This invention relates to high capacity materials for batteries and processes for preparing such materials. More particularly, this invention relates to amorphous titanium oxide and vanadium oxide materials useful as components of electrodes for lithium-ion and sodium-ion batteries.
Limited energy resources and the growing demand to decrease greenhouse gas emissions have intensified research of carbon-free energy sources. Batteries that store high-energy densities will play a large role in implementation of green energy technologies and non-petroleum vehicular mobility. To date, rechargeable Li-ion batteries offer the highest energy density of any battery technology, and are expected to provide a solution for our future energy-storage requirements. Unfortunately, Li-ion batteries have a number of limitations, such as capacity loss over time during long-term cycling due to phase transitions leading to detrimental volume changes in the electrode materials. This can cause local atom rearrangements that block the diffusion of Li ions, leading to high over potentials and loss of capacity. In addition, Li-ion batteries that have been charged quickly can form dendritic Li deposition at the commercial graphite anode and can create a safety problem that in the worst scenario could cause thermal runaway, cell rupture and explosion. Use of chemically inert anode materials such as metal oxides with lithiation voltages positive of Li-deposition compared to carbon can address these issues and improve safety of Li-ion battery operation.
High-performance battery materials are critical for the development of new alternative energy storage systems. While Li-ion batteries are a mature technology for energy storage, disadvantages include cost, Li supply, safety, reliability and stability. Moreover, the electrolyte stability over time is additional major concern for long-term operation and advanced applications. Thus, the discovery, research and development of new transporting ions that can provide an alternative choice to Li batteries are essential for further advancement of energy storage materials. Sodium-based batteries are attractive due to the promise of low cost associated with the abundance of sodium, and enhanced stability of non-aqueous battery electrolytes due to the lower operating voltages. However, lower voltage leads to insufficient energy density, thus cathode materials for Na batteries must possess high-capacities. Since the ionic volume of sodium is almost twice that of lithium, unique crystalline structures have to be used to accommodate incorporation of large ions.
Titanium dioxide is one of the few metal oxide materials that intercalates Li ions at reasonably low voltage (approximately 1.2 V vs. Li/Li+) and is suitable as a battery anode material. The first attempts of using TiO2 for a durable and safe electrode material were focused on microcrystalline TiO2 materials such as rutile, anatase, and TiO2(B). These electrodes materials showed moderate specific capacities (e.g., maximum Li uptake of 0.5 Li/Ti for anatase and TiO2(B), and no activity for rutile) due to the limited room temperature reactivity and conductivity at microscale. Recently, the idea of using TiO2 electrodes has been revisited with the consideration that nanosize morphologies provide enhanced intercalation kinetics and large surface area associated with high accessibility of transporting ions. Reversible capacities with stoichiometries up to about approximately 0.5-0.7Li/Ti have been demonstrate; however, repetitive cycling caused loss of capacity independent of the crystalline modification. It was expected that all TiO2-based electrodes will have an intrinsic capacity limitation, because of a low number of crystallographic sites, and their electronically insulating structure. Both experimental and theoretical studies of intercalation of Li ions in crystalline polymorphs of TiO2 show that high lithium content can be obtained exclusively at elevated temperatures raising concerns from the application point of view.
Vanadium pentoxide (V2O5) has been intensively studied as the positive electrode (anode) material for lithium ion batteries. In previous studies, various fabrication methods were used: sputtering, thermal evaporation, thermal decomposition, electrophoretic deposition and many chemical routes, such as hydrothermal synthesis, and sol-gel method. It has been reported that chemical composition, crystal structure and crystallinity of V2O5 may have pivotal roles in lithium ion intercalation capacity and cycling stability. To date, the practical application of vanadium oxides in lithium ion batteries was still limited due to the poor cyclic stability and undesirable phase transitions to inactive materials.
In contrast to lithium batteries, a report of Liu et al. considered employment of vanadium oxide by insertion/deinsertion of sodium-ion into NaV6O15 nanorods. Even though the morphology of the reported material could be retained, the initial discharge capacity of 142 mAh/g substantially decreased by cycling at higher current densities, which led to poor overall performance. In order to explore full potential in utilization of nanostructured V2O5 electrodes for sodium batteries a detailed fundamental insight is necessary.
There is an ongoing need for new, more efficient, electrode materials for lithium-ion and sodium-ion batteries. The present invention addresses this need.
The present invention provides a nanostructured metal oxide material for use as a component of an electrode of a lithium-ion or sodium-ion battery. The material comprises a nanostructured titanium oxide or vanadium oxide film on a metal foil substrate. The film is produced by depositing or forming a nanostructured material selected from titanium dioxide and vanadium oxide on the surface of the substrate, and then charging and discharging the material in an electrochemical cell from a high voltage in the range of about 2.8 to 3.8 V, to a low voltage in the range of about 0.8 to 1.4 V over a period of about 1/30 of an hour or less.
In one embodiment, the nanostructured metal oxide material of the present invention comprises a film of titanium dioxide nanotubes. Preferably, the titanium dioxide nanotubes comprise densely packed TiO2 nanotubes oriented perpendicular to the surface of the metal foil substrate. In one form of this embodiment, the substrate is a titanium foil and the densely packed TiO2 nanotubes are amorphous and are produced by electrochemical anodization of a surface of the titanium foil, and subsequently drying the film to remove water therefrom (e.g., by heating at a temperature in excess of 100° C.). The densely packed TiO2 nanotubes can have a wall thickness of about 8 to 25 nm and an outer tubular diameter of about 50 to 150 nm. In one preferred form, the nanotubes have a wall thickness of about 8 to 12 nm (e.g., about 10 nm) and an outer tubular diameter of about 50 to 70 nm (e.g., about 65 nm). In another form, the densely packed TiO2 nanotubes have a wall thickness of about 18 to 25 nm and an outer tubular diameter of about 100 to 150 nm.
In another preferred form of this embodiment the titanium dioxide comprises nanostructured crystalline TiO2 produced by electrochemical anodization of a surface of the titanium foil to form amorphous nanotubes, subsequently drying the film to remove water, and then charging and discharging the amorphous film in an electrochemical cell from a high voltage to a low voltage over a short period of time. For example, charging and discharging from a high voltage in the range of about 2.6 to 3 V (e.g., about 2.8 to 2.9 V), to a low voltage in the range of about 0.7 to 1 V (e.g., about 0.8 to 0.9 V), over a period of about 1/30 of an hour or less.
