Abstract
V2O5, one of the earliest intercalation-type cathode materials investigated as a Li+ host, is characterized by an extremely high theoretical capacity (441 mAh g–1). However, the fast capacity fading upon cycling in conventional carbonate-based electrolytes is an unresolved issue. Herein, we show that using a LiTFSI/tetraglyme (1:1 in mole ratio) electrolyte yields a highly enhanced cycling ability of V2O5 (from 20% capacity retention to 80% after 100 cycles at 50 mA g–1 within 1.5–4.0 V vs Li+/Li). The improved performance mostly originates from the V2O5 electrode itself, since refreshing the electrolyte and the lithium electrode of the cycled cells does not help in restoring the V2O5 electrode capacity. Electrochemical impedance spectroscopy (EIS), post-mortem scanning electron microscopy (SEM), energy-dispersive X-ray (EDX) spectroscopy, and X-ray photoelectron spectroscopy (XPS) have been employed to investigate the origin of the improved electrochemical behavior. The results demonstrate that the enhanced cyclability is a consequence of a thinner but more stable cathode–electrolyte interphase (CEI) layer formed in LiTFSI/tetraglyme with respect to the one occurring in 1 M LiPF6 in EC/DMC (1:1 in weight ratio, LP30). These results show that the cyclability of V2O5 can be effectively improved by simple electrolyte engineering. At the same time, the uncovered mechanism further reveals the vital role of the CEI on the cyclability of V2O5, which can be helpful for the performance optimization of vanadium-oxide-based batteries.
Keywords: lithium batteries, highly concentrated electrolytes, cathode−electrolyte interphase, tetraglyme, vanadium oxides
Introduction
The limited supply of critical materials, e.g., lithium, nickel, and particularly cobalt, for the state-of-the-art lithium-ion batteries, is pushing the research efforts toward alternative batteries relying on more abundant metal cation carriers,1 e.g., Na+,2−5 K+,6,7 Mg2+,8 Ca2+,9 Zn2+,10 and Al3+.11 However, their higher charge density and/or larger ionic radius compared with Li+ lead to difficulties in finding suitable cathode host materials, especially for multivalent batteries.8,9,12 Among the limited choices, vanadium-oxide-based materials are promising candidates.13 Their tunable crystal structure usually offers large tunnels or interlayer space for the intercalation of the abovementioned cation guests,14 while the multielectron transition of the metal (V3+/5+) provides high theoretical specific capacities.15 Therefore, these materials have been widely investigated as hosts for various battery chemistries employing the abovementioned cations.16−21 However, the high specific capacity and good rate performance of these batteries are usually accompanied by fast capacity fading, especially at low rates, which limits the practical use of vanadium oxides.22−26 Searching for feasible strategies to enhance the cyclability of vanadium oxides and further explore the mechanism behind could lead to vanadium-oxide-based batteries with optimized performance. Due to the complexity of the newly emerging cell chemistries, whose components have not been well investigated, we selected a mature battery technology, i.e., lithium-based batteries, to reduce the complexity in the investigation of the fading mechanism.
Orthorhombic V2O5 is one of the earliest materials explored as reversible hosts for Li+, which can be traced back to more than 40 years ago.27 V2O5 exhibits an extremely high theoretical capacity (441 mAh g–1, 1.5–4.0 V vs Li+/Li), thus attracting broad research interests in the early exploration of cathode host materials for Li+.28 Its structural evolution and electrochemical behavior upon (de)lithiation have been well investigated and presented.29 However, the severe capacity fading is still an unsolved issue. Therefore, Li/orthorhombic V2O5 battery is an excellent model to investigate the parameters affecting the cyclability of vanadium-oxide-based materials. Several approaches have been applied to mitigate the fast capacity fading of V2O5, including the addition of secondary components,30 lattice dopant,31 and nanoarchitectures.22 Nonetheless, a capacity fading of 0.5–2.5% per cycle within the operation window of 1.5–4.0 V vs Li+/Li is still commonly seen in the literature.22 Therefore, strategies focusing only on the electrode materials are not enough to resolve the reduced lifespan of V2O5. Other cell components playing an active role in the cell need to be considered, such as the electrolyte.
Herein, we underline the importance of the proper electrolyte design to tune the battery performance at a higher level. The reported results indicate that the replacement of an LP30 carbonate electrolyte with a LiTFSI/tetraglyme electrolyte (mole ratio 1:1) leads to the enhanced cyclability of V2O5. Through refreshing the electrolyte and the lithium electrode of the cycled cells, to eliminate the effect originating from the anode degradation, it is proved that the enhanced cycling ability mainly originates from the cathode side. Scanning electron microscopy (SEM), energy-dispersive X-ray (EDX), X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), and electrochemical impedance spectroscopy (EIS) were carried out to investigate further the mechanism responsible for the improved capacity retention.
Results and Discussion
The crystal structure of commercial orthorhombic V2O5, herein used as the model material, was investigated via XRD (Figure S1a). The SEM image (Figure S1b) shows that the V2O5 powder is composed of large aggregates (50–60 μm) formed by smaller particles with dimensions in the range of 0.5–2 μm.
