CA3137220A1 - Metal oxide-based electrode compositions - Google Patents

Abstract

The invention provides a method of charging and/or discharging an electrochemical cell at a high rate, wherein the electrochemical cell has a working electrode comprising a niobium tungsten oxide and/or a niobium molybdenum oxide. The invention also provides an electrode comprising a niobium tungsten oxide wherein, the ratio of Nb2O5 to WO3 is from 8:5 to 11:20, and an electrode comprising niobium molybdenum oxide, wherein the ratio of Nb2O5 to MoO3 is from 6:1 to 1:3.

Description

METAL OXIDE-BASED ELECTRODE COMPOSITIONS
Related Application This present case is related to, and claims the benefit of, GB 1809467.2 filed on 08 June 2018 (08.06.2018) and GB 1905218.2 filed on 12 April 2019 (12.04.2019), the contents of which are hereby incorporated by reference in their entirety.
Field of the Invention The present invention provides an electrode and an electrochemical cell, such as a lithium ion battery, comprising the electrode, together with methods for using the electrode within the electrochemical cell.
Background High-rate lithium ion battery electrode materials can store large quantities of charge in a few minutes of charging, rather than hours. Such materials are required to alleviate the technological challenges associated with the adoption of electric vehicles and grid-scale batteries, and to enable new power-intensive devices.
The most intuitive and commonly used approach to increase the rate performance of an electrode material is to create a nanosized or porous (and often hierarchical) structure. This minimizes the lithium ion solid-state diffusion distance, enabling more rapid lithium ion transport through the electrode and increasing the surface area of electrode materials in contact with electrolyte. Carbonaceous hierarchical structures and carbon-coating are also frequently employed to improve electronic conductivity, which is another prerequisite for high-rate applications.
In practice, despite excellent lithium ion mobility, graphite cannot be used at high-rates due to particle fracture and the risk that lithium dendrites form, leading to short circuits and the risk of fires and explosions (Zhao, etal.; Downie, etal.). The latter issue inherently limits the use of low voltage anodes in high-rate applications, since the electrode inhomogeneity, or any source of increased overpotential, can lead to lithium plating potentials on the surface of the low-voltage electrode (Downie, etal.).
Li4Ti5012 (lithium titanate; LTO), with an average voltage of 1.55 V against Li/Li, enables high-rate (de)intercalation without the risk of lithium dendrites or substantial solid¨electrolyte interphase (SEI) formation, albeit with an undesirable but necessary decrease in full-cell voltage and thus energy density. However, even in this well-established "high-rate" anode, the capacity of 1 pm particles from solid-state synthesis reaches only 60-65 mA=h=g-lat a rate of 10C (Kim, etal.).

2 A number of strategies have been proposed to increase the capacity of LTO
electrodes at high C-rates, and present carbon-coated nanoparticles of LTO can reach at least 150 mA=h=g-1 at 10C (Wang etal.; Odziomek, etal.). This corresponds to approximately 0.5 lithium ions per transition metal (Li/TM).
However, using nanostructured and porous materials for electrochemical energy storage applications inherently results in a severe penalty in terms of volumetric energy density.
Furthermore, these carefully designed porous and nanoarchitectures are time consuming and expensive to synthesize, characterize, and manufacture. Synthesis methods often result in relatively low yields and/or large quantities of chemical waste generation (Oszajca, etal.). Moreover, these porous and nanoarchitectures are also susceptible to degradation during electrochemical cycling from processes such as catalytic decomposition of electrolyte (Palacin etal.), morphological changes that result in loss of nanostructuring (Wu etal.), and higher first cycle capacity loss (Kasnatscheew etal.).
Another problem with the use of nano-LTO electrodes in a full cell is gas evolution during repeated charging and discharging cycles, and the associated swelling or pressure build-up.
This arises from heterogeneous catalysis between the metal oxide surface and organic electrolyte (He et al.; Lv, etal.). The small particle sizes required to compensate for poor lithium ion and electron diffusion in LTO increase the reactive surface area, exacerbating this problem.
Fast charging or high-power delivery from a full cell also requires a cathode to match the anode. LiFePat has been used as a promising high-rate cathode (Zaghib, etal.).
However, both LiFePat and LTO have exceptionally flat voltage profiles. This combination provides a constant voltage but presents a serious challenge in terms of battery management systems (BMS). Simple and accurate BMS is a crucial factor for battery applications in electric vehicles and mobile technology and is even more important at high-rates to prevent dangerous and degradative over(dis)charging while maximizing utility. BMS rely on the ability to measure state-of-charge, which cannot be done simply by charge counting alone as the battery degrades and electron-consuming side reaction occur.
In light of the above challenges, there is a need to provide new electrode materials for lithium ion batteries that are capable of operating at high rates.
Summary of the Invention The invention generally provides an electrode comprising niobium tungsten oxide, an electrochemical cell comprising the electrode, and the use of the cell, for example, in a lithium ion battery, at high C-rates of 5C or more, such as 10C or more, during charging and/or discharging.

3 The present inventors have established that extremely high volumetric energy densities and impressive charging and discharging rates can be achieved using electrode materials comprising niobium tungsten oxides in a high-rate lithium ion cell. The niobium tungsten oxides have favorable lithium diffusion properties, and thus exhibit superior performance.
Above 1.0 V vs. LOLL the formation of SEI is minimal, which means that lithium will not be lost into side reactions with the electrolyte.
In addition, a high-rate lithium ion cell using electrode materials comprising niobium tungsten oxide can operate above 1.3 V. (For example, the average voltage of Nb16W5055 is 1.57 V
vs Li/Li and the average voltage of Nb18W16093 is 1.67 V vs LOU). Operating in this voltage range negates the need to perform an initial formation cycle, simplifying the cell manufacturing process. A typical lithium-ion cell comprising a graphite electrode operates below 1.3 V and must undergo an initial formation cycle before the cell is sealed. Typically, this formation cycle takes place at elevated temperature, for example 60 C, in order to allow degassing to occur. This adds signification time and cost to the cell manufacturing process.
Furthermore, in a full cell against e.g. LiFePat, LiN(CF3S02)2 (LiTFSI) can be used to replace the more toxic LiPF6 electrolyte salt commonly used in standard commercial electrolytes. Moreover, aluminum can be used as the current collector instead of the more expensive copper while avoiding LiAl alloying potentials (0.3 V vs. LOU).
The use of a niobium tungsten oxide as an electrode material, for example in a high-rate lithium cell, allows the open-circuit voltage to be used as a measure of state-of-charge. This has the potential to provide a simple and reliable BMS, which may prove to be a significant advantage for high power/fast charging applications.
In a first aspect of the invention there is provided a method of charging and/or discharging an electrochemical cell at a C-rate of at least 5C, such as at least 10C, wherein the electrochemical cell has a working electrode comprising niobium tungsten oxide.
The electrochemical cell may contain a counter electrode and an electrolyte, and optionally the electrodes are connectable to or are in connection with a power supply.
The method may be a method of charging and/or discharging an electrochemical cell at a current density of at least 750 mkg-1, such as at least 800 mkg-1.
The method may involve a cycle of charging and discharging or discharging and charging the electrochemical cell, and the method may comprise 2 cycles or more, 5 cycles or more, 10 cycles or more, 50 cycles or more, 100 cycles or more, 500 cycles or more, 1,000 cycles or more, or 2,000 cycles or more.

4 In one embodiment, the working electrode does not have a porous nor hierarchical structure.
The working electrode may comprise the niobium tungsten oxide in particulate form. For example, the niobium tungsten oxide may have a primary particle size of at least 1 pm.
The smaller surface area of the particulate niobium tungsten oxides decreases side reactions and mitigates the problems of gas evolution and the associated swelling or pressure build-up observed with nano-LTO electrodes. Moreover, particulate niobium tungsten oxides can be quickly and easily prepared using solid state synthesis.
The working electrode may have a solid-state lithium diffusion coefficient (Du) of less than 10-14 m2.s-1 at 298 K, such as less than 10-15 m2.s-1 at 298 K.
The favorable lithium diffusion properties allow micrometer-sized particles of niobium tungsten oxide to be used at extremely high rates.
The working electrode may have a capacity of 50 mA=h=g-1 at 200. For example, 75 mA=h=g-1 at 200 or 50 mA=h=g-1 at 600.
The molar ratio of Nb2O5 to W03 in the working electrode may be from 6:1 to 1:15. For example, from 8:5 to 11:20.
The working electrode may comprise a niobium tungsten oxide selected from the group consisting of Nb12W033, Nb26W4077, Nb14W3044, Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093, Nb22W200115, Nb8W9047, Nb54W820381, Nb20W310143, Nb4W7031, or Nb2W15050.
For example, Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093 or Nb22W200115.
Additionally, the working electrode may comprise a mixture of niobium tungsten oxide and an additional active material. For example, the working electrode may comprise a mixture of niobium tungsten oxide and LTO. The ratio of niobium tungsten oxide to LTO may be from 95:5 to 5:95 by weight. For example, the ratio may be from 90:10 to 10:90 by weight, from 80:20 to 20:80 by weight, from 70:30 to 30:70 by weight, from 60:40 to 40:60 by weight or the ratio of niobium tungsten oxide to LTO may be 1:1 by weight.
In a further aspect of the invention, there is provided an electrode, which may be referred to as a working electrode, comprising a niobium tungsten oxide, such as wherein the molar ratio of Nb2O5 to W03 in the electrode is from 8:5 to 11:20. The working electrode is suitable for use in a lithium ion battery.
The working electrode may comprise a niobium tungsten oxide selected from Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093 or Nb22W200115. For example Nb16W5055 or Nb18W16093.

In one embodiment, the working electrode does not have a porous nor hierarchical structure.
The working electrode may comprise a niobium tungsten oxide in particulate form. For example, the niobium tungsten oxide may have a primary particle size of at least 1 pm.

5 Additionally, the working electrode may comprise a mixture of niobium tungsten oxide and an additional active material. For example, the working electrode may comprise a mixture of niobium tungsten oxide and LTO. The ratio of niobium tungsten oxide to LTO may be from 95:5 to 5:95 by weight. For example, the ratio may be from 90:10 to 10:90 by weight, from 80:20 to 20:80 by weight, from 70:30 to 30:70 by weight, from 60:40 to 40:60 by weight or the ratio of niobium tungsten oxide to LTO may be 1:1 by weight.
In a further aspect of the invention, there is provided an electrochemical cell comprising the working electrode of the invention.
In a further aspect of the invention, there is provided a lithium ion battery comprising one or more electrochemical cells of the invention. Where there are a plurality of cells, these may be provided in series or parallel.
In a further aspect of the invention there is provided the use of a working electrode comprising a niobium tungsten oxide in a high-rate electrochemical cell, for example wherein the cell is operated at a C-rate of at least 5C, such as at least 10C.
In a further aspect of the invention there is provided a method of charging and/or discharging an electrochemical cell at a C-rate of at least 5C, such as at least 10C, wherein the electrochemical cell has a working electrode comprising niobium molybdenum oxide.
The present inventors have found that high energy densities and impressive rates can be achieved using electrode materials comprising niobium molybdenum oxides in a high rate lithium ion battery. The niobium molybdenum oxides display a higher average voltage in comparison to common high-rate anode materials, and so reaction with the electrolyte is avoided or minimized.
In a further aspect of the invention, there is provided an electrode, which may be referred to as a working electrode, comprising a niobium molybdenum oxide, such as wherein the molar ratio of Nb2O5 to Mo03 in the electrode is from 6:1 to 1:3, for example 1:3.
The working electrode is suitable for use in a lithium ion battery.
The working electrode may comprise a niobium molybdenum oxide selected from Nb2Mo3014, Nb14Mo3044 or Nb12Mo044. For example Nb2Mo3014.

