Open Access Article
Lounis H. Bekkar
a,
Alex Lemarchand
a,
Noël Girodon-Boulandeta,
Cyrille Bazin
b,
Mathieu Frégnaux
c,
Hubert Perrot
b and
Mehrdad Nikravech
*a
aUniversité Sorbonne Paris Nord, UPR CNRS 3407, Laboratoire des Sciences des Procédés et des Matériaux LSPM, 93430 Villetaneuse, France. E-mail: mehrdad.nikravech@lspm.cnrs.fr
bSorbonne Université, UMR CNRS 8235, Laboratoire Interfaces et Systèmes Electrochimiques LISE, 4, place Jussieu, F-75005 Paris, France
cInstitut Lavoisier de Versailles, Université de Versailles Saint-Quentin-en-Yvelines, Université Paris-Saclay, CNRS, UMR 8180, Versailles Cedex 78035, France
First published on 23rd January 2026
The need to develop safe, environmentally-friendly and low cost batteries has led to a growing interest in zinc-ion batteries (ZIBs), due to the abundance of zinc and the high theoretical capacity of this material. For large scale applications, it will be necessary to find adequate cathode materials capable of reversible Zn2+ electrochemical storage over prolonged cycling. Among various promising candidates, ZnMn2O4 spinel has attracted attention because of its high theoretical capacity, higher voltage than vanadium-based cathodes, and better cyclability among manganese oxide-based cathodes. However, most of the elaboration routes of manganese oxide based cathodes rely on cost-ineffective and time-consuming multi-steps processes. In this work, we report the elaboration of nanostructured thin films of ZnMn2O4 spinel using a single step non-equilibrium plasma method without calcination and without using any additives. The electrochemical behavior of the as-deposited ZnMn2O4 spinel thin film was studied for application as a cathode in ZIBs. It gave a remarkably high specific capacity of 235 mA h g−1 at 0.1 A g−1 and 155 mA h g−1 after 1100 cycles at a current intensity of 1 A g−1. These electrochemical performance results demonstrate that the plasma-based elaboration process is a promising strategy for the development of advanced next-generation ZIBs based on the use of nanostructured materials with a controlled structure and microstructure.
Currently, lithium-ion batteries (LIBs), with organic electrolytes, are the most attractive and widely used energy storage technology.5,6 Nevertheless, the lack of security, high-cost production, lithium resource limitations and environmental issues are prompting a search for sustainable alternatives to LIBs.6–8
In this context, other kinds of rechargeable metal-ion (Na+,9 K+,10 Mg2+,11 Zn2+,12 Ca2+,13 Al3+)14 batteries with aqueous electrolytes have received extensive attention, as safety, high performance, environmental friendliness, recyclability and low cost are among the required criteria for batteries of the future. Zinc cations present an ionic radius very close to that of lithium. The higher redox voltage of zinc (−0.763 V vs. a standard hydrogen electrode (SHE)) allows metallic zinc to be used in slightly acidic aqueous media,15 and the two-electron transfer mechanism offers zinc a high theoretical specific capacity of 820 mA h g−1 or 5854 mA h cm−3. Therefore, zinc-ion batteries (ZIBs) could provide high energy density and excellent rate performance.16,17 Moreover, zinc metal is naturally abundant, evenly spread within the earth's crust, low cost and non-toxic. These attributes make zinc a very promising candidate for producing high-performance aqueous metal-ion batteries.
However, the main challenge that ZIBs are facing is finding adequate cathodic materials capable of reversible Zn2+ storage after prolonged cycling.18 This challenge is even bigger given that the cathode material is arguably one of the most important components in ZIBs, as it influences the overall electrochemical performance of the battery.
So far, three types of cathode materials have been mainly studied for ZIBs: manganese-based oxides,19 vanadium-based oxides20 and Prussian Blue analogues.21 Manganese-based oxides are among the most promising and the most studied ones due to their high capacities and high voltage simultaneously.22 However, they suffer from capacity decay due to irreversible structural transformations, Mn dissolution, and by-product generation during the charging/discharging process.23
It has been reported that the binary manganese oxides have superior rechargeability compared to mono-oxides.24 Spinel ZnMn2O4 is one of the binary manganese oxides with a high redox potential, large natural abundance of raw materials and low toxicity to the environment. Inspired by the LiMn2O4 cathode in LIBs,25 it has been investigated in many studies as a cathode material for ZIBs.26–30 Importantly, no phase transition has been observed for this material, leading to stable cycling performance.24,31
A wide range of ZnMn2O4 synthesis routes have been reported to date, including sol–gel,32,33 solvothermal,34,35 hydrothermal,36,37 co-precipitation,38,39 micro-emulsion40,41 and solid state methods,42 as well as microwave-assisted colloidal synthesis,43 electrospinning44 and electrodeposition.24 However, most of the conventional elaboration methods of manganese-based oxides rely on annealing (>400 °C) to achieve sufficient crystallinity and require the incorporation of conductive carbon and polymer binders to ensure electrical conductivity and mechanical stability.26,31,45–47 These successive steps significantly increase the process complexity, duration, resource consumption and overall manufacturing cost, which limits their suitability for scalable and sustainable electrode production.
