J. Electrochem. Sci. Technol Search

CLOSE


J. Electrochem. Sci. Technol > Volume 16(4); 2025 > Article
Chu, Li, and Bae: Novel Li3V2-xMox(PO4)3 Electrode Material and Liquid Electrolytes for Lithium-Ion Batteries Cycled at Cryogenic Temperatures

Abstract

Lithium-ion batteries (LIBs) are widely used owing to their high specific energy and long lifespans. However, cryogenic temperatures can restrict their application considerably—for example, during cold weather (winter) and military and aerospace exploration. Molybdenum (Mo)-doped Li3V2-xMox(PO4)3 has a beneficial tetrahedron and octahedron structure that is stable at low temperatures and shorter distances (for Li+ transmission), which contributes to higher ion conductivity at low temperatures. The theoretical capacity of Li3V2(PO4)3 in the 3.0–4.3 V working range is 132 mAh/g, reaching 197 mAh/g in the 3.0–4.8 V working range. In this study, we first examined the optimal molar ratio of Mo in a commercial electrolyte, the most suitable Mo molar ratio being 0.02 with a specific capacity of 121.3 mAh/g in the 3.0–4.3 V working range under ambient temperature conditions. Subsequently, we developed a novel electrolyte with a volume ratio of 1,3-dioxolane:1,2-dimethoxyethane (DOL:DME) of 8:2. Here, the specific capacity was 102.3 mAh/g at room temperature with a capacity retention of 42.3%; moreover, the specific capacity was 43.3 mAh/g at 223 K with a capacity retention of 0.11% at 193 K.

ABBREVIATIONS

The following abbreviations are used in this manuscript:

CV

Cyclic voltammetry

DOI

Digital object identifier

DOL

1,3-dioxolane

DME

1,2-dimethoxyethane

EV

Electric vehicle

LIB

Lithium-ion battery

SEI

Solid electrolyte interface

SEM

Scanning electron microscopy

STD

Standard electrolyte

TEM

Transmission electron microscopy

XPS

X-ray photoelectron spectroscopy

XRD

X-ray diffraction

INTRODUCTION

With the ongoing development of electric vehicles (EVs), laptops, mobile phones, and other commercial electronics [13], the demand for energy storage devices has increased considerably. Moreover, lithium-ion batteries (LIBs) are widely used in modern industrial production because of their high specific energy [4] and long lifespan [5]. However, although LIBs are well-proven in myriad electronic applications, extremely cold working environments can limit their performance considerably [6,7] —such as EVs operating at high latitudes where winter temperatures can fall below −40°C, or in military and aerospace exploration which require LIBs to operate stably under wide temperature conditions (−40°C to 60°C) [7]. Consequently, cryogenic battery research has become a popular topic in the field of electrochemical research to improve the operating temperature range of batteries.
Over the past few decades, LiFePO4 has been the main commercial cathode material [810], used for LIBs, as it offers good performance [11], low cost and safety [12]. However, the performance of LIBs diminishes considerably at cryogenic temperatures [13], which presents a major challenge to their application in various fields. For example, in cold weather conditions during winter, the reduced efficiency of LIBs can hinder their use in EVs [14], portable electronics [15], and energy storage systems [16]. This temperature sensitivity is particularly problematic for critical applications, such as military operations and aerospace exploration [17], where reliable battery performance in extreme environments is essential. Consequently, overcoming the challenges posed by low temperatures is crucial for expanding their practical application in these demanding fields. Owing to their high operating voltage [18] and discharge capacity [19], and particularly their excellent low-temperature cycling performance [20,21], molybdenum (Mo)-doped cathode materials have attracted considerable attention [2,22,23].
In this study, we investigated the optimal molar ratio of Mo in a commercial electrolyte. Our findings revealed that a molar ratio of 0.02 for Mo provided the best performance, delivering a specific capacity of 121.3 mAh/g within an operating voltage range of 3.0–4.3 V at ambient temperature. Based on these results, we developed a novel electrolyte formulation with a volume ratio of 1,3-dioxolane:1,2-dimethoxyethane (DOL:DME) of 8:2. The new electrolyte exhibited a specific capacity of 102.3 mAh/g at room temperature. Even under cryogenic conditions, the electrolyte exhibited impressive stability, with a capacity retention of 42.3% at 223 K, corresponding to a specific capacity of 43.3 mAh/g. Notably, the electrolyte retained 0.11% of its capacity even at 193 K. These results demonstrated that the novel electrolyte not only performed well under standard conditions, but also exhibited remarkable resilience under extremely low-temperature conditions, making it a promising candidate for use in applications requiring robust performance across a wide temperature range.

