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Communication  |  Open Access  |  27 Aug 2025

Fe3+-driven tunnel engineering for stabilizing metastable ramsdellite MnO2 in high-performance zinc-ion batteries

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Energy Mater. 2025, 5, 500142.
10.20517/energymater.2025.113 |  © The Author(s) 2025.
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Abstract

Ramsdellite MnO2 (R-MnO2), with its expanded (1 × 2) tunnels, offers superior Zn2+ diffusion kinetics for aqueous zinc-ion batteries but suffers from metastability-induced phase collapse. Herein, Fe3+ doping is demonstrated as a critical strategy to thermodynamically stabilize R-MnO2 while optimizing its electrochemical functionality. Through a synergistic H+/Fe3+ hydrothermal process, spent ZnMn2O4 from alkaline batteries is converted into orthorhombic R-FexMn1-xO2 nanocrystals. Fe3+ incorporation enlarges the tunnel structure, reduces surface energy, and mitigates Jahn-Teller distortion by increasing the Mn4+/Mn3+ ratio. This yields a high specific surface area, enhanced ion diffusion kinetics, and exceptional cycling stability. The R-FexMn1-xO2 cathode achieves a 286.8 mAh g-1 capacity at 0.1 A g-1, outperforming β-MnO2 (30.9 mAh g-1 at 1.5 A g-1). This work establishes Fe3+ doping as an essential mechanism for stabilizing high-performance metastable cathodes, enabling sustainable upcycling of battery waste.

Keywords

Ramsdellite MnO2, zinc-ion batteries, energy density, chemical and electrochemical stability

INTRODUCTION

Aqueous zinc-ion batteries (AZIBs) have attracted significant attention due to their high safety, low cost, and environmentally friendly characteristics[1-3]. Among previously reported cathode materials, Mn-based oxides have become promising cathode materials for AZIBs due to their advantages in safety and high theoretical capacity. Mn-based materials from spent alkaline batteries (SABs) share chemical homology with AZIB cathodes, enabling resource regeneration from spent batteries into high-performance AZIBs[4,5]. On the other hand, the casual discarding of SABs inevitably leads to the leakage of heavy metals such as zinc (Zn) and manganese (Mn), posing potential threats to the ecological balance and human health, thereby making the recycling and safe disposal of SABs imperative[6].

Manganese dioxide (MnO2) exhibits various phases in aqueous environments, including β-MnO2, α-MnO2, R-MnO2 (ramsdellite-MnO2), δ-MnO2, λ-MnO2, and γ-MnO2. While β-MnO2 demonstrates phase stability, it is limited by its (1 × 1) narrow tunnel structure; conversely, R-MnO2 with (1 × 2) expanded tunnels significantly improves Zn2+ diffusion kinetics[7-9]. Recently, our group investigated the recycling and synthesis of β-MnO2 from SABs through hydrochloric acid hydrothermal treatment[10]. Previous studies show that highly reactive R-MnO2 forms initially during hydrothermal processing, but metastable R-MnO2 transforms rapidly into β-MnO2 with longer treatment or at high temperatures[11]. β-MnO2 hinders H+/Zn2+ extraction/insertion due to its narrow tunnels[12]. In contrast, (1 × 2) tunnels in R-MnO2 enhance ion insertion kinetics[13]. Huang et al. synthesized an R-MnO2-based composite material with supercapacitor characteristics and excellent electrochemical performance[14]. Chen et al. prepared R-MnO2 through the low-valent ion doping; the material exhibits high oxygen vacancy concentration, further improving the electrical conductivity and reactivity[15]. Nevertheless, traditional synthesis methods face challenges in producing stable R-MnO2, necessitating controllable and convenient strategies for its preparation[16,17].