In contrast, the present work introduces a one-step route for the elaboration of ZnMn2O4 spinel cathode materials in the form of nanostructured thin films using a low pressure non-equilibrium plasma process. This approach eliminates the need for high-temperature annealing and avoids any additives, simplifying electrode fabrication while reducing energy input and material use. The resulting ZnMn2O4 films are directly functional in their as-deposited state, exhibiting a high specific capacity of 235 mA h g−1 at 0.1 A g−1 and a cyclability of 70% over 2000 cycles at a high current density of 4 A g−1. These performance results highlight the strong potential of the plasma process as an efficient, low-cost and environmentally friendly alternative to conventional synthesis routes. We believe that this work will pave the way for the development of more efficient strategies to obtain high performance battery materials and accelerate the development of next-generation energy technologies, especially in giving fast and cheap ways to meet the exploding battery demand.
:
Mn molar ratio of 1
:
2 ([Mn2+] = 0.1 M; [Zn2+] = 0.05 M). The precursor solution was nebulized using a home-made ultrasonic sprayer (1 MHz), and then carried into the plasma reactor by a mixture of argon and oxygen gas at a flow rate of 470 mL min−1. There, the droplets are subjected to rapid evaporation as the vapour pressure of the solvent (methanol saturated vapour pressure = 130.2 mbar at 20 °C) is much higher than the 1 to 10 mbar inside the reactor. The plasma chamber is a quartz tube positioned in the centre of an inductive coil and maintained at 60 Pa by a vacuum pump to ensure the consistency and stability of the plasma throughout the deposition process. A radiofrequency power generator coupled with a matchbox provides the plasma discharge at 450 W. The argon and oxygen gas flow rate and plasma discharge power values are, respectively, key parameters to control the residence time of the chemical precursors in the plasma and its reactivity through the amount of reactive species. The influence of these parameters was studied in a previous work48 and they were fixed here to guarantee the acquisition of a well-crystallized thin film. The substrates used were amorphous quartz, silicon and platinum. The substrate temperature was controlled with a temperature regulation system and maintained between 25 °C and 200 °C. Fig. 1c shows that the samples mass is proportional to the deposition time. The deposition rate was estimated at 20 μg min−1 for a 1 cm2 surface. Considering that 0.6 mg was enough to perform the different characterizations, the deposition time was fixed at 30 min in all experiments.
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| Fig. 1 a) Photograph of the plasma reactor; b) experimental setup; c) low pressure plasma thin film mass as a function of the growth time. | ||
![]() | (1) |
![]() | (2) |
![]() | (3) |
| Phase | ZnMn2O4 | ||||
|---|---|---|---|---|---|
| Space group | I41/amd | ||||
| System | Tetragonal | ||||
| Lattice | |||||
| a | 5.74 Å | ||||
| c | 9.18 Å | ||||
| Atomic positions | |||||
| Atom | Wyckoff site | x | y | z | Occupancy |
| Zn | 4(a) | 0 | 0.25 | 0.375 | 0.125 |
| Mn | 8(d) | 0 | 0 | 0 | 0.25 |
| O | 16(h) | 0 | 0.513 | 0.236 | 0.5 |
| Crystalline size domains | |||||
| Orientation | (200) | (101) | (004) | ||
| Size | 20.5 nm | 14.9 nm | 3.4 nm | ||
| Goodness of the fit | |||||
| χ2 | 2.23 | ||||
| Rp | 3.61 | ||||
| Rwp | 4.58 | ||||
| Rexp | 3.07 | ||||
All peaks are well assigned to the I41/amd space group (space group no. 141) and the structural parameters (unit cell, atom positions and occupancy) are consistent with the literature. The refinement data correspond to a negligible amount of microstrain. The particle size is thus considered to be the main contribution to the peak enlargement. The crystal domain sizes in the three directions show that the Plasma-ZMO 200 nanoparticles are anisotropic with a large shape factor, suggesting the potential formation of plate-shaped nanoparticles. The good quality of the refinement using the anisotropic grain size model suggests that the film is not textured. In order to confirm the particle size obtained with Rietveld refinement, the High Resolution Transmission Electronic Microscopy (HRTEM) images of Plasma-ZMO 200 are displayed in Fig. 2c and d. A clear lattice structure is observed. Crystalline domains of 14–19 nm can be observed with anisotropic shape. This justifies the anisotropic broadening model considerations. Inter-reticular distances of 0.483 nm, 0.305 nm and 0.244 nm are also calculated and matched, respectively, to the (101), (112) and (122) planes of the spinel ZnMn2O4.