EXPERIMENTS

Materials synthesis

The LVMP samples were prepared using the hydrothermal treatment method. The V2O5, LiH2PO4, and (NH6)Mo7O24·4H2O precursor salts were obtained from Sigma–Aldrich, and the various elements were added in a stoichiometric ratio—that is, the molar ratio of Li:V:P was 3:2:3. First, 0.01 mol V2O5 was dissolved in 35 ml deionized water, named Solution 1, and the slurry was stirred at 70°C. Solution 2 comprised an aqueous solution of 0.03 mol LiH2PO4 and 0.00014 mol (NH6)Mo7O24·4H2O (the amount of Mo being 0.001 mol) dissolved in 35 mL deionized water. A mixture of Solutions 1 and 2 was continually stirred at 400 rpm for 0.5 h at 70°C.
Next, 2.5 mL ethylene glycol was added to the mixture and the pH was adjusted to 2 using HNO3, before being continually stirred for 40 min at the same temperature. Subsequently, the solution was transferred into a Teflon autoclave and heated for 3 h at 180°C in a vacuum oven. After the hydrothermal process, the slurry was dried by stirring at 70°C overnight to obtain a green gel, after which the sample was dried at 90°C for 12 h in the vacuum oven to obtain a green powder. The green powder was mixed with α-glucose (the molar ratio of glucose:V being 1:4) in an ethanal solvent and stirred at room temperature to evaporate the solvent. Finally, the sample was ground and calcined at 700°C at a heating ramp rate of 5°C/min under an argon (Ar) atmosphere for 12 h to obtain the target sample (recognized as LVM0.1P). The preparation of the LVP, and LVM0.02P samples used the same process, with just the amount of Mo changing.
Novel electrolytes were prepared using 1,3-dioxolane (DOL) and 1,2-dimethoxyethan (DME), with the volume ratios of 2:8 and 1:1 being recorded as DDL and DDL(1), respectively. The lithium salt used was bis(trifluoromethane) sulfonimide (LiTFSI), at a concentration of 1.0 M. All the chemicals were purchased from Sigma–Aldrich. All the processes were carried out in a glove box without water or oxygen.

Materials characterization

X-ray diffraction (XRD) patterns were obtained using a Rigaku (MPA-2000) diffractometer with Cu Ka radiation (l = 1.5418 Å). The scan speed was 1°/min and the scan range was from 10 to 80°. X-ray photoelectron spectroscopy (XPS) was conducted using an ESCALAB 250 spectrometer with an Mg Ka X-ray source. The morphologies, structures, and energy-dispersive spectra were examined using the JEOL JSM-7500F scanning electron microscope, and high-resolution transmission electron microscopy (HRTEM) was performed using an FEI Tecnai F30 instrument operated at 300 kV.

Electrochemical measurements

CR2032 coin cells were assembled in an Ar-filled glove box using the synthesized NCF-Mo-doped LVMP as the cathode substrate. The polysulfide catholyte was added dropwise, and lithium metal served as the anode. A polypropylene film (Celgard 2500) was used as the separator, with the electrolyte comprising a 1 M LiTFSI solution in a 1:1 volume ratio of DOL:DME standard (STD) electrolyte and copper as the anode. A CR2032 coin cell with the novel electrolyte—that is, the DDL—was designed for cryogenic IV measurements. Galvanostatic charge-discharge experiments were conducted using a LAND CT2001A battery analyzer within a 3.0–4.3 V voltage range. Cyclic voltammetry (CV) tests were conducted within a voltage window of 3.0–4.3 V using the CHI604E electrochemical workstation from Chenhua, Shanghai, China at a scanning speed of 10 mV/s. Low-temperature IV measurements were then performed using the cryogenic system.

