤x≤0.5.
The invention also relates to a hydrothermal method of making a cathode material of an alpha phase of copper vanadium oxide comprising preparing an aqueous solution of a copper oxide precursor and a vanadium oxide precursor, subjecting the aqueous solution to ultrasound, and heating the aqueous solution at a temperature of at most about 180° C., then filtering off the cathode material. Preferably, the cathode material is a solid. The hydrothermal method may further include (1) washing the cathode material with a solvent mixture; (2) washing the cathode material with a solvent mixture and drying the cathode material under vacuum; or (3) washing the cathode material with a solvent mixture, drying the cathode material, and ball milling the cathode material. The method may also further include assembling the cathode material into a coin cell.
The present α-phase of Cu—V—O may have a crystal structure in space group R-3 (No. 148) and lattice parameters of a=12.8560 Å and c=7.1939 Å when x=0.1. The present α-CVO may be used as a cathode material and may have a stoichiometry of about Cu6.90V6O19, i.e. Cu7−xV6O19−X, wherein 0≤x≤0.5. Both Cu and V may access multiple valence states during cycling, 2+ and 1+ and 0+ for Cu and 5+ and 4+ for V. The α-CVO structure may have a cluster structure that allows it to exchange ions (such as Li) during electrochemical cycling without irreversibly destroying its framework. The specific gravimetric capacity of α-CVO may be 350 mAh/g, giving a theoretical energy density of approximately 350 mAh/g·2.6=910 Wh/kg (based on displacement reaction), and even higher theoretical values of 549 mAh/g or 549 mAh/g·2.6=1400 Wh/kg (based on combined displacement and intercalation reaction mechanism), which may be 2-4 times higher than the prior art cathodes (such as LiCoO2˜140 mAh/g, or LiFePO4˜169 mAh/g).
In an embodiment an energy density of the present cathode material may be up to 850 Wh/kg, a specific capacity and may be of up to at least 350 mAh/g with working potentials (above 2.4V). The present methods may be utilized to prepare cathodes of copper vanadium oxide (α-CVO) by either (1) a solid state reaction process, or (2) a hydrothermal method. Copper vanadium oxide (α-CVO) may be used as a rechargeable cathode in lithium ion batteries. These cathodes therefore may not be used only in primary batteries.
With the present α-CVO, high capacity (high capacity meaning for example multiple-electron transfers per formula) and 3D lithium diffusion channels may lead to an improvement in rate capacity. Two (2) electrons may be transferred from the Cu displacement reaction (electrochemical window 2.0 V to 3.6 V) and one (1) more electron may be contributed from vanadium in an enlarged electrochemical window of 1.0 V to 4.5 V. The vanadium redox reaction may occur if the discharge voltage is lowered down to 1.0 V. Vanadium is also an active element which may contribute to electrochemical performance. Below 2.0 V, vanadium may be reduced from +4 to +3 as may be shown by an in-situ XAS test. In the higher voltage region, for example above 3.6 V, the valence of vanadium may change from +4 to +5, where the valence change in the high voltage window may be deduced from the electrochemical curve.
The present α-CVO may have “wide” open channels for Cu-ion and Li-ion transport, where vanadium ions are clusters that are separated from each other by intervening Cu and/or Li ions, which facilitates fast ionic transport in the ceramic matrix during electrochemical cycling. Because of the open channels, the α-CVO exhibit high rate capability (or high power density): for example, 92% of the maximum specific discharge capacity was retained with a doubling of the current density (from C/35 to C/17.5), and about ⅔ was still accessible even at high rate of C/1.75, corresponding to 220 mAh/g.
The batteries with the present α-CVO may have a discharge capacity of at least 250 mAh/g after 20 cycles. The batteries may have a discharge capacity of at least 289 mAh/g after 20 cycles.