In another preferred embodiment, the nanostructured metal oxide material comprises a film of bilayered V2O5. In one preferred form, the bilayered V2O5 is amorphous and the layers thereof have an interlayer spacing of greater than about 12 Å. In another preferred form, the bilayered V2O5 is amorphous and is produced by electrochemical deposition from a VO2+ salt solution (e.g., aqueous VOSO4) onto the metal foil substrate, and drying deposited film to remove water therefrom. In another preferred form, the bilayered V2O5 comprises nanostructured crystalline bilayered V2O5 produced by electrochemical deposition from a VO2+ salt solution onto the metal foil substrate to form an amorphous bilayered V2O5 film, drying film, and then charging and discharging the dried film in an electrochemical cell from a high voltage in the range of about 3.3 to 3.8 V (e.g., about 3.5 V), to a low voltage in the range of about 1.4 to 1.6 V (e.g., about 1.5 V), over a period of about 1/30 of an hour or less.
The metal foil substrate can comprise any metal suitable for use as a current collector for an electrode in lithium-ion or sodium-ion electrochemical cell or battery. Preferably, when the metal oxide material comprises titanium oxide, the substrate comprises titanium. When the metal oxide material comprises vanadium oxide, the substrate preferably comprises nickel or stainless steel.
In one aspect, the present invention provides a lithium-ion electrochemical cell comprising a cathode, an anode, and a nonaqueous lithium-containing electrolyte therebetween. In one preferred form, the anode comprises a nanostructured titanium oxide material of the invention as described herein. If desired, the anode can comprise a carbon material or other suitable components in addition to the titanium oxide material. The cathode in this embodiment can comprise a vanadium oxide material as described herein, or can comprise any other cathode material suitable for use in electrochemical cells, such cathode materials being well known in the battery art.
In another preferred form of the lithium-ion electrochemical cell, the cathode comprises a nanostructured vanadium oxide material of the invention as described herein. The anode in this form can comprise a titanium oxide material as described herein, or can comprise any other anode material suitable for use in electrochemical cells, such anode materials being well known in the battery art.
The electrolyte in the lithium-ion electrochemical cells and batteries can comprise any lithium-ion containing electrolyte material that is suitable for use in lithium-ion electrochemical cells and batteries. Such electrolyte materials also are well known in the battery art.
The present invention also provides a sodium-ion electrochemical cell comprising a cathode, an anode, and a nonaqueous sodium-containing electrolyte therebetween. In one preferred form, the anode comprises a nanostructured titanium oxide material of the invention as described herein. If desired, the anode can comprise a carbon material or any other suitable component in addition to the titanium oxide material. The cathode in this embodiment can comprise a vanadium oxide material as described herein, or can comprise any other cathode material suitable for use in electrochemical cells, such cathode materials being well known in the battery art.
In another preferred form of the sodium-ion electrochemical cell, the cathode comprises a nanostructured vanadium oxide material of the invention as described herein. The anode in this form can comprise a titanium oxide material as described herein, or can comprise any other anode material suitable for use in electrochemical cells, such anode materials being well known in the battery art.
The electrolyte in the sodium-ion electrochemical cells and batteries can comprise any sodium-ion containing electrolyte material that is suitable for use in sodium-ion electrochemical cells and batteries. Such electrolyte materials also are well known in the battery art.
The electrochemical cells of the present invention can be assembled in to a battery by electrochemically linking the cells (e.g., in series or parallel or both), if desired. In addition, the batteries and electrochemical cells can include other components besides the cathode, anode and electrolyte, such as a housing, porous separators, binders, and the like, as is well known in the battery art.
The present invention provides an electrochemically driven transformation of amorphous TiO2 nanotubes for Li-ion battery anodes into a face-centered-cubic Li2Ti2O4 crystalline phase that self-improves as the cycling proceeds. The intercalation and deintercalation processes of Li ions in the electrochemically-grown TiO2 nanotubes provide spontaneous development of a long-range order in amorphous TiO2 in the presence of high concentration of Li ions (>75%). Reversible intercalation and preservation of the resultant cubic structure during cycling is maintained, and the electrode shows superior stability for more than 600 cycles. Moreover, the adopted cubic structure supports very fast (26 s) charging with good retention of capacity. A full lithium-ion cell with a LiNi0.5Mn1.5O4 cathode provided an average 2.8 V which shows near theoretical reversible capacity of 310 mAh/g, corresponding to a Li1.84Ti2O4 stoichiometry. The observed capacity is the highest among all reported values for any form of TiO2 anodes to date. In addition, in the same manner we obtained the first reversible metal oxide anode for sodium-ion batteries that also improves with cycling. The simplicity of the electrode design and the use of fast electrochemical cycling foster the ability for these materials to maximize their capacity in operando, opening a new avenue for synthesis of safe and durable high power/high capacity batteries.
The vanadium oxide embodiments of this invention are particularly suited for use in sodium-ion cells and batteries. The approach to achieving sodium intercalation is to use materials that have adjustable d-spacing and two-dimensional layered structure that can accommodate large volume changes. Furthermore, to facilitate reversible insertion of sodium ions, a host lattice that has short range order would be preferred to crystalline structures due to the conservation of low-entropic energy associated with ordering of intercalated atoms. The present invention provides, inter alia, electrochemically grown nanostructured bilayered vanadium pentoxide as a highly efficient 3 V cathode material for rechargeable sodium batteries. With capacity of 250 mAh/g, excellent rate capability and life cycle, as well as high energy density of 760 Wh/kg, this material can be used in advanced energy storage applications.
The present invention provides new, more efficient electrode materials for lithium-ion and sodium ion batteries. In one embodiment, the present invention provides anodes for lithium-ion or sodium-ion batteries comprising a nanostructured amorphous titanium or vanadium oxide on a metallic substrate.
In one preferred embodiment the electrode comprises titanium dioxide nanotubes on a titanium metal (e.g., titanium foil) support. In another preferred embodiment, the electrode material comprises a bilayered V2O5 film on a metal (e.g., nickel) substrate.
Certain aspects and features of the present invention are illustrated by the following discussion, which is not to be considered as limiting.