Meanwhile, challenges remain; lattice collapse of metastable phases (e.g., R-MnO2) during ion insertion causes pulverization of cathode materials. Over the years, much research has employed multidimensional regulation strategies, including ionic doping, surface engineering, and defect engineering, to optimize the physicochemical properties of materials[18]. Pan et al. synthesized Fe-MnO/C via annealing to achieve an MnO crystal structure and demonstrated that Mn-O-Fe bond formation promotes charge transfer kinetics while mitigating structural collapse, thereby synergistically improving rate capability and cycling stability[19]. Zhong et al. showed that iron doping effectively mitigates the Jahn-Teller effect, stabilizes lattice water, and prevents lattice collapse, thus regulating the layered structure in AZIBs[20]. Although ionic doping is widely utilized to stabilize MnO2, the stabilization of metastable phases during synthesis remains underexplored[21,22].

Herein, we demonstrate that Fe3+ doping acts as a dual-function regulator by thermodynamically stabilizing R-MnO2 through reduced surface energy and enlarged (1 × 2) tunnels, while kinetically enhancing Zn2+ diffusion via optimized Mn4+/Mn3+ ratios that suppress Jahn-Teller effects. Through a synergistic H+/Fe3+ hydrothermal process, spent ZnMn2O4 waste is successfully converted into stable R-FexMn1-xO2 nanocrystals, achieving retention of the metastable R-phase, a high surface area of 218 m2 g-1, and low charge-transfer resistance. Electrochemical performance reaches 286.8 mAh g-1 at 0.1 A g-1 with 88.9% capacity retention after 1000 cycles. This study establishes Fe3+ doping as a universal design principle for metastable functional materials, offering simultaneous advancements in AZIB cathode engineering and sustainable battery upcycling.

EXPERIMENTAL

Materials

The materials used in this study include Nanford alkaline batteries (spent battery, LR6-2B/1.5V), potassium hydroxide (KOH, AR), hydrochloric acid (HCl, AR), Sulfuric acid (H2SO4, AR, 98 wt.%), N-methyl pyrrolidone (NMP, AR), and polyvinylidene fluoride (PVDF, AR).

Preparation of materials from spent alkaline batteries

Used Nanford alkaline batteries were further discharged to 0.8 V using a Neware Battery Test System (CT-4000). The discharged batteries were manually disassembled to collect cathode materials for further processing. The cathode powder was stirred in 0.1 M KOH solution for over 30 minutes to remove residual adhesives and alkaline compounds. The mixture was filtered and sequentially washed with 0.01 M H2SO4 solution, deionized (DI) water, and ethanol. The resulting precipitate was dried under vacuum at 60 °C, yielding brown-black Spent Materials (SABs).

Synthesis of β-MnO2 and R-FexMn1-xO2

Firstly, 0.9 g of SABs powder was dispersed in 66 mL of DI water. Then, 4 mL of concentrated hydrochloric acid (AR, 37 wt.%) was added dropwise. Subsequently, 0.2g Fe2(SO4)3 was added under continuous stirring at 20 °C for 30 min. The mixture was then transferred to a 100 mL hydrothermal reactor and reacted at 140 °C for 12 h. The product was washed with DI water and dried in a vacuum oven at 60 °C to obtain R-FexMn1-xO2. When Fe2(SO4)3 was omitted during stirring, β-MnO2 was obtained.

Characterizations

The materials were further characterized using an X-ray diffraction (XRD, Cu Kα, Bruker D8 Advanced, λ = 1.5481 Å) to obtain their structural information. The morphology and microstructure were examined using Scanning Electron Microscopy (SEM, FEI Quanta FEG 250) and Transmission Electron Microscopy (TEM, JEOL 2100). The selective area electron diffraction (SAED) patterns were employed to examine the polycrystalline nature of the materials. The surface elemental properties of the samples were analyzed using an X-ray Photoelectron Spectrometer (XPS, Thermo Fisher Scientific K-Alpha) with an Al Kα X-ray excitation source. The N2 adsorption/desorption isotherm was measured using ASAP 2460 at 77 K, and the specific surface area was determined using the Brunauer-Emmett-Teller (BET) method.