In an embodiment, the present α-CVO may be prepared by a solid-state reaction route. With the present solid state synthesis, α-CVO may be produced at low temperatures (e.g., 495° C. or lower) providing a lower cost method of synthesis compared to traditional methods which require high heat followed by extensive cooling steps. The solid state synthesized α-CVO materials may be a powder. The solid state synthesis may be carried out with precursors of Cu2O and V2O5. The precursors may be ground by mechanical ball milling for a first round. The ground precursors may be collected from the ball mill for further processing. The conditions for the mechanical ball milling may be determined by a skilled practitioner. For example, the precursors may be subject to ball milling for about 20 minutes, 30 minutes, or 40 minutes at a rotational speed of about 250 rpm, 300 rpm, or 350 rpm. The ground precursors may form a powder mixture. The powder mixture may be mechanically pressed for a first round into a first solid pellet. For example, the pressed first pellet may be heated under inert gas at a temperature of at least about 250° C. for about 6 hours, 8 hours, or 10 hours, and then cooled down to room temperature. The solid state synthesized first powder or pellet may be micron-sized particles. The first pellet or powder may be pristine α-CVO. For example, after pre-heating at 250° C. (or higher), α-CVO may be formed and there may be precursor residue. A post-processing procedure for particle size reduction of the pristine α-CVO may be employed.
In one example, a second round of grinding of the first pellet or powder may be carried out for about 10 minutes, 20 minutes, 30 minutes, or 40 minutes followed by a second round of mechanically pressing into a second solid pellet. The second pellet may be heated under inert gas to a temperature of at most about 495° C. for about 6 hours, 8 hours, or 10 hours and then cooled down to room temperature. Finally, the cooled second pellet may be subjected to a third round of ball milling for about 2 hours. The second pellet may be assembled into a coin cell.
The purpose of grinding, pressing, and heating the mixture multiple times is to ensure that the mixture becomes as homogeneous as possible. The components tend to segregate during heating and require more than one round involving grinding, pressing, and heating. Preferably, two or three rounds may be required to ensure the cathode material is uniform. Furthermore, after the first round of grinding, the particles may be micro-sized. After the second round of ball milling, the particles may be nano-sized.
In general, mechanical ball milling may be used on the solid state synthesized powder. The ball milling time may be in intervals of about 2 hours, with crystallinity maintained and a particle size of a few hundred nm.
The present α-CVO cathode may involve the displacement of Cu2+ and Cu+ ions from the α-CVO structure that may lead to the formation of Cu metal. The reversible capacity (350 mAh/g (twice of prior art cathodes) in the window of 2.0-3.6V and >500 mAh/g in the window of 1.0-4.5V, may be found with present α-CVO cathodes. This performance may be due to an open framework that may accommodate multiple electron redox reactions.
For the pristine α-CVO as prepared by solid-state reaction, its 1st discharge capacity is 82 mAh/g while it delivers 200 mAh/g at its 10th cycle (
For α-CVO after 12 hours ball milling, its 1st discharge capacity is 241 mAh/g while it delivers 202 mAh/g at its 20th cycle (
The discharge capacity of α-CVO after two hours of ball milling is 342 mAh/g, 352 mAh/g and 321 mAh/g in its 1st, 2nd and 10th cycle respectively (
The particle size of α-CVO (inset of
The α-CVO after two (2) hours of ball milling exhibits long cycling stability and high Coulombic efficiency (
In an embodiment, the present alpha copper vanadium oxide may be synthesized by hydrothermal reaction method which may be carried out at a low temperature (e.g., 180° C. or below or at most 180° C.), and may be solution based, energy efficient and low in cost. The hydrothermal synthesis may be characterized by the following reaction.
Cu(NO)3.2H2O+NH4VO3→α-CVO (1)
Cu(NO)3.2H2O+NH4VO3 may be dissolved into distilled water, with 0.2204 g Cu(NO)3.2H2O and 0.1538 g NH4VO3 in 96 ml, and subjected to ultrasound for 30 minutes. The mixture (solution) may be transferred into a Teflon vessel and sealed into autoclaves. The autoclave (containing the mixture) may be placed into an oven and heated to a temperature of at most 180° C. for about 48 hours. A solid cathode material product may be filtered after the autoclaving and cooled down. The cathode material may be washed. The cathode material may be washed with a solvent followed by water. The solvent may be ethanol or acetone. The cathode material may be washed with ethanol, followed by distilled water and then acetone. After washing, the cathode material may be dried using a vacuum oven. Next, the cathode material may be manually ground or milled. The cathode material may be assembled into a coin cell.