The cyclability of V2O5 electrodes was investigated in three-electrode cells, employing lithium reference and counter electrodes, at a low specific current (50 mA g–1) to reduce the influence of the lithium negative electrode. The first cycle voltage profiles of the V2O5 electrodes in the two electrolytes and their derivative curves are reported in Figure 1a,b, respectively. The observed voltage plateaus and differential peaks are associated with the α → ε and ε → δ phase transitions in the 3.4–2.7 V region (peak 1), which are followed by the δ → γ phase transition occurring in the 2.5–2.0 V region (peak 2) and the γ → ω phase transition taking place in the 2.0–1.5 V region (peak 3).32 The last phase transition is irreversible. In fact, the following reversible cycling involves only the transition between the disordered ω- and β-phases.32,33 However, the voltage plateaus (Figure 1c,e) and differential capacity peaks (Figure 1d,f) related to the phase transitions are observed until the 5th cycle, demonstrating that the irreversible transition from the initial α-phase to the ω-phase is not complete after the first discharge. In both electrolytes, the complete transformation to the ω-phase occurs only after the 5th cycle as demonstrated by the typical sloping voltage profile of disordered V2O5.
Figure 1.

First cycle (a) charge–discharge profiles and (b) corresponding differential capacity profiles of the Li/V2O5 cells using LP30 and LiTFSI/tetraglyme electrolytes. Panels (c) and (e) show the charge–discharge profiles of the Li/V2O5 cells during second to fifth cycles using, respectively, the LP30 and LiTFSI/tetraglyme electrolytes. The calculated differential capacity plots in second to fifth cycles of the Li/V2O5 cells using (d) LP30 and (f) LiTFSI/tetraglyme electrolytes. Galvanostatic cycling test performed at 50 mA g–1 and 20 °C.
Figure 2a shows the evolution of discharge specific capacity comparison upon 100 charge–discharge cycles for the Li/V2O5 cells employing the LP30 and LiTFSI/tetraglyme electrolytes. For both systems, the irreversibility in the initial cycles is mainly due to the irreversible transition from the α-phase to the ω-phase. Upon further cycling, the higher viscosity and lower ionic conductivity of the LiTFSI/tetraglyme electrolyte34 lead to lower initial capacity, however, with an improved cyclability. The capacity slowly decreases from 266 mAh g–1 at the sixth cycle to 225 mAh g–1 at the 100th cycle, exhibiting a capacity retention of 84%. With the conventional carbonate electrolyte (LP30), the capacity rapidly decreases from 309 mAh g–1 at the sixth cycle to 63 mAh g–1 at the 100th cycle, retaining only 20% of the initial capacity. Similar phenomena are also observed at elevated specific current, i.e., 440 mA g–1, as shown in Figure S2. These results demonstrate that the use of the highly concentrated LiTFSI/tetraglyme electrolyte can effectively promote the cyclability of V2O5 as a reversible cathode host material for Li+.
Figure 2.

Evolution of (a) discharge specific capacity and (b) Coulombic efficiency of the Li/V2O5 cells employing different electrolytes (see legends) upon cycling ability tests at 50 mA g–1 within 1.5–4.0 V versus Li+/Li. (c) The charge–discharge curve of the Li/V2O5 cells using cycled V2O5 electrodes and refreshed Li electrodes and electrolytes at 50 mA g–1.
Figure 2b displays the Coulombic efficiency (CE, calculated as Qdischarge/Qcharge) evolution upon cycling. The observed CE values higher than 100% in the initial cycles relate to the irreversible phase transitions occurring in the electrode material, which result in Li trapping. In fact, the CE value for the cell employing the LiTFSI/tetraglyme electrolyte reaches a stable value (about 99.98%) after 15 cycles, indicating the high reversibility of the (de)lithiation process. However, in the LP30 electrolyte, the steady-state CE is always higher than 100% (∼103%), which implies continuous side reactions during the reduction (discharge) process upon cycling, e.g., electrolyte decomposition35 or/and vanadium oxide dissolution.36 To evaluate the origin of the capacity decay, the cycled V2O5 electrodes were unmounted from the cells after 100 cycles and coupled with fresh lithium electrodes and electrolytes.37 The charge–discharge profiles at 50 mA g–1 of the reassembled cells are displayed in Figure 2c. These tests reveal that no capacity recovery is observed for the electrodes tested with both LP30 and LiTFSI/tetraglyme electrolytes, suggesting that the observed capacity fading originates mostly from the cathode side rather than degradation of the lithium electrode or the electrolyte. The possible influence in the intercalation process of the electrolyte was verified by the ex situ XRD of the cycled electrodes at their delithiated state (Figure S3). However, after 100 cycles, the XRD patterns of the electrodes cycled in the two electrolytes are very similar. Because the anion and the solvent are not involved in the intercalation in disordered V2O5, these two electrolytes unlikely affect the Li+ intercalation/deintercalation mechanism in V2O5. Therefore, it is reasonable to infer that the capacity decay does not result from the structural instability of V2O5 or degradation of lithium metal electrodes.