Electrochemical measurement

The active materials (β-MnO2 and R-FexMn1-xO2), carbon black, and PVDF were uniformly mixed at a 7:2:1 mass ratio. The resulting slurry was coated onto stainless steel foil with mass loading of 0.8~1.2 mg cm-2 and vacuum-dried. The 2032 button cells were assembled using zinc foil anode and glass fiber filter (Whatman GF/D grade) as a separator. The electrolyte was a mixed solution of ZnSO4 (3 M) and MnSO4 (0.05 M). The electrochemical performance was evaluated using a Neware Battery Test System (CT-3008). Cyclic voltammetry (CV) was conducted on a CHI 760E electrochemical station, while electrochemical impedance spectroscopy (EIS) was recorded on a DH7000D electrochemical station.

Computational details

In order to study the mechanism of the reconstruction process, density functional theory (DFT) calculations were used to determine the surface energies of the exposed crystal surfaces R-FexMn1-xO2 (210), β-MnO2 (110) and R-MnO2 (210) to evaluate the stability differences of various crystalline phases of MnO2. We established R-FexMn1-xO2, R-MnO2 and β-MnO2 cluster models using the commercially available software, Materials Studio 2020. The Castep module was employed to perform the geometry optimization step and the corresponding calculation program of the models. The smooth part of the wave function was expanded and the kinetic energy cut-off was 500 eV. The relaxation convergence criteria for structural optimization were a maximum displacement of 1.0 × 10-3 Å and a maximum force of 0.03 eV Å-1.

RESULT AND DISCUSSION

R-FexMn1-xO2 was synthesized via a pretreatment of SABs (sequential cleaning with mixed alkali solutions and acid solutions) followed by a 12 h hydrothermal reaction at 140 °C co-induced by H+ and Fe3+, while β-MnO2 was prepared identically without the addiction of Fe3+ [Figure 1A]. SEM images and XRD patterns [Figure 1B-D and Supplementary Figures 1-4] reveal the overall morphology of the original SABs and Mn-based materials. β-MnO2 exhibits a regular granular structure, while R-FexMn1-xO2 displays irregular shapes with numerous adhered and agglomerated small particles. XRD analysis revealed that [Figure 1C] all the diffraction peaks of R-FexMn1-xO2 correspond to R-MnO2 (JCPDS #42-1316), demonstrating the stability of the R-MnO2 structure upon Fe3+ doping. In contrast, β-MnO2 was identified as rutile type (JCPDS #24-0735). Although R-MnO2 is generally metastable, Fe3+ doping stabilized the main R-MnO2 phase in R-FexMn1-xO2 using this synthesis method. To validate the hydrothermal regeneration pathway and the phase transformation, comprehensive materials characterization was conducted. Combined with the material source and characterization results in Supplementary Figure 2, we confirmed the presence of impurities including Zn, C, and organics in the raw materials. During pretreatment steps, Zn and organics were effectively removed, while trace residual organics underwent carbonization during the hydrothermal process, resulting in conductive carbon that does not compromise material performance. BET surface area analysis [Figure 1E, Supplementary Figure 1C and D] demonstrated a substantial increase in specific surface area (from 78.78 m2 g-1 to 218.01 m2 g-1) and higher mesopore volume for R-FexMn1-xO2 compared to β-MnO2. Combined with Rietveld refinement of XRD patterns, the breaking of the long-range crystal order reduced particle size, enhanced specific surface area, and enlarged pore volume of R-FexMn1-xO2, establishing abundant active sites for H+/Zn2+ extraction/insertion.