The Raman spectra of samples elaborated with and without plasma are displayed in Fig. 2e. According to group theory, the factorial group analysis gives 10 Raman active modes. Indeed, ZnMn2O4 belongs to AMn2O4 spinels (A = Mn, Mg, and Zn), which have the following phonon modes T = 2A1g + 3B1g + B2g + 4Eg.53 All Raman spectra of the ZMO thin layers show vibrational bands. Surprisingly, the ZMO 250 spectra exhibit one Raman vibrational mode at 665 cm−1. It seems that heating at 250 °C leads to the formation of metal–oxygen bonds. The Plasma-ZMO 50, -ZMO 145, -ZMO 175 and -ZMO 200 spectra show three Raman vibrational modes at 311, 356 and 666 cm−1, which can well match the ZnMn2O4 spinel phase. The low frequency modes (311 and 356 cm−1) are the responses of the octahedral BO6 sites; the high-frequency mode at 666 cm−1 can be ascribed to vibrations involving the motion of oxygens inside the tetrahedral unit AO4, which can represent A1g symmetry.54,55 So, the formation of Mn–O and Zn–O bonds does not seem to be dependent on the substrate temperature. However, at low temperature (50 °C), two large bands are observed at 1358 cm−1 and 1590 cm−1, which can be attributed to the G band and D band of amorphous carbon. This means that at low substrate temperature, there is residual carbon from the organometallic precursors. But at high temperatures, all of the precursor carbon is converted into CO and CO2.
The surface of the ZMO 200 sample was characterized by X-ray Photoelectron Spectroscopy (XPS) in order to investigate the valence state of the Mn atoms and, consequently, to confirm the formation of the ZnMn2O4 spinel phase in thin films fabricated by the spray plasma process. The wide-scan XPS spectrum is shown in Fig. 3a. Peaks corresponding to Zn, Mn, O, and C elements are clearly observed. Fig. 3b displays the high-resolution XPS spectrum of the Mn 2p core level, where two distinct peaks centered at 641.0 eV and 653.1 eV correspond to Mn 2p3/2 and Mn 2p1/2, respectively. These two peaks are separated by a binding energy of ΔE = 12.1 eV, confirming the presence of Mn3+ species in spinel ZnMn2O4.56–58 Fig. 3c presents the high-resolution XPS spectrum of the Zn 2p core level. The two peaks located at 1021.3 eV and 1044.4 eV correspond to Zn 2p3/2 and Zn 2p1/2 of Zn2+, respectively. The energy separation between them, ΔE = 23.1 eV, is consistent with values reported in the literature.58,59 The O 1s core-level spectrum, shown in Fig. 3d, exhibits a main contribution with a shoulder feature. After reconstruction, the component at 529.6 eV is attributed to oxygen atoms in the metal–oxide bonds (Mn–O and Zn–O).60,61 The component at 531.6 eV may be assigned to –OH and C–O groups,59 and/or to adsorbed oxidized species on the surface, such as water vapor.61,62 Finally, Fig. 3e presents the XPS spectrum of the C 1s core level. Reconstruction of the spectrum reveals three components: the peak at 285.1 eV corresponds to C–C bonds (sp3-hybridized carbon), the one at 286.3 eV is associated with C–O bonds, and the peak at 288.6 eV is attributed to O–C
O groups.62 Given that the X-ray diagram and Raman spectrum of the ZMO 200 sample show no features related to carbon, these C 1s contributions are most likely due to surface contamination.