6 These and other aspects and embodiments of the invention are described in more detail below.
Summary of the Figures Figure 1 is a wide-field SEM image of (A) Nb16W5055 and (B) Nb18W16093 at a low magnification to show the roughly uniform particle size and presence of agglomerates. The background of (A) is a Cu grid and of (B) is adhesive carbon. The scale bars are 50 pm in both images.
Figure 2 is an atomic structure and SEM image showing (A¨C) Nb16W5055 and (D¨F) Nb18W16093. The scale bars shown in (B) and (E) are 5 pm. The scale bars shown in (C) and (F) are 10 pm.
Figure 3 is a diagram showing the bronze-like structure of Nb18W16093 and its relationship to the classic tetragonal tungsten bronze (TTB). Partially filled spheres represent K+ ions, which are not present in Nb18W16093 Figure 4 is a diagram showing the rate performance of bulk Nb16W5055 and Nb18W16093. (A) galvanostatic discharge and charge curves for Nb16W5055 from 60C (leftmost curve at 1.0 V
and 3.0 V) to 0.2C (rightmost curve at 1.0 V and 3.0 V); (B) dQ/dV plot for Nb16W5055 from 0.2C (leftmost curve at 50 mA=h=g-1) to 60C (rightmost curve at 50 mA=h=g-1);
(C) galvanostatic discharge and charge curves for Nb18W16093 from 100C (leftmost curve at 1.0 V and 3.0 V) to 0.2C (rightmost curve at 1.0 V and 3.0 V); (D) dQ/dV plot for Nb18W16093 from 0.2C (leftmost curve at 50 mA=h=g-1) to 100C (rightmost curve at 50 mA=h=g-1); (E) a summary of the rate performance and (F) high-rate cycling of 250 cycles at 10C
followed by 750 cycles at 20C.
Figure 5 shows voltage profiles of Li4Ti5012 (curves with plateau at 1.55 V), Nb16W5055 (curves crossing at 1.57 V) and Nb18W16093 (curves crossing at 1.65V).
Discharge and charge voltage profiles normalized to (A) gravimetric capacity and (B) lithium ions transferred per transition metal atom. The average voltage of Li4Ti5012, Nb16W5055, and Nb18W16093 is 1.55 V, 1.57 V, and 1.65 V, respectively. The Li4Ti5012 electrochemistry shown here (extracted with WebPlotDigitizer 2017, Ankit Rohatgi) represents an optimal performance, consisting of 5-20 nm particles on 15-20 nm carbon nanofibers (CNF) with a mass loading of 1 mg=cm-2.
Figure 6 is a comparison of Cu foil to carbon-coated Al foil current collector. Fig. 6A shows Nb16W5055 cycled for 1000 cycles under constant current discharge and charge at 10C (first 200 cycles) and 20C (last 800 cycles); Cu foil at 1.0 V (topmost line); Cu foil at 1.2 V (second from top); C-Al at 1.0 V (third from top) and C-Al at 1.2V (bottommost line).
Fig. 6B shows discharge and charge profiles between 3.0 and 1.0 V for the 100th cycle at 10C; order of

7 curves at 100 mA=h=g-1: C-Al charging curve (topmost); Cu foil charging curve (second from top); Cu foil discharging curve (third from top) and C-Al discharging curve (bottommost).
Figure 7 shows longer term cycling as a function of minimum cutoff voltage.
(A) Nip%WsOss cycled at C/5 (fist 50 cycles) and 1C (second 50 cycles) on Cu foil with a 1 h potentiostatic hold at the top of charge; Vi-nin = 1.2 V (topmost curve); Vi-nin = 1.0 V
(bottommost curve). (B) Nip%WsOss cycled at C/5 on Al foil without a potentiostatic charging step.
Figure 8 shows overpotential in a Li II Li symmetric cell as a function of current density.
Figure 9 shows the stimulated echo pulsed field gradient sequence used to measure 7Li diffusivities showing both radiofrequency (7Li) and magnetic field gradient (Gz) pulses. Here, gradient pulse duration (tg) includes the up ramp, time on, and down ramp of the opt composite gradient pulses.
Figure 10 shows representative 7Li decay curves showing normalized NMR signal intensity as a function of gradient strength for (A) Lilo 2NbisWis0s3 at 453 K, (B) Lis sNbisWis0s3 at 453 K, (C) Li34Nb18W16093 at 453 K, (D) Lis 3NbisWsOss at 353 K, and (E) Li84Nb16W5O55 at 383 K. Black circles represent experimental data points and red lines represent (A¨C; E) mono- or (D) biexponential fits of the data to the Stejskal¨Tanner equation.
Figure 11 shows lithium diffusion measured via 7Li pulsed field gradient nuclear magnetic resonance (PFG NMR) spectroscopy. The lithium diffusion coefficients of Lis 3NbisWsOss and LixNb18W16093 (x = 3.4, 6.8, 10.2) were measured in the temperature range 333-453 K.
The filled (85% signal contribution) and empty (15% signal contribution) symbols for Lis 3NbisWsOss correspond to the observed two-component diffusion.
Figure 12 shows (A) relative changes in lithium diffusion as a function of open-circuit voltage (Voc) and (B) open-circuit voltage vs. closed-circuit voltage (Vcc) from galvanostatic intermittent titration technique (GITT) measurements showing the "thermodynamic"
electrochemical profiles at C/20 rate with a 12 h rest period at each point, reaching a full discharge in approximately one month.
Figure 13 shows (A) Nip%WsOss and Nb18W16093 from this work as compared to high-rate electrode formulations from the literature. Volumetric capacities at 1C and 20C are determined from reported capacities and reported, measured, or estimated tap densities.
(B) Ragone (log¨log) plot of energy density and power density on the basis of anode active materials vs. a 4.0 V cathode. The mass loading of the niobium tungsten oxides here was 2.6 mg=cm-2, the mass loading of the other titanium and niobium-based materials was typically ca. 1 mg=cm-2. Graphite is included as a reference, though it cannot be used for high-rate applications due to lithium plating risks and particle fracture.
Literature values for the Ragone plot were extracted with WebPlotDigitizer.

8 Figure 14 shows theoretical volumetric capacity assuming a reaction of one electron per transition metal and crystallographic (single crystal) densities. The capacity for Li4-1,5012 is shown for the well-established reaction to Li7Ti5012; the capacity of graphite is based on the reaction of one electron per 06 unit.
Figure 15 shows the capacity versus cycle number for Nb2Mo3014 at 0.050 and from 1.0 to 3.0 V vs. LOLL
Figure 16 shows discharge and charge voltage profiles of Nb2Mo3014 within three different voltage windows (1.0 V, 1.2 V and 1.4 V). The discharge and charge curves are normalized to gravimetric capacity; order of curves at 200 mA=h=g-1: 1.4 V charging curve (topmost);
1.2 V charging curve (second from top); 1.0 V charging curve (third from top);
1.2 V
discharging curve (third from bottom); 1.0 V discharging curve and 1.4 V
discharging curve (overlapping; bottommost).
Figure 17 shows discharge and charge voltage profiles of (A) NM0622 (LiNio60002Mno 202), (B) LiFePat and (C) LiMn2O4against Li/Li.
Figure 18 compares capacity at varying charge and discharge rates for electrodes comprising Nb16W5055 and different separators, binders, binder quantity, conductive carbon type and with calendaring of the electrode.
Figure 19 shows discharge and charge voltage profiles of full cells comprising a Nb16W5055 anode and (A) LiFePat, (B) LiMn204, and (C) NM0622 cathode. Figure 19(D-E) shows the rate performance of a cell comprising a Nb16W5055 anode and NM0622 cathode;
order of cures in (E): capacity (topmost, sloping); coulombic efficiency (lower, horizontal).
Figure 20 shows (A) long-term cycling at 10 charge and discharge rates of a cell comprising a cell comprising a Nb16W5055 anode and NM0622 cathode; capacity (sloping);
columbic efficiency (horizontal). (B) shows performance of the extracted NM0622 electrode against LOLL (C) shows performance of the extracted Nb16W5055 electrode against LOLL
Figure 21 shows (A) charge and discharge profiles of Nb16W5055-LTO mixtures in a ratio of 7:3, 1:1 and 3:7 normalised to gravimetric capacity, order of charging curves at 3.0 V: 3:7 (leftmost), 5:5 (second from left), 7:3 (rightmost); order of discharging curves at 1.0 V: 3:7 (leftmost), 5:5 (second from left) and 7:3 (rightmost). (B) rate performance of the mixtures, order at 0.20: 7:3 (topmost), 5:5 (second from top), 3:7 (bottommost). (C) longer term cycle performance at 100 change and discharge rates, 10 points: 7:3 (topmost), 5:5 (second from top), 3:7 (bottommost); 100 curves: 3:7 (topmost), 5:5 (second from top), 7:3 (bottommost).

