Promoted de-solvation effect and dendrite-free Zn deposition enabled by in-situ formed interphase layer for high-performance zinc-ion batteries
Abstract
The use of aqueous electrolytes and Zn metal anodes in Zn-based energy storage systems provides several benefits, including competitive energy density, excellent safety, and low cost. However, Zn dendrites growth and slow ion transfer at the electrode/electrolyte interphase reduce the cycle stability and rate capability of the Zn anode. Herein, the V2O5-x interface layer was rationally and controllably constructed on the Zn surface through in situ spontaneous redox reaction between V2O5 and the Zn anode. The V2O5-x interface layer, with an optimized thickness, plays a crucial role in ion screening and de-solvation, leading to a uniform dispersion of Zn2+ ions and dendrite-free morphology. Moreover, as Zn2+ transports through the V2O5-x interface layer, the V element in a
Keywords
INTRODUCTION
With the large-scale and efficient use of renewable energy such as solar and wind energy, there is an urgent need to develop low-cost, high-safety and high-performance energy storage devices as intermediate media for power transmission[1-3]. Due to the use of aqueous electrolytes, aqueous rechargeable batteries have the benefits of being inexpensive, safe, non-flammable, and environmentally friendly[4-7]. Among them, aqueous Zn-ion batteries (AZIBs) are thought to be a promising kind of rechargeable battery for large-scale applications because of their affordable water electrolyte and manufacturing process, safety, and plentiful Zn resources[8,9]. Unfortunately, the following factors are the principal hindrances to the practical application of Zn metal anodes: growth of Zn dendrites, parasitic reactions, and sluggish transport kinetics[10-12]. Numerous pits on the rough surface of commercial Zn foil result in the unequal distribution of the electric field[13,14].
To address the aforementioned issues, various strategies have been developed to stabilize the Zn anode, including electrolyte modification, structural design, and interface layer construction[27-29]. Among these, the introduction of an interface layer is considered more promising than the other two methods[30-32]. The interface layer not only physically isolates Zn metal from the aqueous electrolyte to inhibit side reactions, but also offers great possibilities for regulating Zn deposition behavior due to its diversity of materials and functions[33-35]. For example, different oxides including ZnO[36], CeO2[37], WO3[38], and MoO3[39] have been used as interfacial materials and have been shown to be effective in Zn anode stabilization. However, it is important to note that most reported interfacial protective layers are quite thick, typically ranging from 5 to 25 μm, to maintain membrane integrity and ensure complete isolation of Zn from the electrolyte
Inspired by this, a thin V2O5-x protective layer was constructed on the surface of the Zn anode by a simple chemical reduction method (designated as V@Zn). By altering the reaction time, the thickness of the protective layer (220 nm, 320 nm, 615 nm) can be precisely controlled. The optimized thickness of the protective layer can prevent direct contact between the electrolyte and Zn metal anode, and demonstrated a de-solvation effect, which effectively promotes the uniform deposition of Zn2+ and inhibits dendrite formation. In addition, the low-valent V element in the protective layer promotes the combination of oxygen anion and Zn2+, forming an efficient Zn2+ transport channel and accelerating the ion transport process. As a result, the symmetrical V@Zn//V@Zn cell demonstrates an ultra-long life of 1400 h at a current density of 1 mA cm-2 with a capacity of 1 mA h cm-2. Moreover, a full cell consisting of a V@Zn anode and a V2O5 cathode shows improved capability and cycling stability.
EXPERIMENTAL
Preparation of V@Zn electrodes
First, 0.6 g of V2O5 was added to 50 mL of deionized water. Then, 8 mL of H2O2 was poured in and stirred for 30 min. The mixture was introduced to the reactor and heated for 6 h at 190 °C to yield the V2O5 solution. After that, a 0.05 mm thick Zn foil with polyimide tape on one side was immersed in the prepared 10 mL of V2O5 solution (0.5 mg mL-1) and left for a certain period of time (1, 5, 10 min) to control the thickness of the V2O5-x layer. Finally, the V@Zn was obtained by rinsing with deionized water and drying overnight in a vacuum oven at 80 °C for 8 h.