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| Fig. 3 a) Full XPS spectrum of ZMO 200. b) XPS spectra of Mn 2p. c) XPS spectra of Zn 2p. d) XPS spectra of O 1s. e) XPS spectra of C 1s. | ||
In our experimental conditions the plasma is considered as a non-equilibrium medium where electrons acquire mean energy, to be in the range of 3–5 eV (measured by the Langmuir probe technique and Optical Emission Spectroscopy method).63,64 The kinetic energy of electrons is sufficient to the break down bonds in chemicals (3.58 eV for the C–C bond). Moreover, in previous work, we demonstrated that in the range of plasma power applied, oxidant species, e.g. O and OH radicals, are formed and are able to oxidize the fragments of chemical precursor injected in the plasma participating in the formation of metal oxide thin films.65,66 In our experimental conditions, the temperature of the reactor walls remains generally around 60–70 °C. In previous work, we estimated the temperature inside the plasma vicinity to be equal to (392 ± 50) K, independent of the RF power in the range explored in similar conditions as presented in this work, measuring the rotational temperature of the OH radical (A2∑+ − X2π)(0,0) transition and from the Boltzmann plot method of the OH emission lines.48 It is noteworthy that the rotational temperature represents the thermal temperature of plasma gas rather than the electronic temperature. The fact that in conventional elaboration methods the oxidation of manganese acetate necessitates temperatures over 500 °C confirms that, in our conditions where the temperature doesn't exceed 70 °C, the chemical transformation of the starting materials into ZnMn2O4 is governed by electronic collisional processes via radical species.
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| Fig. 4 a and b) SEM images of the Plasma-ZMO 200 surface. c) SEM image of a Plasma-ZMO 200 straight section. d) EDX elemental mapping images. e) AFM micrograph of Plasma-ZMO 200. | ||
Fig. 5a and b show the cyclic voltammetry (CV) profiles of the Plasma-ZMO 200 cathode in the potential window of 0.8–1.8 V, recorded at scan rates of 1 mV s−1 (Fig. 5a) and 0.1 mV s−1 (Fig. 5b). At the higher scan rate, the CV curves display a single oxidation peak at 1.55 V during the anodic sweep and two reduction peaks at 1.19 V and 1.37 V during the cathodic sweep. At the lower scan rate, two distinct oxidation peaks at 1.53 V and 1.61 V emerge, while the two reduction peaks remain visible at 1.19 V and 1.37 V during the cathodic sweep. According to the literature, the interpretation of these current peaks remains controversial, as no consensus has been reached regarding the reaction mechanisms governing this class of batteries.67 Although a large number of studies address MnO2 cathodes, very few propose detailed reaction mechanisms for ZnMn2O4 cathodes. Nevertheless, two plausible mechanisms may be considered in the context of this work. The first involves Zn2+ intercalation and deintercalation. The oxidation peaks observed in the CV profiles of the Plasma-ZMO 200 cathode are attributed to the oxidation of Mn4+ atoms within the ZnMn2O4 spinel structure, induced by Zn2+ deintercalation. This process is ascribed to the strong electrostatic repulsion of neighbouring Mn cations occupying octahedral sites. The reduction peaks are instead associated with the reduction of Mn atoms in the spinel framework caused by Zn2+ intercalation. The presence of two oxidation and two reduction peaks is interpreted as stepwise Zn2+ deintercalation and intercalation, respectively.28,59,68–70 The second mechanism considers the co-insertion and co-extraction of H+ and Zn2+ ions. In fact, other reports suggest that the occurrence of two anodic and two cathodic peaks indicates that the system is governed by two distinct electrochemical processes, namely the reversible insertion of protons (H+) and Zn2+ ions, which accompanies the Mn redox transitions in the ZnMn2O4 structure.45,71,72 In this scenario, several authors have reported the precipitation of zinc hydroxysulfate (Zn4(OH)6SO4·xH2O, commonly referred to as ZHS) on the cathode surface. Proton insertion into manganese oxides depletes H3O+ ions at the solid–liquid interface, leading to a local pH increase and subsequent ZHS deposition.45
Meanwhile, the increase of redox peak current during the first CV scans indicates the possible existence of an activation process or a better accessibility to the whole material.