9 Figure 22 shows (A) change and discharge profiles of a full cell comprising a 3:7 (Nbi6W5055:LTO) anode and an NM0622 cathode and (B) rate performance of the cell.
Detailed Description of the Invention The invention generally provides an electrode comprising a niobium tungsten oxide, an electrochemical cell comprising the electrode, and the use of the cell, for example, in a lithium ion battery, at high C-rates of 5C during charging and/or discharging.
The preparation of Nb16W5055 has previously been described by, amongst others, Roth and Wadsley. The preparation of Nb18W16093 has previously been described by, amongst others, Stephensen. However, the electrochemical properties of Nb16W5055 and Nb18W16093 are not described in these documents.
Electrodes comprising NID8W9047 (Montemayor et al.); Nb26W4077 (Fuentes etal.); Nb14W3044 (Fuentes etal.); and NbxWi_x03,d2, wherein 0 x 0.25 (Yamada et e/.), have been previously described. However, the capacity of the materials against the C-rate was not measured.
Electrodes comprising Nb8_xW9_x047, wherein 1 x 6, have been described by Cruz et e/.
However, the electrochemical cell comprising the electrodes is used under limited conditions, and there is no disclosure of the cell operating under high-rate conditions.
Moreover, the authors report that irreversible structural transformations in the matrix-host result in loss of capacity after the first cycle.
Electrodes comprising Nb12W033 have been described by Saritha et al. and Yan et al.
Yan et al. test an electrochemical cell comprising a electrospun Nb12W033 electrode at a maximum current density of 700 mkg-1 (corresponding to a C-rate of 3.6C).
Saritha et al.
test an electrochemical cell comprising Nb12W033 at a reported C-rate of no more than 20C.
However, Saritha et al. apparently define the C-rate as reaction (i.e. removal or insertion) of one lithium ion in one hour. This corresponds to one electron transfer per formula unit.
Thus, the 20C rate for Nb12W033 reported by Saritha et al. corresponds to 1.54C using the convention defined in this work (equivalent to 294 mkg-1).
The present inventors have developed electrodes comprising a niobium tungsten oxide that has favorable lithium ion diffusion properties, and thus exhibit superior performance even with micron sizes particles. The electrodes exhibit extremely high volumetric energy densities and high capacities at high rates of charging and discharging.
The voltage values described herein are made with reference to LOU, as is common in the art.

The C-rate is a measure of the rate at which a battery is discharged relative to its maximum capacity. The C-rate may be defined as the inverse of the number of hours to reach a defined theoretical capacity e.g., 10C corresponds to a 6 min discharge or charge time. In 5 this work, C-rate is defined relative to one electron transfer per transition metal, e.g., for Nb16W5055, 1C = 171.3 mA=h=g-1, 20C = 3426 mA=h=g-1. The theoretical capacity is calculated by:
2.c,6485.3 [C.
____________________________________________________________________________ ¨ _71.3 rnA = h = g-1 = 1.6'1 [.i -]
where n is the number of electrons transferred per formula unit, F is Faraday's constant, 3.6 is a conversion factor between Coulombs and the conventional mA=h=g-1, and m is the mass per formula unit. Thus, a 1C rate corresponds to the reaction (i.e. insertion or removal) of 21 lithium ions per formula unit of Nb16W5055in one hour, as this material contains 21 transition metals per formula unit.
The high-rate application may also be described by reference to (gravimetric) current density, for example where the current density is at least 800 mkg-1 or 1000 mkg-1.
Current density is related to C-rate by:
' MI g Thus, for Nb16W5055 a current density of 800 mkg-1 corresponds to a C-rate of 4.67C and for Nb18W16093 a current density of 800 mkg-1 corresponds to a C-rate of 5.36C
using the convention defined in this work.
All (gravimetric) capacities are quoted based on the mass of the active electrode material.
Working Electrode The invention provides a working electrode comprising a niobium tungsten oxide. The working electrode is electrically conductive, and is electrically connectable to a counter electrode, for example within an electrochemical cell.
The working electrode may be an anode or cathode during a discharge step, for example in a lithium ion battery. Typically, the working electrode is the anode during a discharge step.

Typically, the working electrode for use in the method comprises a molar ratio of Nb2O5 to W03 from 6:1 to 1:15. Preferably, the molar ratio of Nb2O5 to W03 in the working electrode is from 8:5 to 11:20.
Typically, the working electrode for use in the method comprises a niobium tungsten oxide selected from Nb12W033, Nb26W4077, Nb14W3044, Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093, Nb22W200115, NID8W9047, Nb54W820381, Nb20VV310143, Nb4W7031, or Nb2W15050 or combinations thereof. Preferably, the working electrode comprises Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093 or Nb22W200115 or combinations thereof.
Typically, the molar ratio of Nb2O5 to W03 in the working electrode is from 8:5 to 11:20.
Preferably, the molar ratio of Nb2O5 to W03 in the working electrode is 8:5 or 9:16.
Typically, the working electrode comprises Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093, or Nb22W200115, or combinations thereof. Preferably the working electrode comprises Nb16W5055 or Nb18W16093, or combinations thereof.
Optionally, the working electrode comprises a mixture of niobium tungsten oxide and an additional active material. The additional active material may be an additional metal oxide.
For example, the working electrode may comprise a mixture of niobium tungsten oxide and an additional active material selected from lithium titanate (LTO; Li4Ti5012), titanium niobium oxides (for example TiNb207), titanium tantalum oxides (for example TiTa207), tantalum molybdenum oxides (for example Ta8W9047) and niobium molybdenum oxides (for example Nb2Mo3014)=
Graphite may also be used as an additional active material. A working electrode comprising a mixture of niobium tungsten oxide and graphite is cheaper to produce while maintaining the beneficial properties outlined above.
Preferably, the working electrode comprises a mixture of niobium tungsten oxide and LTO.
The ratio of niobium tungsten oxide to LTO may be from 95:5 to 5:95 by weight.
For example, the ratio may be from 90:10 to 10:90 by weight, from 80:20 to 20:80 by weight, from 70:30 to 30:70 by weight, from 60:40 to 40:60 by weight or the ratio of niobium tungsten oxide to LTO may be 1:1 by weight.
Preferably, the working electrode consists essentially of niobium tungsten oxide and an additional active material. For example, the working electrode consists essential of a mixture of niobium tungsten oxide and LTO.
Typically, the working electrode does not have a porous nor hierarchical structure. For example, the electrode material may have a specific surface area of less than 20 m2.g-1, less than 10 m2.g-1, less than 5 m2.g-1, less than 3 m2.g-1, less than 2 m2.g-1 or less than 1 m2.g-1.

The specific surface area of the electrode material may be known, or it may be determined using standard techniques such as N2 adsorption isotherm analysis and Brunauer¨Emmett¨

Teller (BET) theory.
Alternatively, the working electrode may have a porous structure. For example, the working electrode may have a specific surface area of at least 50 m2.g-1, at least 60 m2. 70 m2.g-1, 80 m2.g-1, 90 m2.g-1, 100 m2.g-1, 150 m2.g-1, 200 m2.g-1, 300 m2g. -1, or 400 m2.g-1.
The working electrode may have a pore volume of of at least 0.1 cm3.g-1, at least 0.2 cm3.g-1, at least 0.4 cm3.g-1, at least 0.5 cm3.g-1, at least 0.7 cm3.g-1, at least 0.8 cm3.g-1, at least 0.9 cm3.g-1, at least 1.0 cm3.g-1, at least 1.5 cm3.g-1 or at least 2.0 cm3.g-1.
The pore volume of the electrode material may be known, or it may be determined using standard techniques such as N2 adsorption isotherm analysis and Barrett-Joyner-Halenda (BJH) theory.
The porous working electrode may have an average pore size (largest cross section) of at least 1 nm, at least 5 nm, at least, 10 nm, at least 20 nm, at least 30 nm, at least 40 nm, at least 50 nm or at least 100 nm.
The porous working electrode may have macroporous structure. Thus, the porous working electrode may contain pores having pores having a largest cross section of at least 200 nm, at least 500 nm, at least 1 pm, or at least 5 pm.
The pore size of the electrode material may be known, or it may be determined using standard techniques such as scanning electron microscopy (SEM).
The working electrode may additionally comprise porous carbon, such as porous reduced graphene oxide.
Electrodes comprising porous carbon are generally light and conductive, and can provide large pore volumes, which can allow rapid transport of lithium ions and electrons to the active materials. They may also increase the electrochemical capacity of the working device.
The working electrode may additionally comprise reduced graphene oxide, Ketjen black or Super P carbon.
Alternatively, the working electrode may have a hierarchical structure. For example, the working electrode may additionally comprise hierarchical reduced graphene oxide (rG0).

Typically, the working electrode comprise a niobium tungsten oxide in particulate form. The size of the niobium tungsten oxide particles of the working electrode may be known, or it may be determined using standard techniques such as SEM.
Typically, the niobium tungsten oxide particles of the working electrode have primary particle size of at least 1 pm. The primary particle size is the size of the individual crystallite. It is the smallest identifiable subdivision in a particulate system. For example, the niobium tungsten oxide particles have a primary particle size of at least 2 pm, 3 pm, 4 pm, 5 pm or pm.
The individual niobium tungsten oxide particles may agglomerate to form secondary particles. Typically, the niobium tungsten oxide particles have an agglomerate (secondary) particle size of at least 5 pm. More preferably, the niobium tungsten oxides have an agglomerate particle size of at least 10 pm, 15 pm, 20 pm, 25 pm or 30 pm.
Where present, the additional active material may be in particulate form. The size of the additional active material particles may be known, or it may be determined using standard techniques such as SEM.
Preferably, the additional active material particles have a primary particle size of 1 pm or less. For example, the additional active material particles have a primary particle size of 800 nm or less, 750 nm or less, 700 nm or less, 600 nm or less, 500 nm or less, 400 nm or less, 300 nm or less, 200 nm or less or 150 nm or less. Particulate lithium titanate typically has a particle size within this range.
Electrodes comprising a mixture of niobium tungsten oxide and an additional active material having partial sizes within the ranges described above can be charged and discharged at very high C-rates and at very high charge densities.
To improve conductivity at the working electrode, a conductive carbon material (e.g., carbon black, graphite, nanoparticulate carbon powder, carbon fiber and/or carbon nanotubes) is typically admixed with the working electrode material. Alternatively, the conductive carbon material may be coated onto the working electrode material. In one embodiment, the working electrode comprises porous carbon, such as porous reduced graphene oxide, which may wrap the larger niobium oxides particles.
Typically, the working electrode contains 1-5% by weight of binders.
The electrode may consist essentially of niobium tungsten oxide.

Alternatively, the working electrode is admixed with a binder or adhesive.
Some examples of binders or adhesives include PVDF, PTFE, CMC, PAA, PMMA, PEO, SBR and co-polymers thereof.
.. The working electrode is typically fixed to a current collector, such as a copper or aluminum collector, which may be in the form of a plate.
The inventors have assessed a working electrode comprising a particulate niobium tungsten oxide using a standard electrode configuration of 8:1:1 active material/carbon/binder with a 2-3 mg=cm2 loading of active material and a 1.27 cm2 electrode area against a lithium counter electrode in a 2032-type coin cell geometry and using 1.0 M LiPF6 in ethylene carbonate/dimethyl carbonate as electrolyte.
Under these conditions, the inventors have found that a working electrode comprising a niobium tungsten oxide can maintain a capacity of up to 150 mA=h=g-1 at 100 for 1000 cycles, and a capacity of up to 125 mA=h=g-1 at 200 for 750 cycles.
In addition, the inventors have found that a working electrode comprising a niobium tungsten oxide has a sloping, rather than flat, voltage profile.
The inventors have assessed solid-state lithium diffusion within niobium tungsten oxides using both pulsed field gradient NMR (PFG NMR) and the galvanostatic intermittent titration technique (GITT). The inventors have found that the niobium tungsten oxides have a solid-state lithium diffusion coefficient (Du) of 10-13 to 10-12 m2.s-1 at 298 K. This corresponds .. to a characteristic diffusion length of ca. 10 pm for a 1 minute discharge.
The invention also provides a working electrode comprising a niobium molybdenum oxide.
The working electrode is electrically conductive, and is electrically connectable to a counter electrode, for example within an electrochemical cell.
The working electrode may be an anode or cathode during a discharge step, for example in a lithium ion battery. Typically, the working electrode is the anode during a discharge step.
Typically, the working electrode for use in the method comprises a molar ratio of Nb2O5 to .. Mo03 of from 6:1 to 1:3. Preferably, the molar ratio of Nb2O5 to Mo03in the working electrode is 1:3.
Typically, the working electrode for use in the method comprises a niobium molybdenum oxide selected from Nb2Mo3014, Nb14Mo3044 or Nb12Mo044. Preferably, the working .. electrode comprises Nb2Mo3014.