Fe<sup>3+</sup>-driven tunnel engineering for stabilizing metastable ramsdellite MnO<sub>2</sub> in high-performance zinc-ion batteries

Figure 1. (A) Schematic illustration of the phase evolutions from SABs to β-MnO2 and R-FexMn1-xO2; SEM image and BET surface area of (B) β-MnO2 and (D) R-FexMn1-xO2 (x≈3 wt.%); (C) XRD patterns; (E) N2 adsorption/desorption isotherms and corresponding pore size distributions (inset); (F) Fe 2p XPS spectra; (G) Surface morphology and surface quantities of the pristine surface. SEM: Scanning electron microscopy; BET: brunauer-emmett-teller; XPS: X-ray photoelectron spectrometer; SABs: spent alkaline batteries; XRD: X-ray diffraction.

High-resolution XPS analysis of the Fe 2p in R-FexMn1-xO2 revealed a characteristic spin-orbit splitting energy of 13.9 eV between Fe 2p1/2 and Fe 2p3/2 peaks, confirming iron predominantly exists as Fe3+ [Figure 1F][23]. Through Fe3+ doping, the Mn 2p spectra exhibited two peaks at 642.28 eV and 653.68 eV, which correspond to the characteristic peaks of Mn4+ in MnO2[24]. Meanwhile, peak area analysis revealed R-FexMn1-xO2 had a higher Mn4+ content (75%) than β-MnO2 (60%), which is anticipated to effectively mitigate Jahn-Teller distortion, reduce Mn3+ disproportionation, and enhance conductivity [Supplementary Figures 5 and 6]. The O 1s spectra indicated greater O vacancy concentration in R-FexMn1-xO2, facilitating rapid electron transfer. As potent defects, these oxygen vacancies significantly disrupt the lattice and inhibit crystal growth, which also contributed to enhanced nanoscale refinement of the material[25]. DFT calculations [Figure 1G and Supplementary Figure 7] demonstrated that Fe3+ doping reduces surface energy (favoring the formation of R-FexMn1-xO2), enhances the surface thermodynamic stability of R-MnO2, significantly releases lattice stress, modifies the anisotropy of crystal growth and improves ion transport kinetics.

TEM analysis provided detailed elucidation of the material’s morphological characteristics. Figure 2A and B corroborated the morphological features observed by SEM. Compared with β-MnO2 [Supplementary Figure 8]; the particle dimensions of R-FexMn1-xO2 were significantly reduced, consistent with the BET surface area analysis results. SAED and High-Resolution Transmission Electron Microscopy (HRTEM) patterns verified the polycrystalline nature of R-FexMn1-xO2. SAED exhibited well-defined diffraction spots corresponding to the characteristic R-MnO2 (020) and (210) planes, confirming complete phase transformation to R-MnO2 [Figure 2B3][26]. The HRTEM image of R-FexMn1-xO2 clearly shows lattice fringes of (400) (d = 0.24 nm) and (211) (d = 0.22 nm), forming an included angle of 61.8° and it can be assigned to R-MnO2[27]. In contrast, β-MnO2 shows lattice fringes of 0.22 nm (200) and 0.21 nm (111) with θ = 47.7° [Figure 2A]. These results were consistent with XRD patterns and confirm the structure of R-FexMn1-xO2, which facilitates the insertion/extraction of Zn2+ compared to β-MnO2. EDS analysis [Figure 2C] demonstrated the presence of C, Mn, O and Fe elements, with no detectable Zn, confirming the formation of homogeneous Fe3+-doped R-FexMn1-xO2, which regulates the lattice structure and optimizes ion diffusion.

Fe<sup>3+</sup>-driven tunnel engineering for stabilizing metastable ramsdellite MnO<sub>2</sub> in high-performance zinc-ion batteries

Figure 2. The TEM and HRTEM images with corresponding SAED images of (A) β-MnO2, (B) R-FexMn1-xO2. (C) corresponding elemental mapping images of R-FexMn1-xO2 powders. TEM: Transmission electron microscopy; HRTEM: high-resolution transmission electron microscopy; SAED: selective area electron diffraction.

To verify the role of Fe3+ doping in enhancing electrode stability and reaction kinetics, we assembled coin cells to evaluate the electrochemical performance of the materials.