Herein, we explore a new approach of creating high capacity/high power electrodes starting from an amorphous, disordered nanoscale material. Recently, it has been shown that increased concentration of interfacial regions in amorphous materials may form percolation pathways for fast diffusion of ions. Our approach to forming new improved anodes is to take advantage of enhanced diffusion in amorphous materials. This allows for accumulation of a high local concentration of intercalated Li-ions at the reduced transition metal centers (i.e. Ti3+). Ordering of densely packed materials henceforth would result in the formation of a crystalline structure that accommodates the highest concentration of Li ions, ensuring the highest possible electrode capacity.
We synthesized densely packed, vertically oriented amorphous TiO2 nanotubes (TiO2NTs) using electrochemical anodization of Ti foil. Electrochemical synthesis is a method of choice for preparation of nanoscale architectures that require electronic conductivity, and it eliminates the need for conductive carbon additives and binders typically used in electrodes that can alter their long-term stability. As the potential drives the electrons that are used to create reactive species, the chemical reaction propagates to the extent that electrons can penetrate the structure, fostering electrical connectivity. The ease of controlling the kinetic parameters of synthesis by simple manipulation of voltage and current density offers a great advantage in controlling size and shape of formed nanostructures. In addition, nanostructures have direct and electronic connection to a metallic current collector (e.g. Ti foil). As-synthesized TiO2NTs are amorphous, as determined by X-ray diffraction (XRD).
When amorphous TiO2NTs were used as electrodes in a lithium half-cell, a monotonic linear decreasing voltage is observed during the first discharge (Li+ insertion), followed by a characteristic plateau at approximately 1.1 V vs. Li/Li+. The existence of the plateau indicates a phase transition, implying that injected electrons do not contribute to decrease of the potential difference between electrodes but instead are consumed in the change of the structure of the materials with enhanced capacity for Li-ions (
Further charge/discharge profiles do not show evidence of capacity loss or Coulombic inefficiency, and Li ions reversibly intercalate/deintercalate into TiO2NTs (
It is surprising that the amorphous metal oxide electrode materials of the present invention exhibit high capacity on cycling, when conventional wisdom indicates that their collective electron orbitals are not expected to participate in conduction of charge within the electrode material. It is generally accepted that a large fraction of amorphous materials usually possess “dead” volume that adds weight and lowers the energy density of the battery.
Our observation of high reversible capacity in amorphous nanotube electrodes that exceeds the theoretically predicted values for any of the TiO2 polymorphs likely is the consequence of a different intercalation mechanism, different structure, or the presence of different intercalation sites in nanotube electrodes compared to traditional bulk electrodes. The rate capability study confirms superior diffusion of Li ions in these electrodes compared to anatase TiO2NT electrode obtained by annealing the same TiO2NT at 450° C. (
We used a combination of experimental and computational techniques to understand the atomic-scale features of this transformation. XRD synchrotron measurements were employed to investigate phase transition of the amorphous TiO2NTs during the process of cycling. Due to the high brilliance and the phase contrast, synchrotron XRD offers exceptionally high resolution in reciprocal space and sufficient sensitivity to probe even single layer atoms and therefore is ideal for investigation of nanoscale materials. We found that cycling amorphous TiO2NTs repeatedly above approximately 1.1 V, (the potential before phase transition occurs) produces materials with no significant improvement of crystallinity (
The cell parameter of the discharged unit cell of 8.27 Å, is somewhat smaller than the one previously reported for chemically prepared bulk Li2Ti2O4 (a=8.376 Å) of the same symmetry, suggesting a good balance of electrostatic forces. Our geometric optimization using density functional theory (DFT) calculations gives an optimized lattice constant of 8.27 Å (
Molecular dynamics (MD) simulations suggest that atomic diffusivity in the lithiated amorphous TiO2 structure depends strongly on the lithium content. The calculated diffusivity of Ti and O ions for 25% Li loading was significantly lower than that for 75% Li loading in the case of amorphous TiO2. This kinetic fluidity in amorphous TiO2 suggests that crystallization to the thermodynamically stable cubic phase of similar composition should be possible during initial discharge at longer timescales than are accessible to MD simulations. Once the cubic structure forms, atomic motion in the case of Ti and O is confined to localized vibrations, but the lithium mobility is very high.
We found that diffusion coefficients of Ti and O in amorphous TiO2 having low concentrations of Li are fairly small, comparable to those in other titania polymorphs. This suggests that introducing low amount of Li should not produce any large-scale phase transformations. However, at high lithiation level (>75%), atomic diffusion of Ti and O becomes significant, suggesting facile rearrangement of atoms in the structure and leading to phase transformation. This rapid kinetic diffusion, in turn, suggests that crystallization to thermodynamically stable phases of similar composition should be possible during initial discharge of the TiO2 electrodes. Our analysis of the formation energies also indicates that the cubic structure is energetically more favorable than amorphous titania with the same lithium loading (
In order to further understand the evolution of crystalline structure we evaluate the dynamics of the phase transformation from amorphous to crystalline material occurring at high Li loadings, by performing MD simulations for the 100% Li loaded amorphous TiO2 composition. These results indicate evolution of long-range order in highly lithiated TiO2, as revealed by the formation of regularly ordered layers of oxygen. These well-defined layers of oxygen are separated by layers of mixed metal (Ti and Li) atoms that do not show short-range order but are randomly distributed between ordered oxygen arrays. We noted that this layered formation resembles the cubic phase observed in the experiments. The entire structure has long-range order while within the layers, disorder exists. Further simulations performed up to 6 nanoseconds (ns) do not show increase in short-range ordering, suggesting that the structure should possess stable long-range order but that short-range ordering is kinetically inhibited. It should be noted that the MD simulations also indicated that for Li concentrations much lower than 100%, the lithiated amorphous oxide maintains its disordered structure for the same time and temperature conditions (1400 and 1200 K), indicating that the kinetics of this transformation is strongly correlated to the Li:TiO2 stoichiometry.
We believe that existence of long-range order in the absence of short-range order within layers (chemical disorder) is an important factor in the thermodynamic stability of the de-lithiated structure. The fact that, in this structure, all layers continue to contain metal atoms, even in the charged state, provides stability and prevents collapsing of the delithiated structure. Accordingly, our DFT calculations also show that the optimized structure for the fully de-lithiated titania preserves cubic symmetry.