Typically, the working electrode does not have a porous nor hierarchical structure. The working electrode may have a specific surface area, pore volume and average pore size as described above.
5 Typically, the working electrode comprise a niobium molybdenum oxide in particulate form.
The niobium molybdenum oxide particles of the working electrode may have a primary or agglomerate particle size as described above.
The working electrode may contain binders and adhesives as described above.
Electrochemical Cell The present invention also provides an electrochemical cell comprising a working electrode of the invention. The working electrode may be an anode or cathode during a discharge step, for example in a lithium ion battery. Typically, the working electrode is the anode during a discharge step.
The electrochemical cell typically comprises a counter electrode and an electrolyte. The electrochemical cell may comprise a current collecting plate. The electrochemical cell may be in electrical connection with a power supply. The electrochemical cell may be in electrical connection with a measurement device, for example an ammeter or voltmeter.
The counter electrode may be an anode or cathode during a discharge step, for example in a lithium ion battery. The counter electrode is typically the cathode during a discharge step.
Suitable cathode materials include lithium-containing or lithium-intercalated material, such as a lithium metal oxide, wherein the metal is typically a transition metal such as Co, Fe, Ni, V
or Mn, or combination thereof. Some examples of positive electrode materials include lithium cobalt oxide (Li0002), lithium nickel manganese cobalt oxide (NMC, LiNiMnCo02, e.g. LiNio600o2Mno202), lithium vanadium fluorophosphate (LiVP04F), lithium nickel cobalt aluminum oxide (NCA, LiNiCoA102), lithium iron phosphate (LFP, LiFePO4)and manganese-based spinels (e.g. LiMn204).
To improve conductivity at the counter electrode, a conductive carbon material (e.g., carbon black, graphite, nanoparticulate carbon powder or carbon nanotubes) is typically admixed with the counter electrode material. In one embodiment, the counter electrode comprises porous carbon, such as porous reduced graphene oxide.
In one embodiment, the counter electrode is substantially free of binders.

In an alternative embodiment, the counter electrode is admixed with a binder or adhesive.
Some examples of binders or adhesives include PVDF, PTFE, CMC, PAA, PM MA, PEO, SBR and co-polymers thereof.
The counter electrode is typically fixed to a current collecting substrate, such as an aluminum plate.
Typically, the electrolyte in the electrochemical cell is suitable for solubilising lithium ions.
Typically, the electrolyte in a charged and discharged cell contains lithium ions.
Typically, the electrolyte comprises lithium salts, such as LiTFSI, (bis(trifluoromethane)sulfonimide lithium salt, LiPF6, LiBF4, LiC104, LiTF
(lithium triflate) or lithium bis(oxalato) borate (LiBOB).
The electrolyte may be a liquid electrolyte, such as a liquid at ambient temperature, for example at 25 C.
The electrolyte may be a non-aqueous electrolyte. The electrolyte may comprise a polar aprotic solvent. The electrolyte may comprise an organic solvent. Solvents for dissolving lithium ions are well known in the art.
Suitable solvents include carbonate solvents. For example propylene carbonate (PC), ethylene carbonate (EC), butylene carbonate (BC), chloroethylene carbonate, fluorocarbonate solvents (e.g., fluoroethylene carbonate and trifluoromethyl propylene carbonate), as well as the dialkylcarbonate solvents, such as dimethyl carbonate (DMC), diethyl carbonate (DEC), dipropyl carbonate (DPC), ethyl methyl carbonate (EMC), methyl propyl carbonate (MPC), and ethyl propyl carbonate (EPC).
Suitable solvents also include sulfone solvents. For example methyl sulfone, ethyl methyl sulfone, methyl phenyl sulfone, methyl isopropyl sulfone (MiPS), propyl sulfone, butyl sulfone, tetramethylene sulfone (sulfolane), phenyl vinyl sulfone, allyl methyl sulfone, methyl vinyl sulfone, divinyl sulfone (vinyl sulfone), di phenyl sulfone (phenyl sulfone), dibenzyl sulfone (benzyl sulfone), vinylene sulfone, butadiene sulfone, 4-methoxyphenyl methyl sulfone, 4-chlorophenyl methyl sulfone, 2-chlorophenyl methyl sulfone, 3,4-dichlorophenyl methyl sulfone, 4-(methylsulfonyl)toluene, 2-(methylsulfonyl) ethanol, 4-bromophenyl methyl sulfone, 2-bromophenyl methyl sulfone, 4-fluorophenyl methyl sulfone, 2-fluorophenyl methyl sulfone, 4-aminophenyl methyl sulfone, a sultone (e.g., 1,3-propanesultone), and sulfone solvents containing ether groups (e.g., 2-methoxyethyl(methyl)sulfone and 2-methoxyethoxyethyl(ethyl)sulfone).
Suitable solvents also include silicon-containing solvents such as a siloxane or silane. For example hexamethyldisiloxane (HMDS), 1,3-divinyltetramethyldisiloxane, the polysiloxanes, and polysiloxane-polyoxyalkylene derivatives. Some examples of silane solvents include methoxytrimethy lsilane, ethoxytrimethy lsilane, dimethoxydimethylsilane, methyltrimethoxysilane, and 2-(ethoxy)ethoxytrimethylsilane.
Typically, an additive may be included in the electrolyte to improve performance. For example vinylene carbonate (VC), vinyl ethylene carbonate, allyl ethyl carbonate, t-butylene carbonate, vinyl acetate, divinyl adipate, acrylic acid nitrile, 2-vinyl pyridine, maleic anhydride, methyl cinnamate, ethylene carbonate, halogenated ethylene carbonate, a-bromo-y-butyrolactone, methyl chloroformate, 1,3-propanesultone, ethylene sulfite (ES), propylene sulfite (PS), vinyl ethylene sulfite (VES), fluoroethylene sulfite (FES), 12-crown-4 ether, carbon dioxide (002), sulfur dioxide (SO2), and sulfur trioxide (SO3).
The electrochemical cell may also include a solid porous membrane positioned between the negative and positive electrodes. The solid porous membrane may partially or completely replace the liquid electrolyte. The solid porous membrane may comprise a polymer (e.g., polyethylene, polypropylene, or copolymer thereof) or an inorganic material, such as a transition metal oxide (e.g., titania, zirconia, yttria, hafnia, or niobia) or main group metal oxide, such as silicon oxide, which can be in the form of glass fiber.
The solid non-porous membrane may comprises a lithium-ion conductor. For example, LLZO (garnet family), LSPO (LISICON family), LGPS (thio-LISICON family), LATP/LAGP
(NASICON family), LLTO (perovskite family) and phosphide/sulfide glass ceramics The electrochemical cell may be charged or discharged at a C-rate of at least 5C, such as the electrochemical cell may be charged or discharged at a C-rate of at least 5C with respect to one electron transfer per transition metal per formula unit of working electrode material.
Preferably, the electrochemical cell may be charged or discharged at a C-rate of at least 100, 150, 20C, 25C, 30C, 35C, 40C, 50C, 600 or 800.
The electrochemical cell may be charged or discharged at a current density of at least 750 mkg-1. Preferably, the electrochemical cell may be charged or discharged at a current density of at least 800 mkg-1, 850 mkg-1, 900 mkg-1, 950 mkg-1, 1000 mkg-1, mkg-1, 1100 mkg-1, 1200 mkg-1 or 1300 mkg-1.
The electrochemical cell may have a volumetric charge density of at least 200, 300, 400, 500, 600 or 700 A=h=L-1 at 1C. Typically, the electrochemical cell has a volumetric charge density of up to 100, 200, 300 or 400 A=h=L-1 at 20C.
The electrochemical cell may have a capacity retention of at least 70%, 75%, 80%, 85%, 90%, 95%, 96%, 97%, 98%, 99%, or 100% at 20C maintained over at least 50, 100, 150, 200, 250, 300, 400, 500, 600, 700, 800, 900, 1,000, 1,200, 1,500, 1,800, or 2,000 cycles.

The electrochemical cell may be regarded as fully charged when the voltage passes a threshold value. For example, an electrochemical cell comprising a lithium metal anode and a niobium tungsten oxide cathode may be regarded as fully charged when the voltage rises above a practicable level, such as where the voltage rises above 2.0 V against Li/Li, such as above 2.25 V or above 2.5 V.
The electrochemical cell may be regarded as fully discharged when the voltage passes a threshold value. For example, an electrochemical cell comprising a lithium metal anode and a niobium tungsten oxide cathode may be regarded as fully discharged when the voltage drops below a practicable level, such as where the voltage drops below 1.5 V
against Li/Li, such as below 1.25 V or below 1.0 V.
The electrochemical cell may be a lithium ion cell.
Methods The invention provides a method of charging and/or discharging an electrochemical cell at a C-rate of at least 5C, such as the electrochemical cell may be charged or discharged at a C-rate of at least 5C with respect to one electron transfer per transition metal per formula unit of working electrode material. The electrochemical cell comprises a working electrode comprising a niobium tungsten oxide and/or niobium molybdenum oxide.
Preferably the electrochemical cell contains a counter electrode and an electrolyte.
Preferably the method is a method of charging and/or discharging an electrochemical cell at a C-rate of at least 10C, 15C, 20C, 25C, 30C, 35C, 40C, 50C, 60C or 80C.
The method may be a method of charging and/or discharging an electrochemical cell at a current density of at least 750 mA=g' such as at least 800 mA.V. Preferably the method is a method of charging and/or discharging an electrochemical cell at a current density of at least 800 mA.V, 850 mA.V, 900 mA.V, 950 mA.V, 1000 mA.V, 1050 mA.V, 1100 mA.V, 1200 mA=g' or 1300 mA=g'.
The method may involve a cycle of charging and discharging or discharging and charging the electrochemical cell. The cycle may be repeated more than once. Thus, the method comprises 2 cycles or more, 5 cycles or more, 10 cycles or more, 50 cycles or more, 100 cycles or more, 500 cycles or more, 1,000 cycles or more, or 2,000 cycles or more.
Battery The present invention also provides a battery comprising one or more electrochemical cells of the invention. The battery may be a lithium ion battery.