To track the evolution of the specific capacity as a function of cycling, the galvanostatic charge/discharge profiles at 100 mA g−1 between 0.8–1.8 V are superimposed in Fig. 5c. In the charge profiles, two distinct oxidation plateaus can be observed at 1.50 V and 1.57 V, while two reduction pseudo-plateaus appear at approximately 1.24 V and 1.38 V in the discharge profiles. The positions of these plateaus and pseudo-plateaus are relatively close to the oxidation and reduction peak potentials observed in the CV profiles and are in good agreement with values reported in the literature.24,26,28,59,68,72,73 The discharge plateaus are separated by an inflection point—often referred to as a voltage tip—located at 1.26 V, which is commonly observed for manganese-based cathodes in ZnSO4 electrolytes. This voltage tip has been interpreted either as the nucleation point of ZHS45 or as the onset of a decrease in the Zn2+ diffusion coefficient according to another report.74 Based on this interpretation, the galvanostatic discharge profile of the Plasma-ZMO 200 cathode can thus be divided into two distinct regions: region I, prior to the 1.26 V tip, and region II, after the 1.26 V tip. The overall capacity increases progressively with cycling, as shown in the table of Fig. 5c. The first cycle delivers only 56 mA h g−1 during charge and 66 mA h g−1 during discharge. In the second cycle, the discharge capacity rises to 70 mA h g−1, corresponding to a 6% capacity gain, and continues to increase until it reaches 82 mA h g−1 by the fifth cycle, representing a 24% gain relative to the first cycle. This capacity enhancement corroborates the observations made from the CV profiles of the Plasma-ZMO 200 cathode. A closer examination of regions I and II reveals that the capacity contribution of region I is consistently greater than that of region II, regardless of the cycle number, and that the contribution of region I increases more rapidly than that of region II (see table in Fig. 5c). These observations clearly indicate that the two regions are associated with distinct electrochemical kinetics. According to the literature, region I is attributed to the capacity arising from the H+ insertion step, whereas region II corresponds to the capacity associated with Zn2+ intercalation.24
After the galvanostatic charge/discharge measurements, at the end of the 5th discharge, the Plasma-ZMO 200 cathode sample was characterized by scanning electron microscopy (SEM) and X-ray diffraction (XRD), and the results are shown in Fig. 5d. The XRD pattern reveals the presence of diffraction peaks characteristic of the Zn4(OH)6SO4·4H2O phase, while the SEM images of the Plasma-ZMO 200 cathode sample surface at the end of the discharge show lamellar structures that are completely different from the morphology observed before the charge/discharge cycling. According to the literature,72 such structures are characteristic of ZHS deposits forming on manganese oxide cathode surfaces after the 1.26 V voltage tip during discharge. Consequently, it can be concluded that ZHS deposits form on the surface of the Plasma-ZMO 200 cathode sample during discharge and that this process contributes to the recorded electrochemical signal. Given that the reaction mechanism in this type of system remains complex, the results presented above do not allow for a clear identification of all the chemical processes responsible for the observed electrochemical signal. Nevertheless, by combining these results with conclusions drawn from the literature, a mechanism involving the co-insertion of H+ and Zn2+, accompanied by the electrodeposition/dissolution of ZHS, appears plausible to explain the electrochemical behaviour of the Plasma-ZMO 200 cathode.
In order to investigate the behaviour of the Plasma-ZMO 200 cathode under a high number of cycles and at a high current density, the sample was cycled at 1 A g−1 for 1100 cycles. Fig. 6a shows the evolution of the charge and discharge capacities as well as the coulombic efficiency during this cycling, while Fig. 6b presents the charge/discharge profiles of the 1st, 100th, 200th, 500th, 800th, 900th, 1000th and 1100th cycle. Both the charge and discharge specific capacities increase over the 1100 cycles at 1 A g−1, thus confirming the observations made from the CV profiles in Fig. 5a and b and the galvanostatic charge/discharge measurements at 100 mA g−1. The initial discharge capacity is only 20 mA h g−1. It remains stable for about fifty cycles but, surprisingly, begins to increase, reaching 155 mA h g−1 after 1100 cycles. The first cycle shows a coulombic efficiency of 62%. This shows an initial irreversible process, which could be due to SEI formation, irreversible ion trapping and/or side reactions. From the second cycle onward, the CE increases rapidly, and after 20 cycles it reaches between 98% and 99%. The subsequent cycles typically show much higher efficiencies than the initial ones indicating that the system has reached a more reversible electrochemical regime.