Figure 3 shows selected charge–discharge profiles and the resulting derivative capacity profiles of the Li/V2O5 cells upon cycling test performed using LP30 (Figure 3a,c) and LiTFSI/tetraglyme (Figure 3b,d) electrolytes at 50 mA g–1. The fast fading observed in the LP30 electrolyte exhibits dramatic changes in the potential profiles upon cycling (Figure 3a), clearly recognized in the differential capacity profiles (Figure 3c). The decreased peak intensity, associated with the capacity fading, is also accompanied by an increase in cell polarization as indicated by the shift of the peak positions. In contrast, the use of LiTFSI/tetraglyme only leads to minor changes in both the peak potential and the intensity in the differential capacity plots of the cell upon 100 cycles (Figure 3b,d), which is in agreement with the excellent capacity retention observed above.
Figure 3.
Selected charge–discharge profiles of the Li/V2O5 cells using (a) LP30 and (b) LiTFSI/tetraglyme electrolytes, respectively. The calculated differential capacity plots of the Li/V2O5 cells using (c) LP30 and (d) LiTFSI/tetraglyme electrolytes, respectively.
Figure 4a–c displays the SEM images of pristine and cycled V2O5 electrodes. In the pristine electrode (Figure 4a), the submicron V2O5 particles exhibit a smooth surface. After 100 cycles, the particle shape does not change for both electrolytes. Considering the severe capacity fading in the LP30 electrolyte (capacity retention is only 20% after 100 cycles), one can conclude that the dissolution of vanadium oxide reported in previous literature works is not the main reason for the capacity fading.36,38 Meanwhile, it is observed that the particles cycled in LP30 appear much rougher and are coated by a net-like deposit (Figure 4b), which is not observed on the surface of V2O5 cycled in the LiTFSI/tetraglyme electrolyte (Figure 4c). The EDX spectra displayed in Figure 4d evidence that the electrode cycled in LP30 exhibits higher content of C and F, compared with both the pristine electrode and the one cycled in LiTFSI/tetraglyme. This suggests different chemistries of the formed CEI in the different electrolyte formulations.
Figure 4.
SEM images of V2O5 in (a) the pristine electrode and electrodes cycled in (b) LP30 and (c) LiTFSI/tetraglyme electrolytes, and (d) corresponding EDX spectra.
XPS experiments were carried on the cycled electrodes (after 100 cycles) in the two electrolytes to further investigate their surface chemistries. The intensity scale was included and kept the same in both systems (except for the O 1s surface spectrum of the electrode tested in LP30 because it shows a much higher carbonate signal). Figure 5a,b displays the F 1s and O 1s + V 2p regions, respectively, of the electrode tested in LP30. The low intensity of the V 2p peak and the presence of several species with −C–O– and −F bonds in the O 1s and F 1s regions, respectively, clearly indicate that a CEI covers the V2O5 particle surface after cycling.39 The O 1s spectrum of the surface demonstrates that a Li2CO3-rich layer covers the electrode tested in LP30 (note that the carbonate signal is the main component). At higher depth (∼4.8 nm), the carbonate signal decreases, revealing a chemically different layer characterized by a lower amount of Li2CO3, but an increase of LiCO3R (R = alkyl chain), LixPOyFz, LiF, and other species with −COC– groups. Interestingly, a third layer is observed close to the electrode (∼9.6 nm in-depth), mainly consisting of −COC– species and LixPOyFz (shown in the schematic of the CEI, Figure 5e). Therefore, the CEI formed on the V2O5 cycled in LP30 shows three chemically different layers: an organic-rich layer close to the electrode and an inorganic-rich layer close to the electrolyte, separated by a mixed organic/inorganic layer in-between.
Figure 5.

F 1s and O 1s + V 2p photoelectron spectra at different depths (surface, 4.8, and 9.6 nm) of the V2O5 electrode after 100 charge–discharge cycles in (a, b) LP30 and (c, d) LiTFSI/tetraglyme electrolytes, respectively. The schematic of the CEIs formed in (e) LP30 and (f) LiTFSI/tetraglyme electrolytes.
Figure 5c,d displays the F 1s and O 1s + V 2p XPS spectra of the electrode cycled in LiTFSI/tetraglyme, respectively. Comparing the F 1s and O 1s regions with those obtained in LP30, one can find that despite the similarity of the formed species, the CEI formed in LiTFSI/tetraglyme is not carbonate-rich as in the LP30 electrode. In fact, a LiTFSI-rich layer mixed with −COC– species and a lower amount of Li2CO3, LiCO3R, and LiF are formed. At higher depths, i.e., ∼4.8 and ∼9.6 nm, the CEI is composed mainly of LiF. No change of composition is observed at these depths, in contrast with the multilayer structure of the CEI observed in the LP30 electrode (compare Figure 5e,f). In addition, it is known that LiF is a good electric insulator and can effectively block electron leakage through the interface, further mitigating the electrolyte decomposition upon cycling and resulting in a better CE.40
These results demonstrate that the CEI formed in LiTFSI/tetraglyme possesses a low amount of carbonate-based species but more −COC– species. Additionally, more LiF is formed in this electrolyte than in LP30 where more LixPFy or LizPOyFz are formed. These differences can be reasonably attributed to the different salts, solvents, salt concentrations, and, consequently, different solvation in LP30 and LiTFSI/tetraglyme electrolytes, implying that the V2O5/electrolyte interphase can be effectively tuned via the electrolyte formulation.