Where there are a plurality of cells, these may be provided in series or parallel.
A battery of the invention may be provided in a road vehicle, such as an automobile, moped or truck. Alternatively, a battery of the invention may be provided in a rail vehicle, such as a train or a tram. A battery of the invention may also be provided in an electric bicycle (e-bike).
A battery of the invention may be provided in a regenerative braking system.
A battery of the invention may be provided in a portable electronic device, such as a mobile phone, laptop or tablet.
A battery of the invention may be provided in a power grid management system.
Uses The invention generally provides the use of a working electrode comprising a niobium tungsten oxide in a high-rate electrochemical cell, such as an electrochemical cell as described herein. Typically, the electrochemical cell may be charged or discharged at a C-rate of at least 5C, such as the electrochemical cell may be charged or discharged at a C-rate of at least 5C with respect to one electron transfer per transition metal per formula unit of working electrode material. Preferably, the electrochemical cell may be charged or discharged at a C-rate of at least 10C, 15C, 20C, 25C, 30C, 35C, 40C, 50C, 60C
or 80C.
The electrochemical cell may be charged or discharged at a current density of at least 750 mkg-1. Preferably, the electrochemical cell may be charged or discharged at a current density of at least 800 mkg-1, 850 mkg-1, 900 mkg-1, 950 mkg-1, 1000 mkg-1, mkg-1, 1100 mkg-1, 1200 mkg-1 or 1300 mkg-1.
The working electrode may find use in the methods described herein.
Other Preferences Each and every compatible combination of the embodiments described above is explicitly disclosed herein, as if each and every combination was individually and explicitly recited.
Various further aspects and embodiments of the present invention will be apparent to those skilled in the art in view of the present disclosure.
"and/or" where used herein is to be taken as specific disclosure of each of the two specified features or components with or without the other. For example "A and/or B" is to be taken as specific disclosure of each of (i) A, (ii) B and (iii) A and B, just as if each is set out individually herein.
Unless context dictates otherwise, the descriptions and definitions of the features set out 5 above are not limited to any particular aspect or embodiment of the invention and apply equally to all aspects and embodiments which are described.
Certain aspects and embodiments of the invention will now be illustrated by way of example and with reference to the figures described above.
Experimental The following examples are provided solely to illustrate the present invention and are not intended to limit the scope of the invention, as described herein.
Synthesis of Nb16W5055 and Nb18W16093 Nb16W 5055 and Nb18W16093 were synthesized by co-thermal oxidation of dark blue Nb02 (Alfa Aesar, 99+%) and brown W02 (Alfa Aesar, 99.9%) in approximately one to five gram batches. The partially reduced oxides were massed to within 0.001 g of the 16:5 or 18:16 ma ratios, ground together by hand with an agate mortar and pestle, pressed into a pellet at 10 MPa, and heated in a platinum crucible at a rate of 10 K=min-1 to 1473 K, and naturally cooled in the furnace over ca. 2 h.
Synthesis of Nb8W9047 and Nb12W033 Nb8W9047 and Nb12W033 were synthesized by co-thermal oxidation of dark blue Nb02 (Alfa Aesar, 99+%) and brown W02 (Alfa Aesar, 99.9%) in approximately one to five gram batches. The partially reduced oxides were massed to within 0.001 g of the 8:9 or 12:1 -nolar ratios, ground together by hand with an agate mortar and pestle, pressed into a pellet at 10 MPa, and heated in a platinum crucible at a rate of 10 K=min-1 to 1473 K, and naturally cooled in the furnace over ca. 2 h.
Synthesis of Nb2Mo3014 Nb2Mo3014 synthesized by co-thermal oxidation of dark blue Nb02 (Alfa Aesar, 99+%) and dark brown Mo02 (Sigma, 99%), or co-thermal oxidation of white Nb2O5 (Sigma, 99.9985%) and off-white Mo03 (Sigma, 99.5`)/0), in approximately one to five gram batches. The partially reduced oxides were massed to within 0.001 g of the 2:3 or 1:3 ..ioi ratio, ground together by hand with an agate mortar and pestle, pressed into a pellet at 10 MPa, and heated in a platinum or alumina crucible at a rate of 10 K=min-1 to 873 K, 923 K or 973 K, and quenched in air outside the furnace on a metal plate.

Microscopic Characterisation Scanning electron microscopy (SEM) images were taken with a Zigma VP
instrument (Zeiss) at 3.0 kV and a MIRA3 instrument (TESCAN) at 5.0 kV with secondary electron detection.
Tap density was recorded on an AutoTap (Quantachrome Instruments) instrument operating at 257 taps=min-1. Tap densities were measured according to ASTM international standard B527-15 modified to accommodate a 5 to 10 cm3 graduated cylinder.
Both Nb16W5055 and Nb18W16093 formed subhedral particles with ca. 3 to 10 pm primary particles that appeared in the electron microscope to be intergrown/'cemented' into larger secondary particles of ca. 10 to 30 pm (Fig. 1 and 2). The bulk compounds are a series of complex "block" (Nb16W5055) or "bronze-like" (Nb18W16093) oxide structures (Fig. 2) largely comprised of corner and edge sharing NbO6 and W06 octahedra.
Nb16W5055 has a monoclinic structure comprised of subunits of corner-shared octahedra arranged into Re03-like blocks, four octahedra wide by five octahedra long, and infinite in the third dimension (Fig. 2A). The block subunits are connected by crystallographic shear planes along the edges and by tetrahedra at each corner leading to the notation (4 x 5)1 where, in (m x n)p, m and n denote block length in units of octahedra and p relates to the connectivity of the blocks which may also be joined in pairs (p = 2) or infinite ribbons (p = 00).
Nb18W16093 is orthorhombic, a 1 x 3 x 1 superstructure of the classic tetragonal tungsten bronze (TTB) (Fig. 2D and 3). The TTB structure is sometimes stabilized by cations (e.g.
K+, partially filled spheres in Fig. 3); alkali cation-free Nb18W16093 is stabilized by ¨M-0¨
chains partially occupying the tunnels and forming pentagonal bipyramids. The ionic and electronic implications for lithium intercalation, respectively, are that the layers of Nb18W16093 are still fully open and unoccupied by cations (i.e., around the plane (x, y, 1/2)) and all metal cations are in the desired d electron configuration while in classic TTB
structure neither of these criteria is met.
Electrochemical Characterization of Nb16W5055 and Nb18W16093 Electrochemical characterisation was conducted using a stainless steel 2032-coin cell (Cambridge Energy Solutions) with a conical spring, two 0.5 mm stainless steel spacer disks, a plastic gasket, and a glass microfiber separator (Whatman). To form the niobium tungsten oxide electrode, the niobium tungsten oxide and conductive carbon (Super P, TIMCAL) were ground by hand in an agate mortar and pestle in an 8:1 mass ratio. This powder was ground in a 9:1 mass ratio with poly(vinylidene difluoride) (PVDF, Kynar) dispersed in N-methyl pyrrolidone (NMP, Sigma-Aldrich, anhydrous, 99.5%). The slurry was coated onto aluminium or copper foil with a doctor blade (bar coater). The NMP
was removed by heating in an oven at 60 C for 24 hours. Though standard, Super P
carbon is a nanoparticu late powder and NMP is a hazardous organic solvent so appropriate nanoparticle cabinets/fume hoods should be used.
This 80/10/10 metal oxide/carbon/polymer electrode served as the cathode against a Li metal disk (LTS Research, 99.95%) anode in a half-cell geometry. In the electrochemical tests, the electrolyte was 1 M LiPF6 dissolved in 1:1 v/v ethylene carbonate/dimethyl carbonate (EC/DMC; Sigma-Aldrich, battery grade; also known as LP30). No additives were used. Electrochemistry was performed in a temperature-controlled room at 293 K. A
Biologic galvanostat/potentiostat with EC-Lab software was used to perform the electrochemical measurements.
Dense electrodes of large particles with 2 to 3 mg=cm-2 active mass loading were tested at current densities corresponding to discharge times of several hours to tens of seconds.
Nb16W5055 was charged with a 1 h constant voltage step at the top of charge to ensure a comparable starting point on discharge; Nb19W16093 was cycled without this step and stored over 100 mA=h=g-1 at 600 (i.e., in <60 s). High-rate cycling for 1000 cycles was performed on both oxides at 100/200 constant current without any potentiostatic step.
Reaction of Nb16W5055 with lithium (Fig. 4A) proceeds in three regions from 2.5 V to 1.0 V, with an average voltage of 1.57 V (Fig. 5), comparable to the average voltage of Li4Ti5012 of 1.55 V. The three regions, more easily observed in the derivative plot (Fig.
4B), are characterized by their slope and are reminiscent of the three regions observed in other crystallographic shear structures (e.g., H-Nb2O5, PNb9025, TiNb207, and Nb12W033). When the kinetics were examined over a range of current densities from 0/5 (34.3 mkg-1) up to 600 (10.3 ), Nb16W5055 showed unprecedented bulk rate performance (Fig. 4A
and 40). At 0/5, around 1.3 lithium ions can be reversibly intercalated per transition metal for a gravimetric capacity of ca. 225 mA=h=g-1. When the rate is increased by a factor of 25 to 50, Nb16W5055 maintains a capacity of 1.0 Li/TM (171 mA=h=g-1). At 200, which corresponds to a three minute discharge, it is still possible to exchange 0.86 Li/TM and access 148 mA=h=g-1. Rate tests on Nb16W5055 were measured with a potentiostatic hold at the top of charge to ensure a reliable starting point for discharge. To test the performance under more demanding conditions, 1000 cycles were measured with fixed galvanostatic discharge and charge conditions of 100 for 250 cycles followed by 200 for 750 cycles with no hold (Fig. 4F). Under these conditions, 0.90 Li/TM (avg. 155 mA=h=g-1) were reversibly intercalated at 100 with 95% capacity retention after 250 cycles on non-optimized or calendared electrodes. At 200, the capacity was 0.75 Li/TM (avg. 128 mA=h=g-1); the capacity retention was again 95% over the 750 cycles at 200.
The average voltage of Nb19W16093 is 1.67 V (Fig. 4D-F). In terms of gravimetric capacity, Nb19W16093 stores ca. 20 mA=h=g-1 less than Nb16W5055 at 0/5 and 10 due to the higher molar mass of the tungsten-rich bronze phase. However, at 200, Nb19W16093 is still able to accommodate a full unit Li+/TM for a capacity of ca. 150 mA=h=g-1. At 600 and (14.9 A=g-1), the capacity is still 105 and 70 mA=h=g-1, respectively.
Comparison of Cu Foil to Carbon-Coated Al Foil Current Collector Fig. 6 shows the effect of current collectors, which cannot be ignored at high rates.
For Nb16W5055cycled for 1000 cycles under constant current discharge and charge at 100/200, Cu foil current collector displayed moderately higher capacity than carbon-coated Al (C@AI) foil (Fig. 6A). Untreated Al foil has been shown to be insufficient for high current densities (Griffith et al.); C@AI demonstrated significant improvement over untreated Al. In Nb16W5055, the lower voltage region is the source of excess capacity beyond 1.0 Li+/TM at low rates but is effectively shifted below 1.0 V at moderate rates. The second discharge peak (centered at 1.2 V) is only observed at C/5 in the dQ/dV plot (Fig. 4B).
As a result, the capacity observed when cycling with a minimum voltage limit of 1.2 V vs. 1.0 V
becomes less significant as rate increases and safety may be further improved by avoiding lower voltages. Fig. 6B shows discharge and charge profiles between 3.0 and 1.0 V
for the 100th cycle at 100.
Longer Term Cycling as a Function of Minimum Cutoff Voltage Fig. 7 shows the effect of long term cycling at C/5.
Constant current constant voltage charging is a common method to maximize capacity without overcharging, as in (Fig. 7A), but the extra time required means that the cycling could be considered C/5 and 10 discharge but 0/6 and 0/2 charge. The 2nd to 50th cycle retention in Fig. 7A is 96% and 93% for a voltage minimum of 1.2 and 1.0 V, respectively.
The 51st to 100th cycles at 10 show capacity retentions of 99% and 101% for 1.2 and 1.0 V, respectively. Cycle retention for the 2nd to 50th cycles for C/5 in Fig. 7B is 88%, 90%, and 40% for 1.1, 1.0, and 0.9 V, respectively. Cycling time was approximately one month.
Overpotential in a Li II Li Symmetric Cell as a Function of Current Density As a control, Li II Li symmetric cells were cycled at current densities corresponding to those in Fig. 4A-E (Fig. 8). Cells were configured identically to those used for metal oxide testing with the exception of a second Li disk replacing the composite electrode. Rate testing was carried out with 5 cycles at 100 pA (C/5), 500 pA (10), 1 mA (20), 2.5 mA
(5C), 5 mA (100) and 10 cycles at 10 mA (200), 20 mA (400), 30 mA (600), and 50 mA (1000). The "rate" in parentheses indicates the inverse of the amount of time in hours that current was applied, simulating the rate test. At low current densities, below 1 mA (20), the overpotential is below 100 mV; however, at 5 mA (100) it rises to 200 mV and increases to ca.
700 mV at 1000.