Interestingly, previous reports of bulk fcc Li2Ti2O4 suggest that this structure cannot be employed for reversible cycling. Chemically synthesized bulk cubic Li2Ti2O4 can be oxidized to Li0.1TiO2, but removal of Li results in a defective disordered cubic structure that is virtually unreactive for further Li intercalation. On the other hand, nanoscale architectures obtained in this work by self-assembly of amorphous samples show entirely reversible Li insertion/extraction, demonstrating the existence of a solid solution mechanism and good coulombic efficiencies, and confirming facile diffusion of Li ions (
To understand how the diffusion characteristics of lithium in the self-improved cubic structure compare with those in other titania structures, MD simulations of Li ion diffusion in a variety of highly lithiated crystalline and amorphous titania structures were performed, including amorphous and cubic Li2Ti2O4, as well as anatase TiO2. Comparison of the trajectories suggested that Li ion transport in fully lithiated samples follows cubic (100% Li)>amorphous (100% Li)>anatase (50% Li), which is consistent with the high reversible capacity observed for the self-improved structure as compared to other titania polymorphs. In fact, calculation of Li ion diffusion in the cubic Li2Ti2O4 reveals a remarkably low diffusion activation barrier (257 meV—
To demonstrate the practical significance of this material in batteries, the TiO2NT (cubic form) anode was coupled with a 5 V spinel (LiNi0.5Mn1.5O4) cathode for testing in a Li-ion full cell configuration. The 5 V spinel was chosen as the cathode in order to maximize the cell voltage, and the cell was constructed such that the specific capacity is limited by the mass of anode material. The TiO2NT/LiNi0.5Mn1.5O4 cell shows an average cell voltage of 2.8 V and exceptionally good specific capacity that improves as the cycling proceeds. The success of this Li-ion cell made by TiO2NT anode demonstrates that it maintained the advantage of a Li-ion battery (large output potential) while it moved the operating potential at the anode to a higher window, thus avoiding possible safety hazards from Li plating. The discharge capacity of the cell improves with cycles and reaches approximately 310 mAh/g in less than 25 cycles (C/15 rate) (
The success of the synthetic approach of this invention for Li suggests that the use of amorphous electrochemically synthesized 1D nanostructures for creating rechargeable batteries that utilize transporting ions other than Li, for example Na ions, thus presenting an unique opportunity to generate new classes of battery materials. Sodium is a cheap, nontoxic and abundant element that is uniformly distributed around the world and therefore would be ideal as transporting ion for alternative rechargeable batteries. However, to date, no low-voltage metal oxide anodes capable of operating with sodium ion at room temperature have been reported. The reason for this is likely the prohibitively large ionic radius of Na ion (1.02 Å) compared to the size of Li ion (0.76 Å), and therefore insertion of Na ion requires large distortion of the metal oxide lattice which would require unacceptably elevated temperatures not realistic for operation of batteries.
We applied the same method as for Li, i.e., the in situ electrochemically driven self-assembling approach at room temperature, in the presence of large concentration of Na ion. We find that, under electrochemical cycling conditions, narrow amorphous TiO2NTs do not incorporate sodium (e.g. 65 nm O.D. with 10 nm wall thickness). However, when larger tubes having 120 nm O.D. and 20 nm wall thickness are used as a host material, we again observe self-improving phenomenon, but in this case upon cycling at a slow rate (0.05 A/g,
The question that naturally arises is why Na ions do not insert into the smaller (65 nm O.D.) tube while Li ions do, and why the capacity in Na cells self-improves only under slow rate cycling while Li cell improves upon fast cycling. One of the possible reasons is relatively strong adsorption of Li ions on the TiO2 surface in aprotic electrolyte solutions, while no adsorption was found for Na ions under the same conditions. This in turn enables a high local concentration of Li ions even in a small NT diameter, while Na ions remain mainly outside the NT in the bulk electrolyte. Upon injecting electrons into NT, Li ions from the surface are able to insert rapidly into the structure and induce phase transformation to high capacity structures that improves the performance of the cell even at high cycling rate (approximately 7 A/g). On the other hand, Na ions first need to diffuse through the electrolyte, adsorb on the surface of TiO2NTs, and then insert into the TiO2NTs host material. In the larger NTs, however, a larger amount of electrolyte (and therefore Na ions) are trapped within the NT electrode compartment, enabling larger flux of Na ions upon discharge. As accumulation of Na ions at the electrode surface is slower compared to Li ions, capacity self-improvement of the TiO2NT should occur at a slower rate. Indeed we observe Na insertion at approximately 140 times slower rate of cycling (approximately 0.05 A/g) compared to Li ion. The same arguments also account for the different mechanism of cycling in Li and Na cells. The Li-ion cells operate via a diffusion mechanism at high potentials (2.4-1.8 V) where a small driving force is sufficient to insert adsorbed ions into the TiO2 matrix. On the other hand, Na-ion electrodes at high potentials operate under a pseudocapacitive mechanism. At relatively negative potentials, a pseudocapacitative mechanism converts into diffusion mechanism (
Surprisingly, the TiO2NT materials also are suitable as anode materials for a Na-ion battery that can operate at room temperature. The Na-ion cell was made by a TiO2NT anode and a Na1.0Li0.2Ni0.25Mn0.75O6 cathode. The cell shows an operation voltage of approximately 1.8 V and a discharge capacity of approximately 80 mAh/g (C/8) (
It is at the nanoscale that near theoretical capacity and high power electrodes can be achieved using simple self-organization processes. The electrostatic attraction of electrochemically-altered materials provides a strong driving-force for the diffusion of a large concentration of transporting ions into amorphous metal oxide frameworks. This consequently leads to ordering of the atomic building blocks, transporting ions and host metal octahedra into a crystalline array. Inducing crystallization of nanomaterials in operando (i.e., in situ in a battery during charging and discharging) allows realization of the highest possible electrode capacity by optimizing the balance of electrostatic forces. The present invention demonstrates that much higher capacities can be realized if the system is naturally allowed to choose and optimize its crystalline structure through a process of self-organization and self-improvement. The small diffusion length and large surface area of nanostructures also enable exceptionally fast charging leading to high power batteries. Electrochemically induced structural evolution into high capacity/high power electrodes provides a powerful modular approach to the design of improved battery materials with programmable physical and chemical properties.