RESULTS AND DISCUSSION

The XRD pattern of the LVMP is shown in Fig. 1. Compared to the standard cards (JCPDF: 78-5405 and JCPDF: 81-2414), the samples exhibited a monoclinic structure without impurity peaks. However, when Mo was doped at 0.02, no Mo peak was evident owing to the low Mo concentration. The broadening of the peak width indicates an increase in crystal grain size, caused by the incorporation of Mo into the Li3V2(PO4)3 lattice, leading to changes in the lattice parameters. When the Mo content increased to 0.1, distinctively characteristic Mo peaks were evident, verifying a pure phase with homogeneous V doping in the lattice without any detectable phase separation of MoO3 [24]. As shown in the inset of Fig. 1, the XRD peaks of the doped samples systematically shift toward higher 2θ positions with increasing Mo doping concentration. This trend indicates a reduction in unit cell volume, suggesting that the larger V3+ ions (0.064 nm) have been successfully replaced by the smaller Mo6+ ions (0.059 nm). And the cell parameters have been listed in Table 1.
The scanning electron microscopy (SEM) image shown in Fig. 2 shows that the particles of LiV2–xMox(PO4)3 were relatively evenly distributed. Although the particles were irregular in shape, their sizes were mostly between 0.5 and 1 μm. Almost no large secondary particles were formed through agglomeration. This uniform distribution facilitated better penetration of the electrolyte into the electrode, shortening the lithium-ion diffusion path, thereby enhancing the electrochemical performance of the material.
Fig. 3 presents high-resolution TEM (HRTEM) images of the Li3V1.9Mo0.1(PO4)3 batteries, demonstrating that the LVMP sample retained the same layered structure as the LVP sample. The metallic Mo particles on the surface of the LVMP sample were uniformly distributed. The TEM image also revealed a lattice fringe of 0.45 nm, corresponding to the (200) plane of MVO, as noted in reference [24].
The XPS spectra of the Li3V2-xMox(PO4)3 cathode materials are shown in Fig. 4(a,b). After Mo doping, the Li valence band shifted from 55.53 to 55.43 eV, indicating that the incorporation of Mo facilitated the insertion and migration of Li ions during the charge and discharge processes in the electrode material. This enhancement leads to an improvement in the battery capacity at low temperatures because Mo doping promotes better Li+ mobility, thereby increasing the efficiency of the electrode material.
The XPS spectra of the Li3V2(PO4)3 sample, as shown in Fig. 4(c), indicate a V2p binding energy of 517.18 eV, which closely corresponds to the 517.2 eV [25] observed in the Li3V2(PO4)3 sample. This suggests that vanadium in the amorphous Li3V2(PO4)3 precursor existed in the V3+ oxidation state. Compared with the Li3V1.98Mo0.02(PO4)3 sample, after Mo doping the V2p shifted to 517.16 eV suggesting that the Mo could change the electrode structure and enhance the migration of Li+ ions. The band energies and atomic ratios are listed in Table 2 and Table 3.
Fig. 5 shows the CV curves of the commercial STD electrolyte and the novel DDL electrolyte. As shown in Fig. 4, as the voltage increased, the current gradually increased, indicating the onset of decomposition in the STD electrolyte. When the voltage reached approximately 4.25 V, the electrolyte began to decompose, the rate of decomposition increasing with increasing voltage. However, the novel DDL electrolyte used in this experiment maintained a stable current across the entire voltage range of 1–7 V, indicating its superior stability. Moreover, the incorporation of DOL lowered the freezing point of the electrolyte and enhanced its conductivity at low temperatures.
Fig. 6(a) shows the electrochemical cycling curves for different Mo-doping levels in the DDL electrolyte. As shown in the figure, at room temperature an appropriate amount of Mo doping could increase the battery capacity; however, when the Mo-doping level was too high, the battery capacity decreased, leading to reduced performance. This is primarily because Mo, as a transition metal, has good electrical conductivity. Consequently, Mo doping can enhance the electronic conductivity of the electrode materials, allowing faster charge transfer during the charging and discharging processes, thereby improving the rate and overall electrochemical performance of the battery. Moreover, Mo doping can help the formation of a more stable solid electrolyte interface (SEI) layer, reducing side reactions and minimizing electrolyte decomposition. A stable SEI layer contributes to enhanced cycling stability and safety of the battery.
However, excessive Mo doping can introduce too many impurities or defects into the material, obstructing the electron conduction pathways, and thus reducing its conductivity. This can impair the electrochemical performance of the battery, causing lattice distortion or structural instability in the active material, affecting the lithium-ion intercalation and deintercalation. Ultimately, this results in a decrease in the specific capacity and negatively affects the energy density of the battery. In this study, the battery achieved a maximum electrochemical capacity of 121.3 mAh/g when the Mo-doping level was 0.02%. However, when the Mo-doping level was increased to 0.1%, the battery capacity dropped to 117.9 mAh/g.
Fig. 6(b) illustrates the behavior of the Li+ ions during the charge and discharge cycles [26]. In the anodic scan, three distinct peaks appear at 3.60, 3.70, and 4.10 V, representing a sequence of phase transitions that occur during the extraction of Li+ at various stages from the LiV2–xMox(PO4)3 sample (where x = 3.0, 2.5, 2.0, and 1.0). The overall electrochemical reaction can be expressed as follows:
Charge Cycle:
(1)
Li3V2PO43-0.5Li+0.5e-Li2.5V3+V1/24+PO43
(2)
Li2.5V3+VPO43-0.5Li+0.5e-Li2V3+V4+PO43
(3)
Li2V3+V4+PO43-Li+e-LiV24+PO43
(4)
LiV1/24+PO43-Li+e-V24.5+PO43
Discharge Cycle:
(5)
V24.5+PO43+2Li+-2e-Li2V3+V4+PO43
(6)
Li2V3+V4+PO43+0.5Li++0.5e-Li2.5V3+V1/24+PO43
(7)
Li2.5V3+V1/24+PO43+0.5Li++0.5e-Li3V2PO43