The overpotentials in the symmetric cell (Fig. 8) closely match those observed in the electrochemical cycling curves of Fig. 4A and 4D. This suggests that the extremely high rates for a bulk electrode are approaching the limits of Li metal plating/stripping and/or lithium ion desolvation and transport in carbonate ester electrolytes at room temperature, i.e., a significantfraction of the ohmic drop seen during fast charging results from the Li metal and not the complex oxide electrode materials.
'Li Pulsed Field Gradient NMR Spectroscopy 7Li NMR diffusion spectra were recorded on a Bruker Avance III 300 MHz spectrometer using a Diff50 probehead equipped with an extended variable temperature capabilities.
Spectra were recorded with the stimulated echo pulsed field gradient (PFG) sequence shown in Fig. 9 to minimize spin-spin relaxation (T2) losses. After the first radiofrequency (rf) pulse, the net magnetization loses coherence due to T2 relaxation; thus, the time period following this pulse, which includes the first PFG pulse (to encode spin position), must be shorter than T2. In the stimulated echo sequence used here, a second 90 if pulse is applied which stores the net magnetization along the z axis prior to the diffusion time, A, allowing the observed species to diffuse for a time commensurate with the comparatively longer spin-lattice (Ti) value, as no T2 relaxation occurs.
During A, a short spoiler gradient (SINE.100) is applied to remove residual transverse magnetization.
Afterwards, a third 90 if pulse is applied, followed by a PFG pulse to decode spin position.
Sufficiently long delays between PFG and radiofrequency pulses were used 0.5 ms) to minimize eddy currents in the diffusion measurements.
During this sequence, the gradient strength, g, was varied from 0.87 to 1800 or 2300 G=cm-1, and 16 gradient steps were acquired using 'opt' shaped pulses with 1024-4096 transients.
The opt shape is a composite pulse that starts with a quarter of a sine wave, followed by a constant gradient, and ends with a ramp down (Fig. 9). The 'opt' gradient pulses provide the largest gradient integral for a given time period, maximizing the range of diffusion coefficients we could assess in this experiment.
Spectra were analysed in phase-sensitive mode and the response of the NMR
signal intensity, /, to variation in g, is described by the Stejskal¨Tanner equation:
D) /0 ) where /0 is the intensity in the absence of gradients, y is the gyromagnetic ratio (y7L, =
103.962x106.s-1.1-- , ) 1,5 is the effective gradient pulse duration, and D is the diffusion coefficient. Here, NMR signal intensity and integral gave similar 7Li diffusivities, but NMR

signal intensities gave more reliable data, as evaluated by the standard deviation of the fit.
Typical 5 values ranged from 0.8 ms to 1.5 ms and .6 values ranged from 50-100 ms for the bronze and the block phase samples, respectively.
5 Diffusion spectra were recorded at elevated temperatures (333-453 K) due to the increase in T2 observed at high temperature (e.g. T2for Li34Nb18W16093 is approximately 700 ps at room temperature vs. 1.9 ms at 453 K). (N.b. No attempt was made to calibrate the temperature for this experimental setup because a single-tuned 7Li coil was used and no reliable 7Li reference is routinely used for temperature calibration. The Bruker manual states

10 that for static measurements, the temperature calibration should be within 7 degrees of the set value.) The increase in T2 allowed the use of longer gradient pulses, 5, that were necessary to measure diffusion coefficients in the solid oxides.
Representative 7Li diffusion decay curves are shown in Fig. 10. The data quality is directly 15 correlated with the Li content and subsequent signal-to-noise ratio (SNR) of the 7Li NMR
spectra, where SNRs of 95, 56, 10, and 12 were observed for Fig. 10A
(Liio2Nbi8W16093), 10B (Lis 8Nbi8W16093), 100 (Li34Nbi8W16093), and 10D (Li63Nbi6W5055), respectively. We note that while the SNR of the low Li content Li34Nb18W16093 sample is low and the signal decay is only ca. 60%, the observed trend in 7Li diffusivity and activation energy is consistent 20 with that observed in more lithiated bronze structures.
Lis 3Nbi6W5055 shows two-component behavior with lithium transport as rapid as 4.3x1012 M2' S-1 at 333 K (Fig. 11). Assuming Arrhenius behavior and the measured activation energy of 0.23 eV, the room temperature lithium diffusion coefficient is estimated to be 2.1 x10-12 25 m2=s-1 (Table 1).
LixNb18W16093 (x = 3.4, 6.8, 10.2) exhibited similar diffusion and activation energies, with room temperature diffusion coefficients of 1.1 x1013 m2. S-1 and Ea in the range of 0.27 to 0.30 eV.

Table 1 - Du and Ea measurements for selected niobium tungsten oxide materials Compound Du (m2=s-1) at 298 K Du (m2=s-1) at 413 K Ea (eV) Li63Nb16W5O55-a (15%) 2.1x10-12 2.7x10-11 0.23 0.04 Li63Nb16W5O55-b (85%) 1.7x10-13 5.2x10-13 0.10 0.04 Li84Nb16W5055 1.6x10-13 6.5x10_13 (403 K) 0.13 0.01 Li34Nb18W16093 1.1x10-13 2.0x10-12 0.27 0.03 Lis sNbi8W16093 1.1x10-13 1.8x10-12 0.30 0.01 Li1o2Nb18W16093 1.1x10-13 2.7x10-12 0.29 0.01 Lithium diffusion in both niobium tungsten oxide structures is markedly faster than that of Lia+xTi5012 or LixTiO2 at ca. 10_16_10_15 m2.s-1 and is close to the best known lithium solid electrolytes (Table 2).
PFG NMR (Fig. 11) results indicate that initial lithium ion diffusion is of the order 10-12 to 10-13 m2.s-1 while galvanostatic intermittent titration technique (GITT) measurements (Fig. 12) show that the niobium tungsten oxides retain this rapid motion to high capacities 1.5 Li/TM) where the diffusion then drops by about two orders-of-magnitude toward 2.0 Li/TM.
This suggests that the inherent range of the niobium tungsten oxide electrode materials for high-rate multiredox extends to approximately 1.5 Li/TM. The diffusion coefficients on the order of 10-12 to 10-13 m2.s-1 measured for these materials are consistent with the values required to achieve full lithiation of 6 to 19 pm particles on a 600 timescale.

Table 2 - Du measurements for known materials t..) o ,-, o Compound Structure Type Du (m2=s-1) T (K) Technique Reference (...) Li10GeP2S12 Thio-LISICON 2x10-12 298 PFG NMR
Kuhn, et al. (2013) t..) cio Li10GeP2S12 Thio-LISICON 4x10-11 453 PFG NMR
Kuhn, et al. (2013) Li7GePS8 Thio-LISICON 2x10-12 298 PFG NMR
Kuhn, et al. (2013) Li7GePS8 Thio-LISICON 4x10-11 453 PFG NMR
Kuhn, et al. (2013) Li10SnP2S12 Thio-LISICON 1.4x10-12 298 PFG NMR
Kuhn, et al. (2014) Li10SnP2S12 Thio-LISICON 4x10-11 453 PFG NMR
Kuhn, et al. (2014) Li11Si2PS12 Thio-LISICON 3.5x10-12 298 PFG NMR
Kuhn, et al. (2014) P
Li11Si2PS12 Thio-LISICON 4x10-11 453 PFG NMR
Kuhn, et al. (2014) =, , Li7P3S11 Thio-LISICON 1-5x10-12 303 PFG NMR
Hayamizu, et al. (2013) , rõ
Li7P3S11 Thio-LISICON 2-11x10' 353 PFG NMR
Hayamizu, et al. (2013) rõ