TiO2 nanotubes were synthesized by electrochemical anodization. Pure titanium thin foil (0.0127 mm, 99.8%, Alfa Aesar) was cleaned by acetone following an isopropyl alcohol rinse before anodization. The back of the Ti foil was protected by nail polish to ensure uniform current distribution. The anodization was carried out in a two-electrode cell with Ti metal as the working electrode and a Pt mesh as the counter electrode under constant potentials (15-30 V) at room temperature using electrolytes of formamide with 0.8 wt % ammonium fluoride (Aldrich) and 5 vol % water. The as-anodized samples were ultrasonically cleaned in deionized (D.I.) water for 30 seconds. All amorphous TiO2NT samples were vacuum baked at 110° C. overnight before assembly in electrochemical cells. The crystallized TiO2NT samples were prepared by annealing as-prepared TiO2NT under O2 at 450° C. for 4 hours.
The LiNi0.5Mn1.5O4 spinel and Na1.0Li0.2Ni0.25Mn0.75Oδ-layered cathode materials were prepared by solid state reactions as follows: quantities of Na2CO3 and/or Li2CO3, and Ni0.25Mn0.75CO3 (prepared by co-precipitation) to achieve the desired stoichiometry were ground together in an agate mortar until visually homogenous. The mixture was initially fired in a muffle furnace at 550° C. for 12 h, reground, and then calcined at 850° C. for 12 h and allowed to slowly cool to ambient temperature. Structures were verified by powder XRD and the relative metals contents were measured by ICP-OES and found to be the target compositions within the error of the determination. Electrode films were cast from slurries in N-methyl-2-pyrrolidone containing the active material at a concentration of about 82 percent by weight (wt %), carbon black (4 wt %, CABOT XC72), graphite (4 wt %, TIMCAL SFG-6), and poly(vinylidene difluoride) (10 wt %; KYNAR KF 1120) using doctor blade or spin casting techniques.
Electrochemical Insertion/Extraction of Li+ and Na+.
Li half-cells were assembled in coin-type cells (HOHSEN 2032) with a Li metal foil as the negative electrode, microporous polyolefin separators (CELGARD 2325), and 1.2 M LiPF6 in ethylene carbonate/ethyl methyl carbonate (3:7 weight ratio) electrolyte (Tomiyama). Na half-cells were assembled in similar setup with a Na metal foil counter electrode, glass fiber separator (WHATMAN GF/F), and 1 M NaClO4 (Aldrich) in propylene carbonate electrolyte. For comparison, a traditional laminate electrode was made by mixing 84 wt % active material (anatase powder, Aldrich), 4 wt % graphite (TIMCAL SFG-6), 8 wt % poly(vinylidene difluoride) binder (KYNAR), and 4 wt % carbon black (Toka). Half-cells were cycled galvanostatically at varying currents between 2.5 and 0.9 V vs. Li/Li+ or 2.5 and 0.5 V vs. Na/Na+ respectively using an automated Maccor battery tester at ambient temperature. Li-ion and Na-ion full-cells were assembled in the same manner as half-cells with a LiNi0.5Mn1.5O4 cathode and a Na1.0Li0.2Ni0.25Mn0.75Oδ cathodes, respectively. Li-ion full-cells were cycled galvanostatically between 2 to 3.5 V. Na-ion full-cells were cycled galvanostatically between 1 to 2.6 V. Cyclic voltammograms of the cells were recorded in a SOLARTRON 1470E Potentiostat/Galvanostat. Electrodes removed from cells for analysis were thoroughly washed with dry dimethyl carbonate (Aldrich) and allowed to dry under inert atmosphere. All cell assembly and disassembly operations were performed in a He-filled dry glove box (oxygen level <2 ppm). The net weights of the TiO2 nanotube films were obtained by peeling off the nanotube film from Ti substrate using adhesives and checking by SEM to make sure no residual TiO2 nanotube is left on the substrate.
X-ray diffraction measurements were performed at beamline 13-ID-D of GSECARS at the Advanced Photon Source (APS) at Argonne National Laboratory. The X-ray beam (37 keV energy, corresponding to X-ray wavelength of λ=0.3344 Å) was focused to a 2 μm diameter spot with a Kirkpatrick-Baez mirror system. The distance and tilting of the MAR165-CCD detector were calibrated using a CeO2 standard. Charged TiO2NT samples were prepared by stripping nanotube films from Ti support onto KAPTON tape and sandwiching with additional KAPTON tape. Electrochemically lithiated TiO2NT samples were scratched-off and sealed inside a 3 mm-diameter hole in a piece of aluminum foil by sealing KAPTON sheet to the foil using epoxy. All procedures were carried out in a He atmosphere glove box. Simulations of XRD patterns were carried out using CRYSTALMAKER software (CrystalMaker Software, Ltd.).
Scanning Electron Microscopy (SEM) images were recorded with a JEOL JSM-7500F Field Emission SEM operating at 30 kV. High resolution electron transmission microscopy (HRTEM) images and electron diffraction (ED) were obtained using an FEI Tecnai F30 microscope equipped with a field emission gun operated at 300 kV. TEM samples were prepared by scratching cycled TiO2NT samples from Ti support onto a carbon-coated copper TEM grid (ultrathin carbon film on a perforated carbon support film, 400 mesh, Ted Pella Inc.).
MD simulations were performed using the DLPOLY MD package and electronic structure calculations were within Vienna ab-initio simulation package (VASP). The MD simulations utilized the shell potential model in which the polarizable ion consists of two particles—core and shell—that share the ion's charge and are connected via a spring constant. The atoms were treated as point particles, and interact via long-range Coulomb forces and short-range interactions. The short-range interactions were represented by the Buckingham potential, which is described by parameterized functions fitted to reproduce the structure and energetics of Li—Ti—O system. In all MD simulations, a system size of 4320 atoms was used. The calculations spanned a temperature range of 850 K-1400 K, and statistics typically were collected from 1 ns simulations with a time step of 0.2 femtoseconds (fs). DFT calculations were performed using GGA-PBE. The cubic structure was made of 64 atoms, while the amorphous cell was constructed using 96 atoms. The initial structure of the amorphous cell for DFT calculations was obtained from the equilibrated configurations generated from the MD simulations. At least three different amorphous configurations were simulated to ensure that the results were not biased by the initial starting configuration. For all the systems, the cell shape was allowed to change, and ions were allowed to relax. The calculations were performed using 550 eV energy cut-off and 5×5×5 k-point sampling.