A cyclic voltammogram of the LiV2–xMox(PO4)3 obtained at a scan rate of 0.1 mV/s at different temperatures is shown in Fig. 7. Three anodic and three cathodic peaks could be detected during the anodic and cathodic scans in given potential windows (3.0–4.3 V).
Fig. 8 shows three anodic and three cathodic peaks. The potential difference between the anodic and cathodic peaks (ΔV) reflects the insertion and extraction behavior of Li during the charging and discharging process of the lithium battery. An increase in ΔV indicates that the extraction of Li becomes more difficult during the charging process, meaning that the activation energy for Li desorption increases. This phenomenon leads to a reduction in the overall capacity of the battery because Li+ cannot desorb smoothly, thereby reducing the effective discharge capacity.
From Fig. 7 and Table 4, for the LVM0.02P sample, ΔV gradually increased as the temperature decreased. For example, when the temperature decreased from 298 to 243 K, ΔV increased from 0.1 to 0.2 V. This indicates that at lower temperatures, the migration and extraction of Li became more difficult, possibly owing to dynamic changes at the interface between the electrode material and the porous medium, leading to an increase in activation energy.
Using the Randles–Sevcik equation, the diffusion coefficient of Li (DappLi+) was calculated, the detailed results of which are listed in Table 5. The results showed that at 298 K, the diffusion coefficient of Li+ in the LVM0.02P sample was 3.08×10–9 cm2/s, whereas in the LVM0.1P sample, it was 7.44×10–9 cm2/s. This indicates that the insertion and extraction of Li+ were easier in the LVM0.1P sample at room temperature. However, for the LVM0.1P sample, as the temperature decreased, ΔV increased from 0.12 V at 298 K to 0.40 V at 253 K, further proving the effect of temperature on the migration of lithium ions and the battery performance.
ip=0.4463ncFAnFvDRT1/2
· ip = Current maximum in amps (A)
· n = Number of electrons transferred in the redox event (usually 1)
· A = Electrode area in cm2
· F = Faraday Constant in C/mol
· D = Diffusion coefficient in cm2/s
· C = Concentration in mol/cm3
· ν = Scan rate in V/s
· R = Gas constant in J/K/mol
· T = temperature in K
· Constant with a value of 2.69×105 has units of C/mol/V1/2
Fig. 8 shows a comparison of CV curves for the batteries using the commercial STD electrolyte and novel DDL electrolyte with LVM0.02P as the anode under ultralow temperature conditions. Fig. 8(a) presents the CV curves of the STD electrolyte at different operating temperatures, whereas Fig. 8(b) shows the CV curves of the novel DDL electrolyte at various temperatures. The data indicate that as the temperature decreased, the performance of all batteries declined. However, the rate of performance degradation of the STD electrolyte was considerably higher than that of the novel DDL electrolyte. At 233 K, the capacity of the battery with the STD electrolyte dropped from 115.0 mAh/g at room temperature (298 K) to 9.0 mAh/g, which was only 7.8% of its initial capacity. Further temperature reductions led to the battery becoming nonfunctional, with the capacity completely disappearing. By contrast, for the novel DDL electrolyte, the battery capacity at 233 K was 61.6 mAh/g, approximately 60.22% of the initial capacity. Even when the temperature was lowered further to 193 K, the battery was still able to charge and discharge, with a capacity of 0.1 mAh/g, about 0.11% of the initial capacity. Specific values are listed in Table 6 and 7, demonstrating that the novel electrolyte exhibited excellent performance under low-temperature conditions, making it suitable for low-temperature LIB applications.
In Fig. 8, the discharge curves of the STD and DDL electrolytes exhibit distinct differences, primarily due to variations in electrolyte composition, ion transport properties, and electrochemical stability. The STD electrolyte, with its conventional formulation, demonstrates limited ion transport at low temperatures, as evidenced by a significant capacity drop at 233 K. In contrast, the DDL electrolyte, tailored for low-temperature applications, likely incorporates additives or solvents that enhance lithium-ion mobility and reduce electrolyte viscosity, leading to improved capacity retention. The discharge profile of the STD electrolyte shows a pronounced decline in capacity and voltage with decreasing temperature, indicative of sluggish ion diffusion and increased internal resistance. Conversely, the DDL electrolyte maintains stable and well-defined voltage plateaus even at 213 K and 193 K, suggesting enhanced electrolyte-electrode compatibility and sustained redox activity. While both electrolytes exhibit comparable performance at 298 K, the STD electrolyte experiences a sharp capacity decline as the temperature decreases. The DDL electrolyte, however, retains capacity more effectively at extremely low temperatures, mitigating key low-temperature challenges such as lithium plating, sluggish kinetics, and electrolyte freezing.
In LIBs, the diffusion coefficient of lithium ions is a critical factor affecting the battery performance. A higher diffusion coefficient generally indicates that ions can move more quickly within the electrode material, thereby enhancing the charge and discharge rates of the battery. By conducting CV experiments at different temperatures, we could calculate the apparent diffusion coefficient of the lithium ions. Additionally, the activation energies for lithium-ion diffusion in different electrolytes could be determined at various temperatures. As shown in Fig. 9, the migration activation energy for lithium ions in the STD electrolyte was 14.89 kJ/mol, whereas it was 9.58 kJ/mol in the DDL electrolyte. This indicated that lithium-ion diffusion was more favorable in the DDL electrolyte, enabling the battery to function properly at low temperatures while maintaining a higher capacity. Consequently, DDL electrolytes are suitable for low-temperature battery applications.