Besides the difference in chemical composition, the CEI formed in LP30 is evidently thicker than that in LiTFSI/tetraglyme. Comparing the O 1s spectra for the two electrodes at different depths, one can find that the V–O-related peak is much smaller for LP30. Meanwhile, the relative intensity of V 2p against O 1s on the surface spectrum is much lower for LP30 than for LiTFSI/tetraglyme. Furthermore, the peak located at 284.4 eV on C 1s (Figure S4), which results from −C–C– sp2 bonding and mainly corresponds to the conductive additive (C65),41 shows a lower intensity in LP30, again suggesting that the CEI is thicker for the electrode tested in LP30.
The difference in the CEI thickness and chemical composition of the electrodes cycled in LP30 and LiTFSI/tetraglyme agrees well with the electrochemical results reported in Figures 2 and 3 and the different deposit morphologies shown in the SEM images (Figure 4). The reported SEM, EDX, and XPS results present the composition and morphology of the CEI accumulated upon 100 charge–discharge cycles. These results indicate that the net-like deposits formed on V2O5 cycled in LP30 (Figure 4b) are mainly composed of lithium carbonate and lithium fluorophosphates.
To get a better understanding of the effect of the different CEI compositions on the electrochemical behavior, EIS was carried out. The Nyquist plots of the V2O5 electrode in the initial 10 cycles in LP30 and LiTFSI/tetraglyme are shown in Figure 6a,b, respectively. The EIS data can be well fitted according to the equivalent circuit shown in Figure 6c. Aurbach et al. have insightfully investigated the EIS of the V2O5 material and assigned the elements to specific electrochemical processes.42 The high-frequency intercept (ZRe) corresponds to a pure resistor (R1) associated with the bulk resistance of the electrolyte and electrodes. Three depressed semicircles (R2//Q2, R3//Q3, and R4//Q4) can be observed at lower frequencies. R2//Q2 and R3//Q3 stand for the Li+ migration through the surface layer covering the V2O5, while R4//Q4 relates to the Li+ transfer across the surface layer/V2O5 interface.42 At a very low frequency, the diffusion limitation in the bulk of the electrode occurs, noted as a Warburg element. The variation in R1 (Figure 6d) relates to the variation in the electrolyte resistance, while R2 + R3 + R4, summarized in Figure 6e, reflects the influence of the CEI in the electrochemical process. The R1 value is higher for the tetraglyme-based electrolyte, due to its lower ionic conductivity.34 For both electrolytes, the R1 values are stable upon the reported 10 cycles, suggesting no massive degradation of the electrolyte.
Figure 6.

Nyquist plots of the V2O5 electrode in the initial 10 cycles in (a) LP30 and (b) LiTFSI/tetraglyme electrolytes. (c) The equivalent electrical circuit used for fitting. The resistance evolution of (d) R1 and (e) R2 + R3 + R4 upon the initial 10 cycles.
In contrast, the value of (R2 + R3 + R4) shows different behaviors in the two electrolytes. After a small increase in the initial four cycles, this resistance value is seen to decrease for the electrode tested in LiTFSI/tetraglyme. On the other hand, it continuously increases upon cycling in LP30. Thus, despite the lower initial value, (R2 + R3 + R4) in the LP30 electrolyte becomes higher than in LiTFSI/tetraglyme after only six cycles. With more cycles in the LP30 electrolyte, the V2O5 electrode exhibits a significant increase of the impedance (Figure S5a), resulting in the cell not operating after 60 cycles. While the V2O5 electrode cycled in the LiTFSI/Tetragyme electrolyte still maintains a low impedance even after 100 cycles (Figure S5b). The results are also in good agreement with the CE upon cycling (Figure 2b), SEM images (Figure 4), and XPS analysis (Figure 5). Overall, it is reasonable to conclude that the poor cyclability of V2O5 in the LP30 electrolyte is a consequence of the unstable and more resistive CEI hindering the Li+ migration and transfer.
Conclusions
The rapid capacity fading of V2O5 upon cycling in conventional, carbonate-based electrolytes can be effectively mitigated via employing the LiTFSI/tetraglyme electrolyte. The enhanced cyclability mainly originates from a more stable and thinner CEI, mainly composed of LiF and organic ether species (−COC−) in the innermost layer and the outermost layer composed of LiTFSI and −COC–, resulting from the specific solvent, salt and its concentration, and, consequently, different solvation. The obtained results indicate that the cyclability of V2O5 can be improved by electrolyte engineering, while the uncovered mechanism further reveals the vital role of the CEI on the cyclability of V2O5. The insight into the CEI characteristics gives fundamental information, essential for the performance optimization of vanadium-oxide-based batteries.