X-ray photoelectron spectroscopy (XPS, Perkin Elmer PHI 1600 ESCA) was used to analyze the composition and chemical state of the samples. The microstructure of the specimen was studied using scanning electron microscopy (SEM, SUPRA 55). Elemental analysis of SEM results was obtained using energy dispersive spectrometer (EDS). The wettability of the electrode in the Zn(CF3SO3)2 electrolyte was determined using a JC2000C contact angle measurement equipment (POWER EACH, China). Electron paramagnetic resonance (EPR) spectroscopic measurements were performed with a Bruker EMXplus-6/1.
Electrochemical measurements
The CR2032 coin battery was assembled for constant current and CE testing. The CE test was conducted using a charge cut-off voltage of 0.5 V. All tests were performed using Land CT2100A and an electrochemical workstation CHI660E. Symmetrical batteries were assembled using two Zn anodes with a diameter of 1 cm. The half-cell was built with Zn foil as the negative electrode and tested for CE and nucleation overpotential. Zn//Cu and V@Zn//Cu cells were assembled and tested for hydrogen evolution curves at an electrochemical workstation (CHI660E). The V2O5 powder was combined with polyvinylidene fluoride (PVDF) and carbon black in N-methyl pyrrolidone (NMP) at a mass ratio of 7:2:1 to create a uniform slurry. The paste is then coated on a stainless-steel mesh and dried in a vacuum oven at 60 °C for 10 h to obtain the cathode. For three-electrode systems, bare Zn or V@Zn is the working electrode and platinum (Pt) foil is the counter-electrode, while Hg/HgCl is the reference electrode. A 3 M Zn(CF3SO3)2 aqueous solution was chosen as the electrolyte for the assembly of V@Zn//V2O5 full cells. V@Zn, V2O5 and filter paper act as anodes, cathodes and separators, respectively. Activation for five cycles at a low current of 1 A g-1 before cycling is used. Cyclic voltammetry (CV) and electrochemical impedance spectroscopy (EIS) were tested using the electrochemical workstation (CHI660E). The voltage window of CV was 0.3~1.6 V, and the frequency range of EIS was 100 kHz and 0.01Hz.
RESULTS AND DISCUSSION
The structural and dendritic evolution of the electrode surface following the initial plating and cyclic stages is depicted in the schematic diagram of Figure 1. Due to the uneven deposition of Zn2+, some small protrusions formed on the bare Zn surface. After several cycles, the electron attraction is high at the protrusion due to the tip effect, leading to a large amount of Zn2+ deposition[52,53]. After that, the protrusions evolved into Zn dendrites [Figure 1A]. In addition, due to chemical reactions and Zn surface roughness, continuous corrosion begins as soon as the Zn anode comes into contact with the weakly acidic electrolyte. This process consumes both the Zn anode and the electrolyte, producing insulating by-products and hydrogen gas (H2) [Supplementary Figure 1]. Moreover, the competitive hydrogen evolution reaction (HER) during the recharging process not only directly lowers CE but also accelerates H2 generation and increases the local pH. These effects lead to elevated internal pressure and intensified parasitic reactions. In contrast, a uniform electric field and homogeneous distribution of Zn2+ flux was enabled on the surface because of the introduction of the V2O5-x interface interlayer, resulting in uniform deposition of Zn [Figure 1B]. Moreover, the contact between Zn and the electrolyte is effectively blocked, thereby suppressing side reactions.
Figure 1. Diagrammatic representation of the surface-structure differences between the (A) bare Zn electrodes and (B) the V@Zn electrodes.
The V@Zn anode was prepared using a simple in situ chemical reduction method [Figure 2A]. The
Figure 2. (A) Schematic diagram of V@Zn fabricating; Top-view SEM pictures of the bare Zn foil (B) and V@Zn (C and D); (E) SEM image of V@Zn and corresponding elemental maps. SEM: Scanning electron microscopy.