We systematically evaluated the effect of Fe3+ feeding amount on the electrode materials and found that the optimal electrochemical performance was achieved at a Mn:Fe feeding ratio of 100:5 [Supplementary Figures 9-11]. Figure 3A shows the cycling performance of the β-MnO2 and R-FexMn1-xO2 electrodes. The results demonstrate enhanced cycling stability for R-FexMn1-xO2 cathodes compared to β-MnO2 cathodes. At 1.0 A g-1, the R-FexMn1-xO2 cathode exhibited specific capacity of 161.9 mAh g-1 and achieved 88.9% capacity retention after 1000 cycles. In contrast, the β-MnO2 cathode showed a specific capacity of 52.58 mAh g-1 and retained only 48.8 % after cycling [Figure 3A]. The superior cycling capability of R-FexMn1-xO2 can be attributed to Fe3+ doping, which optimizes ion diffusion pathways and enhances the stability of Mn-O bonds (~1.91 Å) through substitution with shorter Fe-O bonds (~1.89 Å). Additionally, the R-FexMn1-xO2 cathodes demonstrated much better rate performance than β-MnO2 cathodes [Figure 3B and Supplementary Figure 11], delivering specific capacities of 286.8, 269.7, 248.5, 206.8, and 163.3mAh g-1 at current densities of 0.1, 0.2, 0.5, 1.0, and 1.5 A g-1, respectively. The β-MnO2 exhibited poor rate capability, achieving only 30.9 mAh g-1 at 1.5 A g-1. Figure 3C illustrates the galvanostatic charge-discharge curve (GCD) profiles of R-FexMn1-xO2 and β-MnO2 cathodes at various current densities. Notably, as current density increased, the second discharge platform below 1.3V [Figure 3C] in β-MnO2 cathodes gradually diminished. Conversely, R-FexMn1-xO2 maintained better plateau retention at high rates, contributing more significantly to the overall capacity.

Fe<sup>3+</sup>-driven tunnel engineering for stabilizing metastable ramsdellite MnO<sub>2</sub> in high-performance zinc-ion batteries

Figure 3. Electrochemical performance of β-MnO2 and R-FexMn1-xO2 cathodes of (A) cycling performance [Coulombic Efficiency (CE)]; (B) rate capabilities; (C) The GCD curves; (D) GITT profiles and corresponding ion diffusion coefficients of AZIBs; (E) CV curves at scan rate of 0.1 mV s-1. (F) radar chart comparing properties of Mn-based cathodes for AZIBs. GCD: Galvanostatic charge-discharge; GITT: galvanostatic intermittent titration technique; AZIBs: aqueous zinc-ion batteries; CV: cyclic voltammetry.

Furthermore, Galvanostatic Intermittent Titration Technique (GITT) was employed to evaluate Zn2+/H+ diffusion kinetics. The GITT curves for β-MnO2 and R-FexMn1-xO2 cathodes, along with the corresponding diffusion coefficients (D) were presented in Figure 3D. The D value was calculated using $$ \mathrm{D}_{\mathrm{Zn}^{2+}}=\frac{4}{\pi \iota }\left(\frac{\mathrm{n}_{\mathrm{M}}\mathrm{~V}_{\mathrm{M}}}{\mathrm{~s}}\right)^{2}\left(\frac{\Delta \mathrm{Es}}{\Delta \mathrm{Et}}\right)^{2} $$. (D: diffusion coefficients; ι: the relaxation time; nM: the number of moles; VM: molar volume of the electrode material; S: the electrode/electrolyte contact area; ΔEs: the voltage change induced by the pulse; ΔEt: the voltage change during galvanostatic charge/discharge). The R-FexMn1-xO2 cathodes exhibited significantly higher ion diffusion coefficients throughout the entire discharge process. This kinetic advantage correlates with the stabilized (1 × 2) tunnel structure and optimized cation diffusion pathways of R-FexMn1-xO2. Besides, CV profiles at 0.1 mV s-1 [Figure 3E] revealed larger redox peaks for the R-FexMn1-xO2 cathode, indicating higher electrochemical activity. More stable redox profiles demonstrated better reversibility, attributed to enhanced mechanical stability of ion transport channels by Fe3+ doping. The peak splitting observed in the CV curves at 1.60-1.65 V is influenced by the Zn2+/H+ co-insertion mechanism. This peak splitting originates from the energy barrier differences between H+ and Zn2+ deintercalation pathways, which leads to divergent transport kinetics and stepwise oxidation processes. In addition, the R-FexMn1-xO2 showed smaller ΔE values between redox peaks, signifying superior electrochemical reversibility, reduced polarization, improved energy retention, and enhanced overall efficiency. Collectively, the cathode material obtained in this work exhibits superior overall performance [Figure 3F and Supplementary Table 1].