rõ
fl-Li3PS4 Thio-LISICON 5.4)00'3 373 PFG NMR
Gobet, et al.
, , amorphous-Li3PS4 Amorphous (Thio-LISICON) 6.5x10-13 303 PFG NMR
Hayamizu, et al. (2016) , .3 amorphous-Li3PS4 Amorphous (Thio-LISICON) 1.6-3.4x10-12 353 PFG NMR Hayamizu, et al. (2016) Lio.6[Lio.2Sno.8S2] Layered (01) 2-20x10-12 298 PFG NMR Holzmann, et al.
Lio.6[Lio.2Sno.8S2] Layered (01) 2.6x10-10 407 PFG NMR Holzmann, et al.
Li3.4V0.6Sio.404 LISICON 5x10-15 333 tracer Ishiyama, et al.
Lit5A10.5Get5(PO4)3 NASICON 2.9x10-13 311 PFG NMR Hayamizu et al. (2017) 1-d n Li12A10.2Ti1.8 (PO4)3 NASICON 1.5x10-12 250 NMR relaxometry PFG NMR
Arbi, et al.
m 1-d t..) o Li6.6La3Zr1.6Ta0.4012 Garnet 3.5x10-13 353 PFG NMR Hayamizu et al. (2015) o O-Li7La3Zr2012 Garnet 1.8x10-18 298 NMR
relaxometry Kuhn, et al. (2011) o u, o Li7La3Zr2012 Garnet 1.3x10-17 325 NMR
relaxometry Kuhn, et al. (2011) o Compound Structure Type Du (m2.s-1) T (K) Technique Reference Li7La3Zr2012 Garnet 3.3x10-14 530 NMR
relaxometry Kuhn, et al. (2011) 0 t..) Graphite (Stage I) Graphite 1-2x10-15 298 NMR
relaxometry Langer, et al. =
,-, Li metal bcc 5x10-15 298 PFG NMR
(extrapolated) Mali, et al.
(...) .6.
Li metal bcc 1x10-12 400 PFG NMR
Mali, et al. t..) .6.
oe Li4Ti5012 Spinel 3.2x10-15 298 p+-SR
Sugiyama, et al.
Li57Ti5012 Spinel 2.7x10-16 298 NMR
relaxometry Wilkening, et al.
LiTi204 Spinel 3.6x10-15 298 p+-SR
Sugiyama, et al.
/3-Li2TiO3 Li2SnO3 2x10-17 433 NMR
relaxometry Ruprecht, et al.
Lio 12TiO2 micro Anatase component 4.7x10-16 293 NMR
relaxometry Wagemaker, et al. (2001) Lio 12TiO2 micro Li-titanate component 1.3x10-15 293 NMR
relaxometry Wagemaker, et al.(2001) P
Lio osTiO2 nano Anatase component 1.9x10-16 293 NMR
relaxometry Wagemaker, et al. (2007) -, Lio osTiO2 nano Li-titanate component 5.7x10-16 293 NMR
relaxometry Wagemaker, et al. (2007) , oe .
Lio 12TiO2 nano Anatase component 1.1x10-16 293 NMR
relaxometry Wagemaker, et al. (2007) IV
, IV
F' I- i 0 12T i 0 2 nano Li-titanate component 1.8x10-16 293 NMR relaxometry Wagemaker, et al. (2007) ,A1 , Lio 12TiO2 nano Li-titanate component 4.9x10-16 413 NMR
relaxometry Wagemaker, et al. (2007) , -Lio55TiO2 nano Li-titanate 1.7x10-16 293 NMR
relaxometry Wagemaker, et al. (2007) Lio55TiO2 nano Li-titanate 4.6x10-16 413 NMR
relaxometry Wagemaker, et al. (2007) LiMn204 Spinel 1x10-20 350 NMR
relaxometry Verhoevenm et al.
LiMn204 Spinel 1.8x10-16 623 Tracer lshiyama, et al. (2016) LiNb03 LiNb03 7.5x10-15 890 NMR
relaxometry Bork and Heitjans Iv n Li3Nb04 Li3Nb04 4x10-21 353 NMR
relaxometry Ruprecht and Heitjans m Li3Nb04 Li3Nb04 1x10-16 553 NMR
relaxometry Ruprecht and Heitjans Iv t..) o ,-, Abbreviations: bcc bcc = body-centered cubic, p+-SR = muon spin resonance o, u, o .6.
o Galvanosta tic Intermittent Titration Technique (GITT) Information on electrode thermodynamics, including phase transitions, and lithium kinetics can in principle be extracted from GITT measurements by tracking the voltage evolution after a brief current pulse as lithium diffuses and the chemical potential equilibrates within the electrode/particles. Reliable quantitative diffusion coefficients, Du, are, however, difficult to extract from GITT alone. In order to determine a diffusion coefficient from GITT
measurements, a diffusion length (L) must be defined but a battery electrode is a heterogeneous system. First, it is a composite of active material (here, metal oxide), porous carbon, and polymeric binder. Within this composite, there will be a distribution of particle sizes (unless single crystals or well-defined particles are employed; even then the diffusion varies with lattice direction). Furthermore, different regimes of diffusion must exist as there are solid/liquid interfaces and porous electrode structure. Nevertheless, in an electrode that does not undergo severe pulverization (e.g. an intercalation electrode), L is a fixed quantity throughout the experiment. Variation in L ¨ a parameter required to relate the rate of relaxation to the diffusion ¨ causes values of Du to vary significantly between reports even for the same material. Thus, while a physically meaningful diffusion coefficient may not be extracted, a relative measure of diffusion is readily obtained. For this reason, we use an extracted proxy for lithium diffusion (Du=L-2, Fig. 12), which removes the uncertainty in L and enables self-consistent analysis of a single electrode and electrodes prepared under identical conditions. The addition of quantitative information from another method, e.g., NMR spectroscopy, allows us to calibrate relative changes in Li kinetics to quantitative diffusion values throughout a range of lithiation.
As shown in Fig.12, in Nb16W5055, the fastest diffusion is observed from the dilute limit to Li45(5)Nbi6W5055, dropping by two orders-of magnitude in the low voltage window where more than 1 Li/TM is incorporated. The GITT data indicates that the 2nd electrochemical region of Nb16W5055 is broader than typically observed for a two-phase reaction but the observed discontinuity in the Du=L-2 values in this region suggests that it is approaching two-phase behavior. The average diffusion coefficient in Nb18W16093 is similar to that of Nb16W5055. The bronze also displays discontinuities at 2.1, 1.85, and 1.7 V.
In both phases, the low voltage region ¨ below 1.25 V, well over 1 Li/TM ¨ is characterized by an increasing overpotential and suppressed kinetics.

Anode Material Ragone Plot Anode material Ragone plot: the energy density of a cathode material is the product of capacity (Q) and voltage (V); however, this product does not work when comparing anode materials, where energy and voltage have an inverse relationship. In the calculation of the anode material Ragone plot in Fig. 13, the energy (E) is computed based on the voltage difference versus a 4.0 V cathode. Thus, normalized to the anode, Eanode =
0/cathodeVanoderQanode=
When compared strictly on the basis of theoretical 1.0 Li+/TM reaction and crystallographic density of the active material, titania, niobia, and graphite all display theoretical charge densities of greater than 800 A=h=L-1 (Fig. 14). Once experimental capacities and tap density are considered (Fig. 13A), the bulk, unoptimized niobium tungsten oxides presented here maintain volumetric charge densities of greater than 500 A=h=L-lat 10 and up to 400 A=h=L-1 at 20 C, volumetric performance that even the most optimised versions of TiO2, Nb2O5, LTO
cannot achieve. This is not to say that the compounds presented cannot be improved by methods such as nanostructuring, calendaring, or carbon-coating as demonstrated by e.g.
Sun et al. with holey-graphene scaffolds but to prove that large micrometer particles can be used for high-rate electrodes and illustrate that nanosizing is not always the most appropriate strategy to improve performance. This is evident in a Ragone plot (Fig. 13B), which shows the higher energy densities of the new bulk niobium tungsten oxides, as compared to state-of-the-art high-rate anode materials and to graphite.
Commercial Materials - Half-Cell Tests Additionally, in order to test the suitability of the niobium tungsten oxides as high-rate anode materials, the commercially-available high-rate cathode materials NM0622 (LiNio6Mno2000202; Targray), lithium iron phosphate (LiFePO4; Johnson Matthey) and LiMn204 (MTI Corp) were purchased. These commercial materials were first characterised in half-cell geometry against Li metal. Electrochemical measurements were conducted using a stainless steel 2032-coin cell and glass microfiber separator in the same manner as for Nb16W5055 and Nb18W16093 described above. The commercial cathode material, conductive carbon (Li-250 carbon; Deka Chemicals) and PVDF were ground together in the same manner as described above to prepare an 80/10/10 electrode (comprising 80 wt%
active material, 10 wt% carbon and 10wt% polymer) which served as the cathode against a Li metal disk anode in half-cell geometry. The electrolyte was 150 pL LP30. No additives were used.
NM0622 showed an average voltage of 3.8 V and a practical capacity of 175 mA=h=g-1 under these conditions (Fig. 17A). LiFePat showed an average voltage of 3.4 V and a practical capacity of 165 mA=h=g-1 (Fig. 17B), and LiMn204 showed an average voltage of 4.0 V and a practical capacity of 120 mA=h=g-1 (Fig. 170).