V@Zn electrodes were obtained by immersing Zn in 0.5 mg mL-1 V2O5 solution for 1 min, 5 min and
Figure 3. Bare Zn and V2O5-x protective layer V@Zn after 1, 5 and 10 min reaction, respectively. (A-C) Thickness of the V2O5-x interface layer; (D) the magnified voltage-time profiles from 200 h to 210 h; (E) long cycle stability testing; (F) contact angle measurement.
The compatibility between the electrode surface and the electrolyte was investigated by a contact angle experiment. The contact angles of the 3 M Zn(CF3SO3)2 solution with bare Zn and different V@Zn anodes were 83.7°, 45.1°, 26°, and 25.6°, respectively [Figure 3F]. This indicates that the V2O5-x film improves the wettability of the electrolyte, facilitating Zn-ion transport due to the easy access of the Zn2+ in the electrolyte. In summary, the 320 nm-thick V2O5-x interface layer shows the best stabilization effect and was used for further battery performance evaluation.
In addition to enhancing the plating/stripping kinetics of Zn2+, the V2O5-x layer is also crucial for adjusting Zn nucleation and enabling uniform Zn deposition. The nucleation overpotential of V@Zn was measured at various current densities in order to demonstrate the function of the V2O5-x layer in controlling Zn nucleation behavior [Supplementary Figure 8]. Apparently, the nucleation overpotential of the V@Zn
The current-time curve, as presented in Supplementary Figure 9, shows both the nucleation process and surface variations of the Zn anode[54]. When the -150 mV overpotential is applied, the current of bare Zn continues to decrease for 150 s, showing that the two-dimensional diffusion process is prolonged and Zn deposition remains uncontrolled. During charging and discharging, Zn2+ tends to concentrate at the electrode tip, reducing surface energy and speeding dendrite formation on the electrode surface. In contrast, the initial Zn nucleation and two-dimensional diffusion process of the V@Zn reached a stable
To further investigate cycling performance, symmetrical cells with bare Zn or V@Zn electrodes were built, and charged/discharged tests at various current densities were conducted. Figure 4A and B shows that at a current density of 3 mA cm-2, the symmetrical cell V@Zn//V@Zn has a stable cycle life and voltage distribution over 700 h. On the other hand, the initial polarization voltage of a bare Zn//Zn symmetrical battery is around 55 mV at the start of the cycle, and severe polarization occurs at 120 h. Even at 5 mA cm-2 current density, V@Zn//V@Zn cells can sustain nearly 320 h [Figure 4C]. In contrast, Zn//Zn cells undergo a short circuit after 175 h. Different current densities were used to investigate the magnification capabilities of V@Zn and bare Zn [Figure 4D]. At varying current densities, the V@Zn clearly shows lower polarization voltages than bare Zn. Therefore, it was proved that the V2O5-x layer could lower the polarization voltage of the cell and effectively induce uniform Zn2+ deposition and inhibit the growth of Zn dendrites[55,56].
Figure 4. Electrochemical characteristics of symmetric Zn and V@Zn cells. (A) cycling performance at 3 mA cm-2; (B) the magnified graph of the long-cycling voltage profiles, which spans 40 h to 50 h; (C) cycling performance at 5 mA cm-2; (D) rate curves.
In order to further illustrate the effect of V2O5-x layer on the reversibility of Zn plating/stripping, the CE of Zn//Ti asymmetric cells was also studied. As shown in Figure 5A-C, the CE and constant current
Figure 5. (A) Coulombic Efficiency comparison at 3 mA cm-2; (B) Voltage profiles at the 50th cycle of Zn plating/stripping of V@Zn and bare Zn at 3 mA cm-2; (C) Coulombic Efficiency comparison at 2 mA cm-2; (D) The CV diagram tested at 0.1 mV s-1; EIS of the Zn foil (E) and the V@Zn electrode (F) at different temperatures; (G) The calculated de-solvation activation energies of both electrodes by using the Arrhenius equation. CV: Cyclic voltammetry; EIS: Electrochemical impedance spectroscopy.