X-ray spectroscopy measurements were performed at the PNC/XSD bending magnet beamline (20-BM-B) of the APS at Argonne National Laboratory. Measurements at the Ti K-edge were performed under transmission mode using gas ionization chambers to monitor the incident and transmitted X-ray intensities. A third ionization chamber was used in conjunction with a Ti-foil standard to provide internal calibration for the alignment of the edge positions. The incident beam was monochromatized using a Si (111) double crystal fixed exit monochromator. Harmonic rejection was accomplished using a Rhodium coated mirror. The charged samples were prepared by stripping NT films onto KAPTON tape. The discharged samples were stripped onto KAPTON tape in a dry glove box under a helium atmosphere and attached to a He-filled, sealed holder. The reference standards were prepared by spreading thin, uniform layers of powders on KAPTON tape and stacking a few layers to attain the desired absorption step height. Each spectrum was normalized using data processing software package IFEFFIT. Alignment of each sample reference spectrum with respect to Ti standard spectrum was within the range of +0.03 eV.
EPR measurements were performed on a Bruker Biospin Elexsys E 580 at ANL. The instrument was operated at a frequency of 9.3 GHz with a modulation frequency of 100 kHz. The field was swept at 3.5 Gauss/s over 300 to 1500 G range. The calibration of the g-values was done with DPPH. The Li content in charged samples was calculated by integrating the area under the EPR curve.
The volume of the unit cell expands slightly (approximately 1%) with cycling from 1st to 582nd cycle. The extent of lattice expansion between charged and discharged samples was less pronounced in the larger NTs (120 O.D. with 20 nm wall thickness) and volumes ranged between 562 to 557 Å3 (Table 1).
TiO2NT electrodes were prepared with varying size and their specific capacities were compared in Table 2. It has been observed that capacity decreases with the increase of the tube length. This can be understood as being due to an increase in ohmic resistance along the tube length, leading to decreased capacity. The capacity of larger NTs (120 O.D.) was enhanced indicating that the diffusion of Li ions into larger tubes was more efficient possibly due to the larger amount of ions in larger NTs.
a. Li System.
SEM images of both amorphous and annealed TiO2NT electrodes before and after electrochemical cycling in Li system are shown in
b. Na System.
The cycle life of amorphous TiO2NT sample in Li system was evaluated by electrochemically cycling for more than 500 cycles at approximately 0.6 A/g (2C) in a potential range of 2.5-0.9 V vs. Li/Li+. It has been found that this material has excellent cycling stability with approximately 95% retention of capacity and close to 100% columbic efficiency (
Charge Storage Behavior for TiO2NT: Capacitive Vs. Diffusion Processes.
The charge storage behavior of TiO2NT electrodes in Li and Na systems were studied using cyclic voltammetry under different scan rates (0.1-5 mV/s) with Li or Na metal serving as both counter and reference electrodes. There can be three contributions to charge storage: the faradaic contribution due to the intercalation of transporting ions (Li+, Na+); faradaic contribution from surface processes, referred to as pseudocapacitance; and non-faradaic contribution due to the double layer capacitance. Contributions to the charge storage mechanisms can be characterized by analyzing the cyclic voltammograms with varying scan rates according to:
i=aν
b (1)
where measured current i obeys a power law relationship with scan rate ν. Both a and b are adjustable parameters and b can be determined from plotting log(i) versus log(ν). For a process limited by diffusion, b would be 0.5 according to the following equation:
where n is number of electrons involved in the electrode reaction, F is faraday constant, A is the surface area of the electrode material, C* is the surface concentration, D is the diffusion coefficient, ν is the scan rate, R is the gas constant, α is the transfer coefficient, T is the temperature, and χ(bt) is the normalized current for a totally irreversible system in cyclic voltammetry. For a purely capacitive process, b is normally 1 according to the following equation:
i
c
=νC
d
A (3)
where Cd is the capacitance.
For charge storage in Li system with TiO2NT (
EPR measurements (
Vanadium pentoxide was synthesized by electrochemical deposition from the aqueous vanadyl sulfate electrolyte on a metal foil substrate, e.g., a Ni foil substrate, and then annealed in vacuum at 120° C. to remove intercalated water. Electrochemically synthesized electrodes offer long-range electronic conductivity, which improves responsiveness to applied potential, and therefore, their intercalation properties. Utilization of electrochemical deposition also brings high level of control to the structure, morphology, and uniformity of electrodes by adjusting the crucial parameters such as: applied current, potential and electric pulses, as well as the temperature and concentration of the electrolyte. In addition, vanadium oxide electrode is deposited directly on a current collector without the use of electronic conductor (such as carbon black or nickel powder) and/or a polymer binder (such as polyvinylidene difluoride).