CONCLUSIONS

This study investigated the effect of molybdenum (Mo)-doping on the electronic structure of an electrode, thereby improving the electrode conductivity and increasing the battery capacity. This allowed the LIBs to maintain good charge and discharge capacities even at low temperatures, thereby broadening their application range. When the Mo-doping level was 0.02%, the battery exhibited its best specific capacity of 121.3 mAh/g. Next, we introduced a novel DDL electrolyte. Using this electrolyte, the battery capacity at 223 K remained at 61.6 mAh/g, approximately 60.22% of the initial capacity, and at 193 K, the battery capacity was 0.1 mAh/g, approximately 0.11% of the initial capacity. By calculating the activation energies for lithium-ion diffusion in different electrolytes, we found that the lithium ions in the DDL electrolyte exhibited a lower diffusion activation energy of 9.58 kJ/mol.

Notes

Author contributions

Mengmeng Chu performed the conceptualization, investigation, formal analysis, data curation, write-original draft, visualization. Man Li performed Software, formal analysis, data curation, and writing-review & Editing. Joonho Bae contributed for supervision, investigation, visualization, project administration, and fund acquisition.

ACKNOWLEDGEMENTS

This study was supported by the National Research Foundation of Korea (grant number: NRF-2021R1A2C1008272). This study was supported by the Gachon University Research Fund of 2021 (GCU-202110340001)