In addition, direct evidence of uniform Zn deposition of V2O5-x layers was obtained from in-situ optical visualization observations[57,58]. An in-situ optical system operating at 5 mA cm-2 was utilized to conduct Zn plating tests in order to investigate the effect of the V2O5-x-protective technique on dendrite formation. During the plating process, the surface of the V@Zn remains smooth at covered time [Figure 6A]. In contrast, some small protrusions appeared on the surface of bare Zn as early as 15 min, and gradually evolved into Zn dendrites. SEM was used to observe the bare Zn and V@Zn electrodes after 50
Figure 6. (A) 100 μm scale bar represents light microscopic pictures of Zn deposition on bare Zn and V@Zn surfaces; The SEM pictures of (B) bare Zn and (C) V@Zn after 50 cycles at 1 mA cm-2; (D) V 2p spectra of the V@Zn electrodes in pristine, discharged and charged states. SEM: Scanning electron microscopy.
The full cell (Zn//V2O5 and V@Zn//V2O5) was built for electrochemical performance testing to evaluate the effect of the V@Zn anode. The CV curve shows a pair of redox peaks, indicating the insertion/extraction reaction of Zn2+ or H+ [Figure 7A]. Furthermore, the gap (0.12 V) between the redox and A1/B1 peaks of V@Zn//V2O5 was less than that of the redox peaks of bare Zn//V2O5 (0.19 V), indicating that the V2O5-x interface layer on the Zn anode enables superior electrochemical activity. In addition, EIS testing is also used to verify the reaction kinetics effect of the V2O5-x layer on the cell. V@Zn//V2O5 has a small charge transfer resistance. In Zn//V2O5, it is shown that the V2O5-x coating improves the kinetics of the cell
CONCLUSIONS
A V2O5-x layer is in situ grown on the surface of Zn foil by a simple chemical reduction method to guide uniform Zn deposition during plating/stripping process thus preventing the growth of Zn dendrite. In addition, the interface layer can be coordinated with Zn2+, which promotes the de-solvation effect, and can be used as a physical barrier to avoid direct contact between the electrolyte and the Zn anode, reducing the occurrence of side reactions. Therefore, symmetrical cells based on V@Zn anodes exhibit low hysteresis voltage and long cycle life. In addition, the V@Zn//V2O5 full cell shows a capacity of 275.9 mA h g-1 after 2,500 cycles, demonstrating excellent cycling stability. Therefore, this work is expected to open up new avenues for the development of high-performance zinc-ion batteries.
DECLARATIONS
Authors’ contributions
Investigation, writing-original draft: Sun, B.
Investigation: Sun, B.; Wang, X.
Supervision, writing - review and editing: Lu, Q.; Wang, X.; Xiong, P.
Availability of data and materials
The data that support the findings of this study are available from the corresponding author upon reasonable request.
Financial support and sponsorship
This work is supported by the National Natural Science Foundation of China (grant no. 22005156), Joint Fund of Henan Province Science and Technology R&D Program (grant no. 225200810093), Science and Technology Development Project of Henan Province (grant no. 242102241042) and Startup Research of Henan Academy of Sciences (grant no. 231817001).
Conflicts of interest
All authors declared that there are no conflicts of interest.
Ethical approval and consent to participate
Not applicable.
Consent for publication
Not applicable.
Copyright
© The Author(s) 2025.
Supplementary Materials
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How to Cite
Song, B.; Lu, Q.; Wang, X.; Xiong, P. Promoted de-solvation effect and dendrite-free Zn deposition enabled by in-situ formed interphase layer for high-performance zinc-ion batteries. Energy Mater. 2025, 5, 500031. http://dx.doi.org/10.20517/energymater.2024.182
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