Based on the scanning electron micrograph (
The result from synchrotron X-ray diffraction (XRD) (
When electrochemically grown V2O5 is annealed in oxygen atmosphere at 500° C., SEM image revealed that nanoribbons were converted to fine rod-like shape that exhibit orthorhombic crystalline structure (
Considering these findings, the crucial question is which one of these structures supports better the reversible intercalation of sodium transporting ions. While bilayered structure is atomically ordered only in a short range, the spacing between bilayers is more random. However, there is a lot of void space between randomly spaced bilayers after removal of intercalated water, which, if flexible enough, can readjust the spacing to enable intercalation of larger Na+ ions (model,
In order to evaluate functionality of these materials, each type of structure is formed on the separate electrode and they were submitted to cycling against sodium metal electrode (
The cycling curve is composed of two distinct parts: the first with a smooth slope indicative of solid solution intercalation mechanism that reaches about 235 mAh/g (theoretical capacity), and the second one at potentials >2.25 V when the slope changes to a steep curve indicative of capacitative mechanism. This small contribution of 15 mAh/g might be due to the capacitance of the surface layer or due to the presence of small amount of NiO formed at the interface between V2O5 and Ni substrate during the electrochemical deposition. Moreover, the shape of galvanostatic curves in
In contrast, the capacity of orthorhombic electrode rapidly decreases with cycling, as previously reported. The phase transformation in orthorhombic crystalline electrode is less pronounced as the cycling proceeds concomitantly with the decrease of the electrode capacity. This behavior suggests that the change in crystalline structure is associated with the fading of the orthorhombic electrode performance. Indeed, examination of XRD patterns with cycling reveals that orthorhombic V2O5 experienced deterioration in its crystallinity after first 10 cycles, which is followed by loss of crystallinity after prolonged cycling (
On the other hand, bilayered V2O5 electrodes were stable to repeated cycling and during prolonged galvanostatic cycling (up to 350 cycles) at high current density of 630 mA/g, and the average capacity of bilayered V2O5 electrodes remains at 85% of its initial value (
The oxidation state of the material is essential for redox processes that are taking place in rechargeable batteries, and for that reason we utilized X-ray absorption near edge spectra (XANES) in the V K-edge range for the bilayered V2O5, orthorhombic—V2O5(V5+ standard) and VO2 (V4+ standard). The obtained values were consistent with the previous results of V2O5 compounds and showed identical pre-edge shape and peak positions, implying that the V redox state in the bilayered V2O5 sample is close to V5+, in a common VO5 environment (
In addition, comparison of the V-K-edge k3 weighted EXAFS spectra show important differences (
The position and shape of the V 2p and O 1s XPS peaks before and after cycling of bilayered V2O5 electrodes confirms the reversibility of Na+ intercalation (
In order to understand mechanism of sodium insertion/de-insertion as well as the limits of discharge capacity and cyclability of bilayered V2O5 electrodes, it is important to understand the response of the bilayered V2O5 structure to the intercalation of sodium. For this purpose, we have used X-ray scattering that is a technique of choice for determining the changes in both short and long range order in crystalline and non-crystalline materials. Small and Wide angle X-ray scattering (SAXS and WAXS) measurements in situ (non-operando) confirm the initial structure of vacuum annealed bilayered V2O5 that was obtained from XRD measurements, i.e., layered structure with bilayers spaced at average distance of 13.5 Å apart, and the structural order within bilayers showing characteristic 3.44 Å spacing (
Upon initial discharging we observed that the interlayer d-spacing of the (001) plane (13.5 Å) and corresponding (002) plane (6.7 Å) dramatically change upon intercalation of sodium to 16.1 Å and 8.0 Å, respectively. Concomitantly, the width of the layer spacing peak narrows, and several peaks in the wide-angle region sharpen, suggesting 3D-like ordering of the structure upon sodium intercalation. Moreover, superimposed to the broader scattering pattern corresponding to newly developed sodium ion assembled layered structure one can observe a set of very narrow peaks, which originate from defined distances of intercalated sodium atom with atoms constituting the V2O5 bilayer. The intensity of these sharp features depends on the applied discharge currents (
Upon electrode oxidation (charging), and consequent Na+ deintercalation, this peak completely vanishes, confirming complete removal of Na ions in agreement with XPS restoration of V5+ state. Also all of the peaks associated with layered structure disappear and only those associated with short range order within bilayered structure are preserved. This suggests that after deintercalation of Na+ ions from the structure the stacking order is removed (
The extent of ordering and corresponding intensity of scattering features is dependent on the current density used for intercalation of Na+ ions. Interestingly, the highest current leads to more pronounced peaks, suggesting that higher concentration (flux) of intercalated atoms produces better ordering of the lattice. Moreover, the specific capacity of fast cycled electrode improves with the cycling. The full capacity of this electrode is established only after a number of cycles at high scanning rate, emphasizing the importance of availability of Na+ ions on electrode surface for obtaining theoretical capacities. Therefore, the superior discharge capacity retention of bilayered V2O5 electrodes compared to the other nanostructured vanadium pentoxide electrode reported in the literature may be attributed to the combined effects of their structural and surface properties. Highly accessible nanoscale architecture that combines conductivity with high surface area plays crucial role for ion and electron transport at the electrode/electrolyte interface.
It has been shown recently that the increased number of electrode/electrolyte interfacial interactions in nanostructured materials is critical to the formation of percolation pathways for fast diffusion of ions. Extensive adsorption of large sodium ions at the nanostructured electrochemical interface is important to initiate the intercalation process. At the same time the layered nature of the active material with low energy sites drives the Na+ diffusion into the material bulk structure. The combination of these processes is necessary for maximizing the flow of Na+ ions into the material. The net effect is enhanced pseudocapacitance that maximizes the electrostatic attraction of Na+ cations into V2O5 matrix. In addition, charge transfer ability of the bilayered V2O5 electrode is improved with the presence of more conductive surface defect species such as lower valence vanadium atoms (
Synthesis of nanostructured V2O5 electrodes.
Nanostructured V2O5 was synthesized by electrochemical deposition on pure Ni foil (0.0127 mm, 99.8%), which was cleaned in acetone and isopropyl. The electrochemical deposition was carried out in a three-electrode cell with Ni foil as the working electrode, Pt mesh as a counter electrode and Ag/AgCl as a reference electrode in aqueous 0.1 M VOSO4 solution at a constant potential of 1.5 V. Bilayered V2O5 electrodes were synthesized by vacuum annealing at 120° C. for 20 hours. The crystallized orthorhombic V2O5 electrodes were obtained by annealing of as-prepared V2O5 under O2 atmosphere at 500° C. for 4 hours.
Na-half cells were assembled in He-filled dry glove box into coin-type cells with a Na foil as the negative electrode, an electrolyte of 1 M NaClO4 in propylene carbonate (PC) and glassy fiber separator. For comparison, traditional electrode was made by mixing 84 wt % active material (V2O5 powder, Aldrich), 4 wt % graphite (TIMCAL SFG-6), 8 wt % poly(vinylidene difluoride) binder (KYNAR), and 4 wt % carbon black (Toka) and pressed on stainless steel mesh current collector. All cells were tested galvanostatically by automated Maccor battery tester at ambient temperature. Cyclic voltammograms of the cells were recorded in a Solartron 1470E Potentialstat/Galvanostat.