Fig. 1.
XRD spectra of (a) Li3V2 (PO4)3; (b)Li3V2-xMox(PO4)3 samples.
jecst-2025-00171f1.jpg
Fig. 2.
SEM images of (a) Li3V2(PO4)3; (b) Li3V1.98Mo0.02 (PO4)3, and (c) Li3V1.9Mo0.1(PO4)3 samples.
jecst-2025-00171f2.jpg
Fig. 3.
High-resolution TEM (HRTEM) images of Li3V1.9Mo0.1(PO4)3 samples.
jecst-2025-00171f3.jpg
Fig. 4.
XPS analysis of the Li3V2–xMox(PO4)3 cathode materials. (a) Li 1s XPS peak in LVP samples, (b) P 2p XPS peak in LVP samples, and (c) O1s and V 2p XPS peak in LVP samples. (d) Li 1s XPS peak in LVM0.02 P samples, (e) Mo 3d XPS peak in LVM0.02 P samples, (f) O1s and V 2p XPS peak in LVM0.02 P, and (g) P 2p XPS peak in LVM0.02 P.
jecst-2025-00171f4.jpg
Fig. 5.
CV curves for the commercial standard electrolyte (STD) and the novel DDL electrolyte.
jecst-2025-00171f5.jpg
Fig. 6.
(a) Galvanostatic charge-discharge curve using the battery analyzer within a voltage range of 3.0–4.3 V at 1 C rate in the DDL electrplyte; (b) Electrochemical voltage-composition curves of the Li3V2(PO4)3 sample in the 3.0–4.3 V range vs. Li+/Li.
jecst-2025-00171f6.jpg
Fig. 7.
CV curve of the Li3V2–xMox(PO4)3 cathode at a scan rate of 0.1 mV/s between 3.0 and 4.3 V vs. Li/Li+.
jecst-2025-00171f7.jpg
Fig. 8.
Electrolyte performance at low temperatures: (a) STD electrolyte; (b) DDL electrolyte.
jecst-2025-00171f8.jpg
Fig. 9.
Activation energy of the Li+ apparent diffusion coefficient for different electrolytes: (a) STD electrolyte; (b) DDL electrolyte.
jecst-2025-00171f9.jpg
Table 1.
Cell parameters of Li3V2–xMox(PO4)3 samples
x a (Å) b (Å) c (Å) β (0) V (Å3)
0 8.6056 8.5917 12.0370 90.609 897.7964
0.02 8.5978 8.5933 12.0327 90.496 896.0842
0.1 8.6201 8.6013 12.7645 90.000 893.3941
Table 2.
The XPS spectra about Li3V2(PO4)3 cathode
Name BE (eV) Atomic (%)
Li1s 55.53 13.84
P2p 133.69 7.77
C1s 284.46 42.66
V2p 517.18 2.59
O1s 531.56 33.14
Table 3.
The XPS spectra about Li3V1.98Mo0.02(PO4)3 cathode
Name BE (eV) Atomic (%)
Li1s 55.43 15.62
P2p 133.58 10.06
C1s 284.46 15.47
Mo3d 233.06 4.63
V2p 517.16 2.44
O1s 531.36 51.78
Table 4.
The ΔV for the Li3V2–xMox(PO4)3 batteries at different temperatures

ΔV (V)
T (K) LVM0.1P LVM0.02P
298 0.12 0.10
273 0.12 0.12
263 0.27 0.15
253 0.34 0.17
243 - 0.20
Table 5.
The DappLi+ for the Li3V2–xMox(PO4)3 batteries at different temperatures

DappLi+ (cm2/s)
T (K) LVM0.1P LVM0.02P
298 7.44×10-09 3.08×10-09
273 1.47×10-09 1.74×10-09
263 1.86×10-09 1.36×10-09
253 3.96×10-11 8.94×10-10
243 - 3.72×10-10
Table 6.
STD electrolyte performance at different temperatures.
Temperature (K) Capacity (mAh/g) Retention (%)
298K 115.0 100.00
273k 110.5 96.10
253K 99.6 86.60
243k 40.5 35.20
233K 9.0 7.80
Table 7.
DDL electrolyte performances at different temperatures.
Temperature (K) Capacity (mAh/g) Retention (%)
298 102.3 100.00
273 89.0 87.00
263 88.6 86.61
253 84.6 82.70
243 75.6 73.90
233 61.6 60.22
223 43.3 42.33
213 18.7 18.28
203 1.2 1.12
193 0.1 0.11