These findings suggest that Fe3+ doping stabilizes the R-MnO2 structure, forming the R-FexMn1-xO2 cathode, which not only alleviates lattice strain to enhance structural resilience against H+/Zn2+ extraction/insertion during cycling but also accelerates reaction kinetics. To figure out the structural transitions and reversibility, in situ XRD analysis was performed on the R-FexMn1-xO2 cathode [Supplementary Figure 12]. During discharge, new diffraction peaks emerged corresponding to Zn4SO4(OH)6·5H2O (JCPDS #039-0688), attributed to precipitation involving dissolved H+ ions from the electrolyte. These peaks disappeared during charging. Notably, the peak intensities of R-MnO2 remained basically unchanged throughout the cycling process, confirming the structural stability of R-FexMn1-xO2 under electrochemical operation.

By plotting i/v1/2 versus v1/2 [i(V) = k1v1/2 + k2v] at different potentials, the values of k1 were obtained to calculate the percentage of capacitance contribution. The capacitive contribution for the R-FexMn1-xO2 electrode increased gradually from 47% to 87%, while ranging between 33% and 73% for the β-MnO2 electrode [Figure 4A and Supplementary Figure 13], demonstrating the relatively higher capacitance contribution of R-FexMn1-xO2 cathode[28]. Thus, the enhancement stems from the Fe3+-induced porous nanostructure of R-FexMn1-xO2, which increases the specific surface area and provides additional active sites for faradic reactions, thereby improving surface pseudo-capacitance. Post-cycling XPS analysis [Figure 4B and Supplementary Figure 14] revealed higher Mn4+ content in R-FexMn1-xO2 compared to β-MnO2. This effectively suppresses the Mn3+ proportion, mitigating Jahn-Teller distortion-induced manganese dissolution and enhancing capacity retention. The O 1s spectra showed significantly intensified H-O-H peaks in cycled R-FexMn1-xO2, indicating guest-bonded water that provides shielding by reducing positive charge density at vertex oxygen sites within the host frameworks[29]. Based on above, Fe3+ provided more active sites and expedited reaction kinetics.

Fe<sup>3+</sup>-driven tunnel engineering for stabilizing metastable ramsdellite MnO<sub>2</sub> in high-performance zinc-ion batteries

Figure 4. Capacitive behaviors and both electrochemical and morphological analysis after 1000 cycles of β-MnO2 and R-FexMn1-xO2 cathodes: (A) Diffusion-controlled and surface-controlled contributions to capacity at different scan rates; (B) Mn 2p and O 1s spectra; (C) Nyquist plots at the open circuit voltage state (Supplementary Figure 15 illustrates the electrical equivalent circuit used for fitting EIS spectra); (D and E) EIS spectra of β-MnO2 and R-FexMn1-xO2 cathodes during charge process; (F) SEM images of β-MnO2 and R-FexMn1-xO2 cathodes. EIS: Electrochemical impedance spectroscopy; SEM: scanning electron microscopy.