Experimental Section
Materials
V2O5 (Pechiney), N-methyl-2-pyrrolidone (NMP, anhydrous, Sigma-Aldrich), poly(vinylidene fluoride) (PVdF, Solef 6020), carbon black (Super C65, Imerys), glass fiber sheet (Whatman GF/F), LP30 (BASF, battery grade), lithium metal (Honjo, battery grade), and dimethyl carbonate (DMC, UBE, battery grade) were directly used as received. Molecular sieves (3 Å, Alfa Aesar) were dried at 300 °C under vacuum (10–3 mbar) for more than 1 week. LiTFSI (3M Co., Ltd.) was dried at 120 °C under vacuum (10–3 mbar) for 12 h before use. The residual water in tetraethylene glycol dimethyl ether (tetraglyme, Sigma-Aldrich, 99%) was removed via the dried molecular sieves before use.
Physical and Chemical Characterizations
XRD was conducted on a diffractometer (D8 Advance Bruker, Germany) equipped with Cu Kα1,2 = 1.5418 Å radiation. SEM images of the as-prepared sample were obtained using a Zeiss LEO 1550 microscope equipped with EDX spectroscopy (Oxford Instruments X-MaxN, 50 mm2, 15 kV). XPS measurements were conducted in an ultrahigh vacuum surface analysis system (10–10 mbar) by a Phoibos 150 XPS spectrometer (SPECS-Surface concept) equipped with a microchannel plate and a delay line detector and monochromatized Al Kα (1486.6 eV) X-ray. The depth profiling was carried out using a focused ion gun for 5 keV Ar+ for 6 and 12 min. The peak fitting was carried out by CasaXPS software, using a Shiley-type background and a 70% Gaussian–30% Lorentzian profile function. For the post-mortem characterization, the electrodes were removed from Swagelok-type T-cells in an Ar-filled glovebox with H2O and O2 levels <0.1 ppm (MBraun). The samples were sealed in a plastic vessel to prevent exposure to humid air for XRD measurements, and for SEM, EDS, and XPS measurements, the samples were sealed in transfer boxes.
Electrochemical Measurements
The electrodes were fabricated by the doctor blade casting of slurries with 70 wt % V2O5, 20 wt % Super C65, and 10 wt % PVdF binder on aluminum foil (current collector). NMP was used as the solvent. After the solvent is evaporated with an electronic oven at 60 °C, electrodes with a diameter of 12 mm were punched and further dried at 120 °C under vacuum (1 × 10–3 mbar) for 12 h. The average mass loading of the active material was around 2 mg cm–2. The electrolyte preparation and cell assembly were carried out in an Ar-filled glovebox with H2O and O2 levels <0.1 ppm (MBraun). The LiTFSI/tetraglyme electrolyte was prepared by dissolving equal mole LiTFSI in tetraglyme. To evaluate the electrochemical behaviors of the V2O5 electrodes in LP30 and LiTFSI/tetraglyme, three-electrode Swagelok-type T-cells employing lithium metal as counter and reference electrodes and GF/F disks as separators were assembled. In each cell, 120 μL of electrolytes were used. Cycling ability was tested at 50 mA g–1 and 20 °C temperature via a MACCOR Series 4000 battery cycler. The EIS was conducted using a galvanostat/potentiostat VMP3 (Bio-Logic, France) and analyzed with Boukamp software.43
Acknowledgments
The research leading to these results has received funding from the H2020 Programme (H2020-FETOPEN-2018-2019-2020) under grant agreement no. 828902, Project “VIDICAT Versatile Ionomers for Divalent Calcium Batteries”. X.L. and B.Q. gratefully acknowledge financial support from the China Scholarship Council (CSC). M.Z. thanks the Basque Government for her Postdoctoral Fellowship. Financial support from the Helmholtz Association is also acknowledged.
Supporting Information Available
The Supporting Information is available free of charge at https://pubs.acs.org/doi/10.1021/acsami.0c16727.
XRD and SEM images of V2O5 particles; XRD pattern of carbon black, the pristine V2O5 electrode, and the ones after 100 cycles in different electrolytes; and C 1s XPS of cycled V2O5 electrodes; Nyquist plots of V2O5 electrodes after cycling in different electrolytes(PDF)
The authors declare no competing financial interest.