The α-CVO synthesized by hydrothermal reaction method may exhibit around 260 mAh/g capacity (
To achieve the present cathode material, crystal structure information may be analyzed based on a crystal structure database, such as the Inorganic Crystal Structure Database (ISCD): https://icsd.fiz-karlsruhe.de. A structure may be selected which has open channels for lithium ion. A connected and flexible structure may be desired to support the reversibility during the cycles. Material having an isolated or firm framework may be deselected as a candidate for the present cathode material.
One may vary the synthesis to increase yield and shape control in hydrothermal synthesis (as demonstrated in
Ex-situ XRD studies (
In-situ XRD studies (
A combination of a LeBail fit for the α-CVO with a Rietveld fit of the Cu phase was used to quantitatively track the change in lattice parameters of the α-CVO phase during discharge process. Based on the fitting result, the unit cell volume of α-CVO increases during the discharge process. One copper atom extrudes from the matrix and leaves one site vacancy for one inserted lithium ion. This may be facilitated by the similar size of the copper and the lithium ions. The ionic radii of Cu2+, Cu+ and Li+ are 0.73 nm, 0.77 nm and 0.76 nm respectively. Because the radius of lithium ion is a little larger than Cu2+, the unit cell volume may increase gradually while a first lithium ion may occupy spare space in the crystal lattice. Due to the limited open space in one unit cell, the unit cell may expand to accommodate the squeezed second lithium ion during the discharge process. This step shows low kinetics due to the large polarization shown in GITT data. (
Additionally, the copper (111) peak area increases during its 1st discharge process. The amount of inserted lithium ions in the matrix is plotted as a function of the amount of copper atoms extruded from the matrix in
For in-situ XAS data shown in
As previously stated, in prior studies of the α-CVO compound, vanadium may go through a reduction reaction during the discharge step. As a result, the vanadium may go through a change in its coordination environment. The stability of the structure may be hard to maintain if the vanadium oxide coordination polyhedron changes. However, in the present compound, the stability of the VO polyhedron may be preserved by the unchanging valence of vanadium during the discharge step if testing electrochemical window is from 2.0 V to 3.6 V. The V—O octahedral clusters may maintain a framework for α-CVO in this electrochemical potential window which may be beneficial to structure reversibility during electrochemical cycling. Although these clusters are not linked to each other through chemical bonds, they may still create a structural scaffold that may maintain structure reversibility during the electrochemical reaction. The mobility of clusters may be less than a single VO6 octahedron due to their heavier mass.
The reaction mechanism of α-CVO during its 1st discharge process is studied by combination analysis of GITT data, in-situ XRD and in-situ XAS characterization. The mechanisms of the lithium reaction are identified in four (4) regions of α-CVO during the 1st discharge. The first region is from OCV to discharge at 2.58V, where a line with a steep slope is observed. According to the GITT data (
The majority of the capacity may occur in Region II (2.58-2.32V) during which lithium ions may insert into the structure accompanied by Cu extrusion due to the displacement of Cu2+ in a 2-electron process. For Region II, a plateau which may contribute large capacity may be observed. This may be a Cu2+ displacement reaction mechanism. (
A modest additional capacity may be found in Region III (2.32-2.0 V), during which Cu+ displacement chemistry may continue to occur but for which Li+ may be forced to insert into substantially less favorable interstitial sites. Further discharge may occur to 2.0V, after a majority of Cu2+ takes part previously in the reaction. Some Cu ions may go through the electrochemical reaction and contribute to capacity. The valence of copper may shift to a low value while the valence of vanadium may remain the same in the second and third regions (