EIS before and after 1000 cycles (at 1 A g-1) further elucidated the role of Fe doping in enhancing interfacial stability, as shown in Figure 4C-E. Due to abundant electrochemically active sites and accelerated ion diffusion kinetics, the charge transfer resistance (Rct) value after cycling was significantly lower for R-FexMn1-xO2 (562.9Ω) than for β-MnO2 (1,720 Ω) [Supplementary Table 2][30]. EIS analysis during cycling stages revealed larger semicircles for both cathodes during charging and post-cycling, correlating with degradation mechanisms. However, R-FexMn1-xO2 maintained more favorable reaction kinetics[31,32]. The SEM images confirmed significantly more dissolution in β-MnO2 than in R-FexMn1-xO2, consistent with the performance degradation mechanisms in Mn-based cathodes. The dissolution of Mn-based materials reduced surface active sites, impaired ion diffusion driving force, and increased Rct, leading to elevated impedance and irregular morphologies [Figure 4F][33-35]. This post-cycle analysis highlights how Fe3+ doping in manganese-based cathodes effectively mitigates the capacity fading inherent to manganese oxide cathodes in AZIBs.

CONCLUSIONS

Fe3+ doping fundamentally transforms the structural stability and electrochemical behavior of metastable ramsdellite MnO2 for zinc-ion batteries. By introducing Fe3+ during the hydrothermal conversion of spent ZnMn2O4, we achieve R-FexMn1-xO2 with engineered (1 × 2) tunnels, reduced surface energy, and optimized Mn4+/Mn3+ ratios. The Fe-mediated mechanism suppresses phase transition to β-MnO2, alleviates lattice strain, and enhances Zn2+/H+ diffusion kinetics, validated by DFT calculations showing lowered surface energy and EIS revealing reduced charge-transfer resistance. Consequently, R-FexMn1-xO2 delivers a high capacity of 286.8 mAh g-1 at 0.1 A g-1, exceptional rate capability (163.3 mAh g-1 at 1.5 A g-1), and long-term stability (88.9% capacity retention after 1000 cycles). Post-cycling analyses confirm Fe3+ mitigates Mn dissolution and structural degradation. This study highlights Fe3+ doping as a universal tunnel-engineering strategy to unlock the potential of metastable MnO2 phases, while offering a sustainable route to repurpose battery waste into high-performance cathodes.

DECLARATIONS

Authors’ contributions

Data curation, methodology, software, writing - original draft, writing - review and editing, funding acquisition: Meng, Y.

Investigation, software, writing - review and editing: Li, Y.

Investigation, software: Xiao, H.; Wang, Z.

Investigation, writing-review and editing: Wang, X.

Software, resources, writing - review and editing: Zhang, F.

Investigation, software, writing - review and editing: Ma, W.

Resources: Xiong, D.; Zhou, T.; Yin, J.

Writing-review and editing: Xiao, Z.

Resources, funding acquisition: Yuan, Z.

Conceptualization, formal analysis, funding acquisition, methodology, resources, supervision, writing-review and editing: Yang, L.

Data analysis, resources: Liu, C.

Supervision, resources: Wu, X.

Availability of data and materials

The linked data has been added to the manuscript. The raw/ processed data required to reproduce these findings can be obtained upon request from the first author.

Financial support and sponsorship

This work is supported by Natural Science Foundation of China (52234001), Science and Technology Planning Project of Hunan Province (2018TP1017), and National Students’ Platform for Innovation and Entrepreneurship Training Program (S202410542060).

Conflicts of interest

Wu, X. is Editorial Board Member of the journal Energy Materials. Wu, X. was not involved in any steps of editorial processing, notably including reviewers’ selection, manuscript handling, and decision making. Yuan, Z. and Zhou, T. are affiliated with Xiangtan Electrochemical Technology Co., Ltd. The other authors declare 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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Fe3+-driven tunnel engineering for stabilizing metastable ramsdellite MnO2 in high-performance zinc-ion batteries

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