Supplementary Material
References
- Vaalma C.; Buchholz D.; Weil M.; Passerini S. A Cost and Resource Analysis of Sodium-Ion Batteries. Nat. Rev. Mater. 2018, 3, 18013 10.1038/natrevmats.2018.13. [DOI] [Google Scholar]
- Eshetu G. G.; Elia G. A.; Armand M.; Forsyth M.; Komaba S.; Rojo T.; Passerini S. Electrolytes and Interphases in Sodium-Based Rechargeable Batteries: Recent Advances and Perspectives. Adv. Energy Mater. 2020, 2000093 10.1002/aenm.202000093. [DOI] [Google Scholar]
- Xu J.; Gu E.; Zhang Z.; Xu Z.; Xu Y.; Du Y.; Zhu X.; Zhou X. Fabrication of Porous Na3V2(PO4)3/Reduced Graphene Oxide Hollow Spheres with Enhanced Sodium Storage Performance. J. Colloid Interface Sci. 2020, 567, 84–91. 10.1016/j.jcis.2020.01.121. [DOI] [PubMed] [Google Scholar]
- Zhang Z.; Du Y.; Wang Q. C.; Xu J.; Zhou Y. N.; Bao J.; Shen J.; Zhou X. A Yolk–Shell-Structured FePO4 Cathode for High-Rate and Long-Cycling Sodium-Ion Batteries. Angew. Chem., Int. Ed. 2020, 59, 17504–17510. 10.1002/anie.202008318. [DOI] [PubMed] [Google Scholar]
- Zhongfan L. Insight into Effects of Fluoroethylene Carbonate Additive on the Cathode in Sodium Ion Batteries. Acta Phys.-Chim. Sin. 2019, 35, 804–805. 10.3866/PKU.WHXB201903013. [DOI] [Google Scholar]
- Pramudita J. C.; Sehrawat D.; Goonetilleke D.; Sharma N. An Initial Review of the Status of Electrode Materials for Potassium-Ion Batteries. Adv. Energy Mater. 2017, 7, 1602911 10.1002/aenm.201602911. [DOI] [Google Scholar]
- Ge X.; Liu S.; Qiao M.; Du Y.; Li Y.; Bao J.; Zhou X. Enabling Superior Electrochemical Properties for Highly Efficient Potassium Storage by Impregnating Ultrafine Sb Nanocrystals within Nanochannel-Containing Carbon Nanofibers. Angew. Chem. 2019, 131, 14720–14725. 10.1002/ange.201908918. [DOI] [PubMed] [Google Scholar]
- Canepa P.; Sai Gautam G.; Hannah D. C.; Malik R.; Liu M.; Gallagher K. G.; Persson K. A.; Ceder G. Odyssey of Multivalent Cathode Materials: Open Questions and Future Challenges. Chem. Rev. 2017, 117, 4287–4341. 10.1021/acs.chemrev.6b00614. [DOI] [PubMed] [Google Scholar]
- Dugas R.; Forero-Saboya J. D.; Ponrouch A. Methods and Protocols for Reliable Electrochemical Testing in Post-Li Batteries (Na, K, Mg, and Ca). Chem. Mater. 2019, 31, 8613–8628. 10.1021/acs.chemmater.9b02776. [DOI] [PMC free article] [PubMed] [Google Scholar]
- Fang G.; Zhou J.; Pan A.; Liang S. Recent Advances in Aqueous Zinc-Ion Batteries. ACS Energy Lett. 2018, 3, 2480–2501. 10.1021/acsenergylett.8b01426. [DOI] [Google Scholar]
- Elia G. A.; Marquardt K.; Hoeppner K.; Fantini S.; Lin R.; Knipping E.; Peters W.; Drillet J.-F.; Passerini S.; Hahn R. An Overview and Future Perspectives of Aluminum Batteries. Adv. Mater. 2016, 28, 7564–7579. 10.1002/adma.201601357. [DOI] [PubMed] [Google Scholar]
- Tang B.; Shan L.; Liang S.; Zhou J. Issues and Opportunities Facing Aqueous Zinc-Ion Batteries. Energy Environ. Sci. 2019, 12, 3288–3304. 10.1039/C9EE02526J. [DOI] [Google Scholar]
- Xu X.; Xiong F.; Meng J.; An Q.; Mai L.. Multi-Electron Reactions of Vanadium-Based Nanomaterials for High-Capacity Lithium Batteries: Challenges and Opportunities. Mater. Today Nano 2020. https://doi.org/10.1016/j.mtnano.2020.100073. [Google Scholar]
- Song M.; Tan H.; Chao D.; Fan H. J. Recent Advances in Zn-Ion Batteries. Adv. Funct. Mater. 2018, 28, 1–27. 10.1002/adfm.201802564. [DOI] [Google Scholar]
- Moretti A.; Maroni F.; Nobili F.; Passerini S. V2O5 Electrodes with Extended Cycling Ability and Improved Rate Performance Using Polyacrylic Acid as Binder. J. Power Sources 2014, 293, 1068–1072. 10.1016/j.jpowsour.2014.09.150. [DOI] [Google Scholar]