Region III processes may or may not be complete before V4+ reduction begins to occur at very low voltages (2.0-1.0V). The chemical reaction schemes associated with these regions can be summarized as:
Cu6.9V6O18.9+xLi++xe−→LixCu6.9V6O18.9(0<x<0.1) (I)
LixCu6.9V6O18.9+yLi++ye−→Lix+yCu6.9−0.5·yV6O18.9+0.5yCu(x>0.1;0<y<13.8) (II)
LixCu6.9V6O18.9+zLi++ze−→Lix+y+zCu6.9−0.5·yV6O18.9+Cu(x>0.1;0<y<13.8;0<z<6) (III)
A specific capacity of 350 mAh/g can be achieved for α-CVO cathodes at an average discharge voltage of 2.42V, resulting in an overall energy density of 847 Wh/kg. This energy density is believed to be more than what would be delivered by a 4V cathode with a 200 mAh/g specific capacity. As such, it may exceed that of commercial intercalation cathode materials such as LiCoO2 and LiFePO4, and may be comparable to the performance being targeted in other Li-ion intercalation systems (such as for example, Li-excess layered compounds and high-voltage spinels). In situ measurements demonstrate that this capacity may be associated with Cu2+ displacement chemistry, though intercalation processes associated with the Cu2+/Cu+ redox couple occur at voltages above 2.6V and some intercalation associated with V4+/V3+ may occur at voltages below about 2.0V. In contrast to other systems that operate through similar displacement mechanisms, the displacement chemistry of the α-CVO phase is more reversible (with a low capacity fade over multiple charge/discharge cycles) and is compatible with relatively higher discharge rates. This enhanced reversibility may in part be attributed to the structural building blocks of isolated V6O18 clusters, which may enable the structural flexibility to accommodate the intercalation of excess Li ions utilizing atomic sites beyond those already occupied by mobile ions in the pristine compound.
Transmission X-ray microscopy (TXM) is a non-destructive and chemical sensitive method which enables the study of correlation between the morphology and chemical phase mapping with sub-30 nm spatial resolution. First discharge and charge curves of α-CVO electrodes that were used for TXM and data schematic are shown in
According to the fitting map result, an extruded copper map presents a homogenous dispersion, which indicates that the extruded copper did not agglomerate into big particles accumulated in a certain area. After the charge process, copper metal would insert into α-CVO matrix reversely, as shown in FIGS. (10(a)-(c). Small particle size and homogenous copper dispersion is supportive for copper insertion back, which contributes to improved cycling reversibility.
A stoichiometric amount of Cu2O and V2O5 as precursors are mixed and milled for 30 minutes in a planetary ball mill device (Gilson, model LC-106A) with a rotational speed of 300 rpm. Then, the mixture is pressed into a pellet and sintered by heating at 250° C. for several hours under inert atmosphere. Precursors are cooled to room temperature. Then they are ground 30 minutes and heated a second time at a higher temperature of 495° C. under inert atmosphere for several hours. Precursors are cooled to room temperature. Procedures are carried out in ambient atmosphere and the raw materials are analytical reagents used without any further purification or treatment.
Powder X-ray diffraction data were collected at room temperature with a Bruker D8 Advance diffractometer with Bragg-Brentano geometry using copper Kα as a radiation source (Kα1=1.54053 Å, Kα2=1.54431 Å). It was equipped with a 1D position sensitive Lynx-Eye liner strip detector with 192 channels and 300 mm was used as the primary radius and secondary radius. Zero background silicon slides were used as sample holders. Routine pattern indexing and phase identification was done by using JADE software package. TOPAS software package (Bruker AXS, version 4.2) was used for Le Bail fitting and Rietveld refinement.
Synchrotron X-ray diffraction data for α-CVO samples were collected at beam line X14A at the National Synchrotron Light Source (NSLS), Brookhaven National Laboratory (BNL). The wavelength used in X14A was approximately 0.7783 A. It was equipped with a 1D linear position sensitive silicon strip detector with 640 channels. Data were collected over the 20 degree range of 4-54° (pristine powder) or 4-40° (in-situ and ex-situ electrode) with a counting time of 15 seconds per step.