Analysis of the profiles in Fig. 6b indicates that the capacity increase is associated with the elongation of the 1.50 V plateau (charge) and the pseudo-plateau around 1.38 V (discharge). CV plots of Plasma-ZMO 200 after 1100 cycles (Fig. 6c) also confirms the GCD results as the redox peak current increases significantly. This capacity growth over prolonged cycling could be due to reversible ZHS deposition/dissolution according to the rising capacity from the H+ insertion step as observed in Fig. 5c. In fact, in the GCD curves shown in Fig. 6b, we can observe the disappearance of the 1.26 V tip. This means that at high current density, the insertion of H+ responsible of ZHS formation is the main electrochemical phenomenon responsible for the specific capacity. Furthermore, according to S. Li et al., the ZHS layer formed on the cathode surface may act as a passivation layer, enhancing the cycling stability of the cathode.47 Zhao et al. even reported a discharge specific capacity of approximately 123 mA h g−1 using a cathode composed solely of ZHS.75
The rate performance of the Plasma-ZMO 200 cathode after the 1100th cycle, shown in Fig. 6d and e, was investigated at different current densities from 1 A g−1 to 0.1 A g−1. The discharge capacity increases when the current density decreases. At current densities of 0.8, 0.6, 0.4, 0.2, and 0.1 A g−1, the reversible discharge capacities are 166, 176, 190, 223 and 235 mA h g−1, respectively. The energy density and power density of the Plasma-ZMO 200 cathode at a discharging current density of 0.1 A g−1 are 331 W h kg−1 and 86 W kg−1 using eqn (2) and (3). A second cycling stage was performed on the Plasma-ZMO 200 sample by further increasing the current density to 4 A g−1 over 2000 cycles (3100 GCD cycles in total). Fig. 6f shows the evolution of the specific capacity and coulombic efficiency of Plasma-ZMO 200 during this second stability test. After a first capacity increase stage to 126 mA h g−1 at 100 cycles, the specific capacity drops to a constant value of 68 mA h g−1. At this very high current density, the phenomena leading to an increase in the specific capacity do not occur. It can therefore be suggested that the kinetics of these reactions are relatively slow. The capacity drop could also be explained by the structural degradation of the cathode, or simply by the loss of mass due to the delamination of part of the active material from the current collector, given that the cycling period here was approximately two months.
Finally, a brief comparison of the electrochemical performance of the ZMO 200 thin film elaborated by plasma with that of ZMO-type cathodes prepared with conventional synthesis methods is presented in Table 2. The performance of ZMO 200 is fully comparable to that of its counterparts, while maintaining the distinctive advantage of being free from carbon and binder additives. It is acknowledged that this comparison does not take into account the influence of cathode thickness and its consequent effect on electron diffusion between the surface and the current collector. Nevertheless, the table provides a useful overview of the recent progress achieved in ZMO-based cathodes for zinc-ion batteries and outlines prospective performance targets for future developments.
| Cathode | Elaboration method | Electrolyte | Maximum specific capacity | Cyclability | Ref. |
|---|---|---|---|---|---|
| Oxygen-deficient Mn3O4 | Solvothermal | 2 M ZnSO4 + 0.2 M MnSO4 | 386 mA h g−1 at 0.1 A g−1 | 272% after 500 cycles at 0.5 A g−1 | 76 |
| α-MnO2 nano-wire/CNT | Hydrothermal | 2 M ZnSO4 | 330 mA h g−1 at 0.05 A g−1 | 8% over 2500 cycle at 3 A g−1 | 77 |
| VO2·xH2O nanoribbons | Hydrothermal | 3 M Zn(CF3SO3)2 | 235.63 mA h g−1 at 0.1 A g−1 | 82% after 1000 cycles at 1 A g−1 | 78 |
| ZnMn2O4/Mn2O3 | Surfactant-assisted solvothermal method | 1 M ZnSO4 | 152 mA h g−1 at 0.1 A g−1 | 143% after 300 cycles at 0.5 A g−1 | 70 |
| Mn2O3@ZnMn2O4/C hollow micro-spheres | Hydrothermal | 2 M ZnSO4 + 0.1 M MnSO4 | 289.9 mA h g−1 at 200 mA g−1 | 203.5 mA h g−1 after cycling for 700 times at 1000 mA g−1 | 79 |
| MoS2@N-CQDs | Solvothermal | 3 M Zn(OTf)2 | 258 mA h g−1 at 0.1 A g−1 | 94.5% after 2000 cycles | 80 |
| ZnMn2O4 | Spray plasma | 1 M ZnSO4 + 0.05 M MnSO4 | 235 mA h g−1 at 0.1 A g−1 | 70% after 2000 cycles at 4 A g−1 | This work |
Supplementary information (SI): the SI file provides an additional comparative table of the electrochemical performances of selected ZMO cathodes fabricated by conventional methods, compared with the cathode material performance obtained in this work (ZMO 200 thin film produced via plasma spray). It also includes additional data related to electrochemical experiments, including sample preparation and cell measurement conditions. See DOI: https://doi.org/10.1039/d5lf00303b.
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