- Moretti A.; Passerini S. Bilayered Nanostructured V2O5·nH2O for Metal Batteries. Adv. Energy Mater. 2016, 6, 1600868 10.1002/aenm.201600868. [DOI] [Google Scholar]
- Liu X.; Qin B.; Zhang H.; Moretti A.; Passerini S. Glyme-Based Electrolyte for Na/Bilayered-V 2 O 5 Batteries. ACS Appl. Energy Mater 2019, 2, 2786–2793. 10.1021/acsaem.9b00128. [DOI] [Google Scholar]
- Liu X.; Zhang H.; Geiger D.; Han J.; Varzi A.; Kaiser U.; Moretti A.; Passerini S. Calcium Vanadate Sub-Microfibers as Highly Reversible Host Cathode Material for Aqueous Zinc-Ion Batteries. Chem. Commun. 2019, 55, 2265–2268. 10.1039/C8CC07243D. [DOI] [PubMed] [Google Scholar]
- Liu X.; Elia G. A.; Gao X.; Qin B.; Zhang H.; Passerini S. Highly Concentrated KTFSI: Glyme Electrolytes for K/Bilayered-V 2 O 5 Batteries. Batteries Supercaps 2020, 3, 261–267. 10.1002/batt.202000003. [DOI] [Google Scholar]
- Wan F.; Zhang L.; Dai X.; Wang X.; Niu Z.; Chen J. Aqueous Rechargeable Zinc/Sodium Vanadate Batteries with Enhanced Performance from Simultaneous Insertion of Dual Carriers. Nat. Commun. 2018, 9, 1656 10.1038/s41467-018-04060-8. [DOI] [PMC free article] [PubMed] [Google Scholar]
- Xu X.; Duan M.; Yue Y.; Li Q.; Zhang X.; Wu L.; Wu P.; Song B.; Mai L. Bilayered Mg0.25V2O5·H2O as a Stable Cathode for Rechargeable Ca-Ion Batteries. ACS Energy Lett. 2019, 4, 1328–1335. 10.1021/acsenergylett.9b00830. [DOI] [Google Scholar]
- Yue Y.; Liang H. Micro- and Nano-Structured Vanadium Pentoxide (V2O5) for Electrodes of Lithium-Ion Batteries. Adv. Energy Mater. 2017, 7, 1602545 10.1002/aenm.201602545. [DOI] [Google Scholar]
- Wei Q.; Liu J.; Feng W.; Sheng J.; Tian X.; He L.; An Q.; Mai L. Hydrated Vanadium Pentoxide with Superior Sodium Storage Capacity. J. Mater. Chem. A 2015, 3, 8070–8075. 10.1039/C5TA00502G. [DOI] [Google Scholar]
- Clites M.; Hart J. L.; Taheri M. L.; Pomerantseva E. Chemically Preintercalated Bilayered KxV2O5· n H2O Nanobelts as a High-Performing Cathode Material for K-Ion Batteries. ACS Energy Lett. 2018, 3, 562–567. 10.1021/acsenergylett.7b01278. [DOI] [Google Scholar]
- Gao X.; Mariani A.; Jeong S.; Liu X.; Dou X.; Ding M.; Moretti A.; Passerini S. Prototype Rechargeable Magnesium Batteries Using Ionic Liquid Electrolytes. J. Power Sources 2019, 423, 52–59. 10.1016/j.jpowsour.2019.03.049. [DOI] [Google Scholar]
- Yang Y.; Tang Y.; Fang G.; Shan L.; Guo J.; Zhang W.; Wang C.; Wang L.; Zhou J.; Liang S. Li+ Intercalated V2O5·: N H2O with Enlarged Layer Spacing and Fast Ion Diffusion as an Aqueous Zinc-Ion Battery Cathode. Energy Environ. Sci. 2018, 11, 3157–3162. 10.1039/C8EE01651H. [DOI] [Google Scholar]
- Whittingham M. S. The Role of Ternary Phases in Cathode Reactions. J. Electrochem. Soc. 1976, 123, 315–320. 10.1149/1.2132817. [DOI] [Google Scholar]
- Yao J.; Li Y.; Massé R. C.; Uchaker E.; Cao G. Revitalized Interest in Vanadium Pentoxide as Cathode Material for Lithium-Ion Batteries and Beyond. Energy Storage Materials 2018, 11, 205–259. 10.1016/j.ensm.2017.10.014. [DOI] [Google Scholar]
- Baddour-Hadjean R.; Marzouk A.; Pereira-Ramos J. P. Structural Modifications of LixV2O5 in a Composite Cathode (0≤x <2) Investigated by Raman Microspectrometry. J. Raman Spectrosc. 2012, 43, 153–160. 10.1002/jrs.2984. [DOI] [Google Scholar]
- Cheng J.; Wang B.; Xin H. L.; Yang G.; Cai H.; Nie F.; Huang H. Self-Assembled V2O5 Nanosheets/Reduced Graphene Oxide Hierarchical Nanocomposite as a High-Performance Cathode Material for Lithium Ion Batteries. J. Mater. Chem. A 2013, 1, 10814 10.1039/c3ta12066j. [DOI] [Google Scholar]