X-ray diffractions were performed at the beamline 13-ID-D of GSECARS sector at Advanced Photon Source (APS) at Argonne National Laboratory. The X-ray beam (37 keV energy, corresponding to X-ray wavelength of λ=0.3344 Å) was focused to a 2 μm diameter spot with a Kirkpatrick-Baez mirror system. The distance and tilting of the MAR165-CCD detector were calibrated using a CeO2 standard. V2O5 samples were prepared by stripping the V2O5 film from Ni support onto KAPTON tapes. Electrodes removed from cells for analysis were thoroughly washed with dry dimethyl carbonate and dried under inert atmosphere. The charged samples were also prepared by stripping V2O5 films onto KAPTON tape. The discharged samples were scratched-off and sealed inside a 3 mm-diameter hole in a piece of aluminum foil by sealing KAPTON sheet to the foil using epoxy. All cell operations were performed in a He-filled dry glove box (oxygen level <2 ppm). Simulations of XRD patterns were carried out using CRYSTALMAKER software (CrystalMaker Software, Ltd.) and are shown in
SAXS/WAXS data were collected at Beamline 12ID-B of the Advanced Photon Source (APS) at the Argonne National Laboratory (ANL). The X-ray was focused, and the spot size on the sample was about 50 m×50 μm. SAXS and WAXS data were presented in momentum transfer, q (q=4π sin θ/λ, where θ is one-half of the scattering angle, and λ=1.033 Å is the wavelength of the 12 keV energy probing X-ray), measured in the range 0.01-2.3 Å−1. The charged samples were prepared by stripping V2O5 films onto KAPTON tape. The discharged samples were scratched-off and sealed inside a 3 mm-diameter hole in a piece of aluminum foil by sealing KAPTON sheet to the foil using epoxy. All cell assembly and disassembly operations were performed in a He-filled dry glove box (oxygen level <2 ppm).
A SCIENTA hemispherical electron analyzer (SES100) was used to obtain the XPS/UPS measurements and total energy resolution of spectra, including photon energy, was set to less than about 0.1 eV. The acceptance angle for incoming electrons is (+) 5 degree. All experimental data were taken under the pressure of 2×10−10 torr or less.
Scanning Electron Microscopy (SEM) images were recorded with a JEOL JSM-7500F Field Emission SEM operating at 30 kV.
X-ray spectroscopy (XAS) and extended X-ray absorption fine structure (EXAFS) measurements were performed at PNC-XOR bending magnet beamline (20-BM-B) of APS in Argonne National Laboratory. Measurements at V K-edge were performed under transmission mode using gas ionization chambers to monitor the incident and transmitted X-ray intensities. A third ionization chamber was used in conjunction with a Ti-foil standard to provide internal calibration for the alignment of the edge positions. The incident beam was monochromatized using a Si (111) double crystal fixed exit monochromator. Harmonic rejection was accomplished using a Rhodium coated mirror. The charged samples were prepared by stripping V2O5 films onto KAPTON tape. The discharged samples were scratched-off and sealed inside a 3 mm-diameter hole in a piece of aluminum foil by sealing KAPTON sheet to the foil using epoxy. All cell assembly and disassembly operations were performed in a He-filled dry glove box (oxygen level <2 ppm). The reference standards (V5+ and V4+) were prepared by spreading thin, uniform layers of the V2O5 and VO2 power in KAPTON tape and stacking a few layers to attain the desired absorption step height. Each spectrum was normalized using data processing software package IFEFFIT. Alignment of each sample reference spectrum with respect to V standard spectrum is within the range of ±0.03 eV.
SEM Characterization of Morphology Before and after Cycling.
SEM images of both layered and crystalline V2O5 electrodes before and after electrochemical cycling in Na system are shown in
XPS Characterization of V Valence State Before and after Cycling.
The V2p and O1s peaks are shown in
XRD Characterization of Bilayered V2O5 Structure Before and after Na+ Intercalation.
Synchrotron X-ray diffraction spectra of bilayered V2O5 vacuum annealed at 120° C., before and after cycling with Na+-ions are shown in
In summary, nanostructured thin films of vanadium oxide prepared on Ni metal substrates by electrochemical deposition have been used as cathodes for Na-ion batteries without the need of electro-conductive carbon additives and polymeric binder. The above theoretical capacity of 250 mAh/g at room temperature, and electrolyte stable redox potentials around 3 V translates into an energy density of about 760 Wh/kg. Stable and reversible high capacity on repeated cycling (C/8) makes bilayered V2O5 a suitable cathode material for high-energy density rechargeable sodium batteries.
All references, including publications, patent applications, and patents, cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
The use of the terms “a” and “an” and “the” and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. The terms “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms (i.e., meaning “including, but not limited to,”) unless otherwise noted. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All numerical values obtained by measurement (e.g., weight, concentration, physical dimensions, removal rates, flow rates, and the like) are not to be construed as absolutely precise numbers, and should be considered to encompass values within the known limits of the measurement techniques commonly used in the art, regardless of whether or not the term “about” is explicitly stated. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate certain aspects of the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. Variations of those preferred embodiments may become apparent to those of ordinary skill in the art upon reading the foregoing description. The inventors expect skilled artisans to employ such variations as appropriate, and the inventors intend for the invention to be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications and equivalents of the subject matter recited in the claims appended hereto as permitted by applicable law. Moreover, any combination of the above-described elements in all possible variations thereof is encompassed by the invention unless otherwise indicated herein or otherwise clearly contradicted by context.
This application is a division of U.S. application Ser. No. 14/227,341, filed on Mar. 27, 2014, which is a continuation of International Application No. PCT/US2012/042230, filed on Jun. 13, 2012, which claims the benefit of U.S. Provisional Application Ser. No. 61/540,604 filed on Sep. 29, 2011, each of which is incorporated herein by reference in its entirety.
The United States Government has rights in this invention pursuant to Contract No. DE-AC02-06CH11357 between the United States Government and UChicago Argonne, LLC representing Argonne National Laboratory.
Number | Date | Country | |
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61540604 | Sep 2011 | US |
Number | Date | Country | |
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Parent | 14227341 | Mar 2014 | US |
Child | 15922596 | US |
Number | Date | Country | |
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Parent | PCT/US2012/042230 | Jun 2012 | US |
Child | 14227341 | US |