Electrode Optimisation - Nbis W5 0 5 5 In order to optimise the performance of the Nb16W5055 electrode, a series of electrodes were made to the specifications set out in Table 3, below. Electrochemical characterisation was conducting using a stainless steel 2032 coin cell and glass microfiber separator as described above. A Li metal disk was used as anode in half-cell geometry. The electrolyte was 150 pL
LP30. No additives were used.
Table 3 - Electrode Optimisation Entry Active Separator Carbon Binder Calendaring Ref 80% Nb16W5055 Glass microfiber 10% Super P 10% PVDF No 1 80% Nb16W5055 Polypropylenel 10% Super P 10% PVDF No 4% SRB2 2 80% Nb16W5055 Glass microfiber 10% Super P No 1% CMC3 3 80% Nb16W5055 Glass microfiber 15% Super P 5% PVDF No 4 80% Nb16W5055 Glass microfiber 8`)/0 Super P10% PVDF No 2`)/0 CNT4 80% Nb16W5055 Glass microfiber 10% Super P 10% PVDF Yes 1Celgard; 2Styrene-butadiene rubber (Zeon); 3Carboxymethyl cellulose (Sigma Aldrich); 4Carbon nanotubes (Sigma Aldrich) Bulk rate performance was shown to be improved where 5 wt% PVDF or 4 wt% SRB
and 1 w% CMC as binder (Fig. 18). Calandering also consistently improved electrode performance.
Full Cell Operation with Commercial Electrode Materials To test the suitability of the niobium tungsten oxides as high-rate anode materials, full cells were produced using the commercially-available high-rate cathode materials NM0622, LiFePat and LiMn204. Electrochemical measurements were conducted using a stainless steel 2032-coin cell and glass microfiber separator in the same manner as for Nb16W5055 and Nb18W16093 described above. The commercial cathode material, Li-250 carbon and PVDF were ground together as described above to prepare an 80/10/10 electrode (comprising 80 wt% active material, 10 wt% carbon and 10 wt% polymer) which served as cathode. The Nb16W5055, Li-250 carbon and PVDF were ground together to prepare an 80/10/10 electrode (comprising 80 wt% active material, 10 wt% carbon and 10 wt% polymer) which served as anode. When the cathode comprised NM0622, the anode comprised Nb16W5055, Li-250 carbon and PVDF in a 80/15/5 ratio. The electrolyte in all cases was 150 pL LP30. No additives were used. The capacity ratio of the anode and cathode was 1:1. For full cell balancing, the theoretical capacity of NM0622 was taken to be 175 mA=h=g-1.
The full cells were evaluated between 1.0 and 3.0 V. The initial change/discharge curves of the full cells with LiFePat and LiMn204 cathodes are shown in Fig. 19A and 19B, respectively. At a low rate of 0/5, the full cell against LiMn204 showed a capacity of 120 mA=h=g-1, close to the practical capacity of the cathode. With LiFePat as cathode, a capacity of 140 mA=h=g-1 was measured. With NM0622 as cathode, a high capacity of 165 mA=h=g-1 (Fig. 190). Capacities are quoted based on the mass of the active cathode material.
The rate performance of the NMC622 full cell was evaluated in a range of current densities from 0/5 to 200. The NM0622 full cell maintained a capacity of 125 mA=h=g-1 at 200, greater than 75% capacity retention relative to the capacity at 0/5 (Fig 19D).
To test longer term cycling, the NM0622 full cell was cycled at 100 charge and 100 discharge rates for 300 cycles. Under these conditions, a capacity of 120 mA=h=g-1 was observed after 300 cycles, corresponding to greater than 80% capacity retention (Fig. 19E).
At lower rates, a very high capacity retention of over 98% was achieved for 100 cycles at 10 charge and 10 discharge (Fig 19F).
Investigation of Electrode Degradation In order to investigate the cause of capacity loss, a full cell using a Nb16W5055 anode and NM0622 cathode as described above was cycled for 500 cycles at 10 change and discharge. A 71.1% capacity retention was observed (Fig. 20A). The cell was disassembled and the cathode and anode reassembled into a cell against a Li metal electrode in half-cell geometry. As shown in Fig. 20B the extracted NM0622 electrode showed a capacity of 0.48 mAh. The initial capacity of an NM0622 half-cell in this configuration was 0.72 mAh.
Thus, the NM0622 electrode showed a capacity retention of 67% (a capacity loss of 33%).
In contrast, the extracted Nb16W5055 electrode showed a capacity of 0.62 mAh against an initial capacity of 0.73 mAh in this configuration (Fig. 200). This corresponds to a capacity retention of 85% (a capacity loss of 15%). Thus, more than half the capacity loss observed in the full cell comprising the Nb16W5055 anode and NM0622 cathode arose from degradation of the NM0622 cathode. This indicates that the Nb16W5055 material is particularly a resilient electrode material.
Mixtures of Nb16W5055 and LTO as anode Additional experiments were carried out to test the use of a mixture of Nb16W5055 and LTO
as electrode material. Electrodes comprising three different ratios of Nb16W5055to LTO were produced and measured against an Li metal anode in the same manner as for Nb16W5055 and Nb18W16093 described above. The galvanostatic charge-discharge curves are shown in Fig 21A normalised to gravimetric capacity. The average voltage of 1.55 V is close to that of pure LTO (Fig. 5A). In a ratio of 7:3 (Nbi6W5055:LTO), a gravimetric capacity of 225 mA=h=g-1 was observed at 0/5, while 125 mA=h=g-1 was seen at 200 (Fig.
21B). For 3:7 (Nbi6W5055:LTO), a gravimetric capacity of 190 mA=h=g-1 was observed at 0/5, while 130 mA=h=g-1 was seen at 200 (Fig 21B). To test longer term cycling, the cell was cycled at 100 charge and 100 discharge rates for 500 cycles. Under these conditions, a capacity of 150 mA=h=g-1 was observed, showing greater than 93% capacity retention (Fig.
210).
A full cell comprising a 3:7 (Nbi6W5055:LTO) anode and an NM0622 cathode was prepared in a stainless steel 2032-coin cell with glass microfiber separator in the same manner as for Nb16W5055 and Nb18W16093 described above. The Nb16W5055, LTO, Super P carbon and PVDF were ground together to prepare an 80/15/5 active material/carbon/polymer anode.
The NM0622, Li250 carbon and PVD were ground together as described above to prepare an 80/10/10 active material/carbon/polymer electrode which served as cathode.
The electrolyte was 150 pL LP30. No additives were used The full cell was evaluated between 1.0 and 3.25 V, as shown in Fig. 22A. At a low rate of 0/5 a capacity of 200 mA=h=g-1 was observed. The average voltage was 2.25V.
The rate performance of the full cell was evaluated in a range of current densities from 0/5 to 200.
The full cell maintained a capacity of 160 mA=h=g-1 at 200, greater than 78%
capacity retention relative to the capacity at 0/5 (Fig 22B).
Electrochemical Characterisation of Nb2Mo3014 Electrochemical characterisation of Nb2Mo3014 was conducted in the same manner as for Nb16W5055 and Nb18W16093described above, using a stainless steel 2032-coin cell (Cambridge Energy Solutions) with a conical spring, two 0.5 mm stainless steel spacer disks, a plastic gasket, and a glass microfiber separator (Whatman). The metal oxide and conductive carbon (Super P, TIMCAL) were ground by hand in an agate mortar and pestle in an 8:1 mass ratio. This powder was ground in a 9:1 mass ratio with poly(vinylidene difluoride) (PVDF, Kynar) dispersed in N-methyl pyrrolidone (NMP, Sigma-Aldrich, anhydrous, 99.5%). This metal oxide/carbon/polymer electrode served as the cathode against a Li metal disk (LTS Research, 99.95%) anode in half-cell geometry.
The electrolyte was 1 M LiPF6 dissolved in 1:1 v/v ethylene carbonate/dimethyl carbonate (EC/DMC, Sigma-Aldrich, battery grade). No additives were used. Electrochemistry was performed in a temperature-controlled room at 293 K. A Biologic galvanostat/potentiostat with EC-Lab software was used to perform the electrochemical measurements.
At 0/20 it is possible to maintain a gravimetric capacity of ca. 200 mA=h=g-1 (Fig. 15).
Nb2Mo3014 displays an average voltage around 2.0 V. Thus, Nb2Mo3014 may be used in a voltage window of, for example 3.0 to 1.4 V, or 3.0 to 1.8 V, and still provide a high capacity at a high rate whilst avoiding or minimizing reaction with the electrolyte.
This is advantageous as many prospective solid electrolyte materials react with low voltage anodes and this could be mitigated using a Nb2Mo3014 anode.
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Claims (25)

Claims:

1. A method of charging and/or discharging an electrochemical cell at a C-rate of at least 5C, wherein the electrochemical cell has a working electrode comprising a niobium tungsten oxide and/or niobium molybdenum oxide.

2. The method of claim 1, wherein the method is a method of charging and/or discharging an electrochemical cell at a C-rate of at least 10C, 15C, 20C, 25C, 30C, 35C, 40C, 50C, 60C or 80C.

3. The method of claim 1 or 2, wherein the method is a method of charging and/or discharging an electrochemical cell at a current density of at least 750 mkg-1, preferably at least 800 mkg-1, 850 mkg-1, 900 mkg-1, 950 mkg-1, 1000 mkg-1, 1050 mkg-1, 1100 mkg-1, 1200 mkg-1 or 1300 mkg-1.

4. The method of any preceding claim, wherein the electrochemical cell has a working electrode comprising a niobium tungsten oxide.

5. The method of claim 4, wherein the ratio of Nb2O5 to W03 in the working electrode is from 6:1 to 1:15, preferably from 8:5 to 11:20.

6. The method of claim 4 or 5, wherein the working electrode comprises a niobium tungsten oxide selected from Nb12W033, Nb26W4077, Nb14W3044, Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093, Nb22W200115, Nb8W9047, Nb54W820381, Nb20W310143, Nb4W7031, or Nb2W15050, or combinations thereof.

7. The method of any of claims 4 to 6, wherein the working electrode comprises a mixture of a niobium tungsten oxide and an additional active material, preferably wherein the additional active material is Li4Ti5012.

8. The method of any of claims 1 to 3, wherein the electrochemical cell has a working electrode comprising a niobium molybdenum oxide.

9. The method of claim 8, wherein the ratio of Nb2O5 to MoO3 in the electrode is from 6:1 to 1:3.

10. The method of claim 8 or 9, wherein the working electrode comprises a niobium molybdenum oxide selected from Nb2Mo3014, Nbi4Mo3044 or Nbi2M0044.

11. The method of any preceding claim, wherein the method comprises a cycle of charging and discharging, or discharging and charging the electrochemical cell.

12. The method of claim 11, wherein the method comprises 2 cycles or more, 5 cycles or more, 10 cycles or more, 50 cycles or more, 100 cycles or more, 500 cycles or more, 1,000 cycles or more, or 2,000 cycles or more.

13. An electrode comprising niobium tungsten oxide, wherein the ratio of Nb2O5 to W03 in the electrode is from 8:5 to 11:20.

14. The electrode of claim 13, wherein the electrode comprises Nb16W5055, Nb18W8069, Nb2W08, Nb18W16093, or Nb22W200115, or combinations thereof

15. The electrode of claim 13 or 14, wherein the electrode comprises Nb16W5055 or Nb18W16093

16. The electrode of any of claims 13 to 15, wherein the electrode comprises a mixture of a niobium tungsten oxide and an additional active material, preferably wherein the additional active material is Li4Ti5012.

17. An electrode comprising niobium molybdenum oxide, wherein the ratio of Nb2O5 to MoO3 in the electrode is from 6:1 to 1:3.

18. The electrode of claim 17, wherein the electrode comprises Nb2Mo3014, Nbi4M03044 or Nbi2Mo044

19. The electrode of claim 17 or 18, wherein the electrode comprises Nb2M03014.

20. The electrode of any of claims 13 to 16, wherein the electrode does not have a porous nor hierarchical structure, preferably wherein the electrode has a specific surface area of less than 100 m2.g-1.

21. The electrode of claims 13 to 16, wherein the electrode comprises a niobium tungsten oxide in particulate form, preferably wherein the niobium tungsten oxide particles have an average primary particle size of at least 1 pm.

22. An electrochemical cell comprising an electrode according to any one of claims 13 to 21.

23. A lithium ion battery comprising one or more electrochemical cells according to claim 22.

24. A vehicle comprising the electrochemical cell of claim 23.

25. Use of a working electrode comprising a niobium tungsten oxide and/or niobium molybdenum oxide in a high-rate electrochemical cell, wherein the electrochemical cell is charged or discharged at a C-rate of at least 5C, such as at least, 10C, 15C, 20C, 25C, 30C, 35C, 40C, 50C, 60C or 80C.