- Song H.; Liu C.; Zhang C.; Cao G. Self-Doped V4+-V2O5 Nanoflake for 2 Li-Ion Intercalation with Enhanced Rate and Cycling Performance. Nano Energy 2016, 22, 1–10. 10.1016/j.nanoen.2016.02.004. [DOI] [Google Scholar]
- Christensen C. K.; Sørensen D. R.; Hvam J.; Ravnsbæk D. B. Structural Evolution of Disordered Li x V 2 O 5 Bronzes in V 2 O 5 Cathodes for Li-Ion Batteries. Chem. Mater. 2019, 31, 512–520. 10.1021/acs.chemmater.8b04558. [DOI] [Google Scholar]
- Feng C. Q.; Wang S. Y.; Zeng R.; Guo Z. P.; Konstantinov K.; Liu H. K. Synthesis of Spherical Porous Vanadium Pentoxide and Its Electrochemical Properties. J. Power Sources 2008, 184, 485–488. 10.1016/j.jpowsour.2008.04.049. [DOI] [Google Scholar]
- Dokko K.; Tachikawa N.; Yamauchi K.; Tsuchiya M.; Yamazaki A.; Takashima E.; Park J.-W.; Ueno K.; Seki S.; Serizawa N.; Watanabe M. Solvate Ionic Liquid Electrolyte for Li–S Batteries. J. Electrochem. Soc. 2013, 160, A1304–A1310. 10.1149/2.111308jes. [DOI] [Google Scholar]
- Fleutot B.; Martinez H.; Pecquenard B.; Ledeuil J. B.; Levasseur A.; Gonbeau D. Surface Film Morphology (AFM) and Chemical Features (XPS) of Cycled V2O5 Thin Films in Lithium Microbatteries. J. Power Sources 2008, 180, 836–844. 10.1016/j.jpowsour.2008.02.080. [DOI] [Google Scholar]
- Moretti A.; Jeong S.; Passerini S. Enhanced Cycling Ability of V2O5 Aerogel Using Room-Temperature Ionic Liquid-Based Electrolytes. ChemElectroChem 2016, 3, 1048–1053. 10.1002/celc.201600040. [DOI] [Google Scholar]
- Jiao S.; Ren X.; Cao R.; Engelhard M. H.; Liu Y.; Hu D.; Mei D.; Zheng J.; Zhao W.; Li Q.; Liu N.; Adams B. D.; Ma C.; Liu J.; Zhang J. G.; Xu W. Stable Cycling of High-Voltage Lithium Metal Batteries in Ether Electrolytes. Nat. Energy 2018, 3, 739–746. 10.1038/s41560-018-0199-8. [DOI] [Google Scholar]
- Sudant G.; Baudrin E.; Dunn B.; Tarascon J.-M. Synthesis and Electrochemical Properties of Vanadium Oxide Aerogels Prepared by a Freeze-Drying Process. J. Electrochem. Soc. 2004, 151, A666 10.1149/1.1687427. [DOI] [Google Scholar]
- Hekmatfar M.; Kazzazi A.; Eshetu G. G.; Hasa I.; Passerini S. Understanding the Electrode/Electrolyte Interface Layer on the Li-Rich Nickel Manganese Cobalt Layered Oxide Cathode by XPS. ACS Appl. Mater. Interfaces 2019, 11, 43166–43179. 10.1021/acsami.9b14389. [DOI] [PubMed] [Google Scholar]
- Fan X.; Chen L.; Borodin O.; Ji X.; Chen J.; Hou S.; Deng T.; Zheng J.; Yang C.; Liou S. C.; Amine K.; Xu K.; Wang C. S. Non-Flammable Electrolyte Enables Li-Metal Batteries with Aggressive Cathode Chemistries. Nat. Nanotechnol. 2018, 13, 715–722. 10.1038/s41565-018-0183-2. [DOI] [PubMed] [Google Scholar]
- Zarrabeitia M.; Gomes Chagas L.; Kuenzel M.; Gonzalo E.; Rojo T.; Passerini S.; Muñoz-Márquez M. Á. Toward Stable Electrode/Electrolyte Interface of P2-Layered Oxide for Rechargeable Na-Ion Batteries. ACS Appl. Mater. Interfaces 2019, 11, 28885–28893. 10.1021/acsami.9b07963. [DOI] [PubMed] [Google Scholar]
- Levi M. D.; Lu Z.; Aurbach D. Application of Finite-Diffusion Models for the Interpretation of Chronoamperometric and Electrochemical Impedance Responses of Thin Lithium Insertion V2O5 Electrodes. Solid State Ionics 2001, 143, 309–318. 10.1016/S0167-2738(01)00819-0. [DOI] [Google Scholar]
- Boukamp B. A. A Nonlinear Least Squares Fit procedure for analysis of immittance data of electrochemical systems. Solid State Ionics 1986, 20, 31–44. 10.1016/0167-2738(86)90031-7. [DOI] [Google Scholar]
Associated Data
This section collects any data citations, data availability statements, or supplementary materials included in this article.