REFERENCES

[1] G. Cai, R. Guo, L. Liu, Y. Yang, C. Zhang, C. Wu, W. Guo and H. Jiang, J. Power Sources, 2015, 288, 136–144.
crossref
[2] N. Chen, C. Wang, F. Hu, X. Bie, Y. Wei, G. Chen and F. Du, ACS Appl. Mater. Interfaces, 2015, 7(29), 16117–16123.
crossref
[3] G. A. Elia, F. Nobili, R. Tossici, R. Marassi, A. Savoini, S. Panero and J. Hassoun, J. Power Sources, 2015, 275, 227–233.
crossref
[4] H. R. Jiang, Z. Lu, M. C. Wu, F. Ciucci and T. S. Zhao, Nano Energy, 2016, 23, 97–104.
crossref
[5] D. Mu, Y. Zhao, L. Yu, L. Liu and J. Xi, Phys. Chem. Chem. Phys., 2017, 19, 29195–29203.
crossref
[6] S. Li, X. Li, J. Liu, Z. Shang and X. Cui, Ionics, 2015, 21, 901–907.
crossref pdf
[7] W. Lin, M. Zhu, Y. Fan, H. Wang, G. Tao, M. Ding, N. Liu, H. Yang, J. Wu, J. Fang and Y. Tang, J. Alloys Compd., 2022, 905, 164163.
crossref
[8] Q. Liang, H. Yue, S. Wang, S. Yang, K. Lam and X. Hou, Electrochim. Acta, 2020, 330, 135323.
crossref
[9] D. Peng, J. Zhang, J. Zou, G. Ji, L. Ye, D. Li, B. Zhang and X. Ou, J. Clean. Prod., 2021, 316, 128098.
crossref
[10] X. Li, J. Zhang, D. Song, J. Song and L. Zhang, J. Power Sources, 2017, 345, 78–84.
crossref
[11] W.-J. Zhang, J. Power Sources, 2011, 196(6), 2962–2970.
crossref
[12] C. Qi, S. Wang, X. Zhu, T. Zhang, Y. Gou, Z. Xie, Y. Jin, Y. Wang, L. Song and M. Zhang, J. Alloys Compd., 2022, 924, 166612.
crossref
[13] A. Senyshyn, M. J. Mühlbauer, O. Dolotko and H. Ehrenberg, J. Power Sources, 2015, 282, 235–240.
crossref
[14] J. Jaguemont, L. Boulon and Y. Dubé, Appl. Energy, 2016, 164, 99–114.
crossref
[15] B. E. Worku, S. Zheng and B. Wang, Int. J. Energy Res., 2022, 46(11), 14609–14626.
crossref pdf
[16] P. Lyu, X. Liu, J. Qu, J. Zhao, Y. Huo, Z. Qu and Z. Rao, Energy Storage Mater., 2020, 31, 195–220.
crossref
[17] M.-T. F. Rodrigues, G. Babu, H. Gullapalli, K. Kalaga, F. N. Sayed, K. Kato, J. Joyner and P. M. Ajayan, Nat. Energy, 2017, 2, 17108.

[18] X. Yuan, Q. Xu, X. Liu, W. Shen, H. Liu and Y. Xia, Electrochim. Acta, 2016, 207, 120–129.
crossref
[19] M. Chen, P. Chen, F. Yang, H. Song and S. Liao, Electrochim. Acta, 2016, 206, 356–365.
crossref
[20] X. Wu, W. Wang and J. Du, Int. J. Energy Res., 2019, 44, 1775–1788.
crossref pdf
[21] T. Kazda, J. Vondrák, A. Visintin, M. Sedlaříková, J. Tichý and P. Čudek, J. Energy Storage, 2018, 15, 329–335.
crossref
[22] X. Ge, Y. Zhu, Z. Cao, J. Jia, Q. Zhao, S. Chang, S. Liu, X. Yang and K. Feng, J. Alloys Compd., 2022, 903, 163914.
crossref
[23] C. Liang, Y. Tao, N. Yang, D. Huang, S. Li, K. Han, Y. Luo, H. Chen and L. Mai, Electrochim. Acta, 2019, 311, 192–200.
crossref
[24] G. Qu, J. Wang, G. Liu, B. Tian, C. Su, Z. Chen, J.-P. Rueff and Z. Wang, Adv. Funct. Mater., 2018, 29(2), 1805227.

[25] J.-C. Zheng, X.-H. Li, Z.-X. Wang, H.-J. Guo, Q.-Y. Hu and W.-J. Peng, J. Power Sources, 2009, 189(1), 476–479.
crossref
[26] X. Rui, Q. Yan, M. Skyllas-Kazacos and T. M. Lim, J. Power Sources, 2014, 258, 19–38.
crossref


ABOUT
ARTICLE CATEGORY

Browse all articles >

BROWSE ARTICLES
AUTHOR INFORMATION
Editorial Office
E-mail: journal@kecs.or.kr    Tel: +82-2-568-9392               

Copyright © 2026 by The Korean Electrochemical Society.

Developed in M2PI

Close layer
prev next