Ex-situ electrode XRD (
Compared to the ex-situ technique, in-situ analysis method may maintain the real reaction environment inside the coin cell. It may provide more accurate information to track the crystal structure change and phase transition during electrochemical processing, and may be a powerful technique to study the cathode reaction behavior in real time. For the in-situ coin cell test, a LaB6 calibration may be performed before running the experiment in order to determine the angle position. A pristine spectrum may be collected at room temperature before current is applied to the coin cell. Synchrotron X-ray diffraction data for as-synthesized α-CVO may be collected at room temperature.
X-ray absorption spectroscopy (XAS) data for copper and vanadium at their own K-edge are collected at beam line X18A of National Synchrotron Light Source (NSLS), Brookhaven National Laboratory (BNL).
In-situ electrode XAS data were collected to get the copper and vanadium valence information at specific discharge or charge stages. The XAS data were collected at room temperature by using a Si (111) double crystal monochromator in a transmission mode with an operating voltage set at 2.8 GeV and a typical current of 300 mA. Harmonics were rejected by detuning. Copper or vanadium foil was used simultaneously as references for energy calibration. X-ray absorption near edge structure (XANES) spectra were taken every 0.5 eV up to 50 eV after the edge with an integration time of 2 s. Based on the experimental setup, a 1 mm slit size was used and the beam experimental resolution was 1.7 eV. Synchrotron X-ray absorption data for as-synthesized α-CVO were collected at room temperature. X-ray absorption near edge structure (XANES) data were processed using the ATHENA software package.
To evaluate electrochemical performance, composite electrodes were constructed by mixing the active materials, super P and Polyvinylidene difluoride (PVDF) in the weight ratio of 70:20:10. Proper amounts of 1-methyl-2-pyrrolidinone (NMP) were added into the mixture and a slurry was formed. Then the slurry was coated on the aluminum foil with the thickness of 25 μm. The diameter of the punched cathode was 10 mm. Typical loading of the active material was 2-3 mg. The cathode was dried under vacuum at 100° C. for several hours. The test cell was assembled in an argon filled glove box with lithium metal as an anode, a Celgard 2300 sheet as separator and 1 M LiPF6 in a mixed ethylene carbonate (EC)/dimethyl carbonate (DMC) (1:1 in volume) solution as an electrolyte. The charge-discharge measurements were carried out in a potential range from 2V to 3.6V (vs. Li+/Li) using an Arbin Cycler. 2025 coin cells were assembled, cycled and tested at room temperature.
Structure information of the present solid state synthesized α-CuVO is solved by Rietveld Refinement result based on synchrotron powder XRD data (
Morphological information was collected using a Hitachi 4800 scanning electron microscope with an operating voltage of 5 kV and working distance of 2.5 mm in under vacuum to minimize charging effects. SEM image and energy-dispersive X-ray spectroscopy (EDX) information were obtained by using JEOL 7600F with an operating voltage 10 kV and working distance of 7.5 mm. Powder samples were mounted on a circular aluminum standard plate sample holder using double sided carbon conductive tape.
The transmission X-ray microscopy method was used to collect sample morphology information and XAS data at beam line X8C, National Synchrotron Light Source (NSLS), Brookhaven National Laboratory. A field view of 40×40 m with a 2048×2048 CCD camera was used. To study the chemical state evolution, X-ray Absorption Near Edge Structure (XANES) image series was measured by scanning Cu absorption K-edge from 8960 to 9040 eV, with a 2 eV step size, and one TXM image at one energy step, which generated 1 k×1 k XANES spectra with 2×2 binned pixels. Each image was collected with 10 s exposure time. 2×2 camera pixels were binned into one output image pixel. The chemical phase maps (fitting) were obtained by using the customized program (MatLab, Mathworks, R201 b) developed by X8C beamline at NSLS.
The present application claims the benefit of U.S. Provisional Application Ser. No. 62/405,664, filed on Oct. 7, 2016, the contents of which are hereby incorporated by reference in its entirety.
The present invention was made with government support under contract numbers DE-AC02-98CH10886 and DE-SC0012704 awarded by the U.S. Department of Energy. The United States government may have certain rights in this invention.
Number | Date | Country | |
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62405664 | Oct 2016 | US |