Open Access Article
Tatsuya Kondo
*ab,
Sota Kawaguchi
a,
Naoto Takeshimab,
Shuto Igaria,
Satoyuki Tatsumib,
Kaori Akiyamab,
Kenji Machidab and
Sekihiro Takedab
aBasic Research Center, Nippon Chemi-Con Corporation, KSP R&D C1025, 3-2-1 Sakado, Takatsu-ku, Kawasaki-shi, Kanagawa 213-0012, Japan. E-mail: chem.edu.tkondo@gmail.com; Fax: +81-44-379-6885; Tel: +81-44-379-6881
bBasic Research Center, Nippon Chemi-Con Corporation, Takahagi, Ibaraki 318-8505, Japan
First published on 18th March 2026
To advance a sustainable society, increasing attention has been directed toward the development of high-performance materials and environmentally responsible synthetic methodologies. Cation-disordered materials have attracted attention across various fields because of their exceptional performance. However, their synthesis requires high-temperature calcination or after-treatment of cation-ordered precursors, resulting in high energy consumption levels, extended processing times, and increased costs, which hinder commercialization. Recently, low-temperature solution-based reactions enabling the synthesis of cation-disordered structures via instantaneous crystallization using spray dryers have been reported; however, technical insights into these processes remain unclear due to very few reports compared with those for solid-state reactions. In this study, we demonstrate low-temperature one-pot synthesis (<40 °C) of cation-disordered Li3VO4, a high-performance anode material, from a solution reaction via a combination of a rotary evaporator and a vacuum dryer, which are standard laboratory apparatuses, under strictly controlled conditions. This cation-disordered Li3VO4 is identified as a kinetically stabilized metastable phase and undergoes a moisture-induced phase transition to the thermodynamically stable β-phase, which results in inferior performance. Moreover, it can be dissolved in water and reverted to its precursor ions, indicating its recyclability. This methodology, in which a kinetically stabilized crystal phase is synthesized via evaporation-driven crystallization, supports the development of innovative materials that simultaneously achieve green chemistry and high performance.
Crystal structure plays a pivotal role in determining device performance, thus rendering its control crucial.1,2 In recent years, high-entropy crystal structures with cation disorder have attracted attention in various applications, including batteries,3–5 solid electrolytes,6–8 and semiconductors (such as thermoelectric9,10 and optoelectronic11,12), because of their potential to increase device performance. Particularly in lithium-ion batteries, the use of cation-disordered lithium transition metal oxides could improve electrochemical properties, such as increasing the capacity and voltage.13–15 For instance, compared with conventional commercialized cathode materials such as NCM (Lithium nickel cobalt manganese oxides) and LFP (LiFePO4), lithium-excess cation-disordered rock salt cathode materials offer higher energy density. Lithium-excess cation-disordered rock salt-type cathode materials have been reported to contain a wide range of variations, thereby incorporating not only Ni, Co, Mn, and Fe but also various other transition metals, such as Ti,16–18 V,19–21 Cr,22 Zr,18 Nb,20,21,23 Mo,16,17,22 and Ta.24 Among these elements, V can be used not only as a cathode25–27 material but also as an anode material because of its wide range of reaction potentials, which is based on its multiple oxidation states. Cation-disordered anode materials such as rock salt-type Li3V2O5
28 and wurtzite-type Li3VO4
29–31 are promising new anodes because of their high capacity, high-rate capabilities, and suitable potential to prevent the formation of lithium dendrites. Li3VO4 (LVO) is a promising insertion-type anode material,32 with a high theoretical capacity (394 mAh g−1, Li3V5+O4 + 2Li+ + 2e− → Li5V3+O4) and a safe operating voltage range (0.4–1.3 V vs. Li+/Li). Although cation-ordered β-phase LVO, featuring an ordered arrangement of LiO4 and VO4 tetrahedra at room temperature, has been extensively reported as a lithium-ion battery anode,33–45 its superior potential as an anode material is limited by its low electronic conductivity (10−10 S cm−1).42,43 Naoi's group reported that cation-disordered LVO, with a lithium diffusion coefficient30,31 that is more than 100 times greater than that of β-phase LVO, demonstrates a remarkable rate performance29,31 and a capacity retention of greater than 50% at 20 A g−1. Despite these advantages, synthesis techniques for cation-disordered LVO remain challenging.
Lithium-excess cation-disordered rock salt cathode materials are generally synthesized via solid-state reactions, which involve mixing raw materials followed by high-temperature calcination. Other techniques, such as mechanochemical treatments with high-energy planetary ball milling21 or electrochemical treatments inducing disordered structures by repeated lithium-ion insertion/extraction,22 have been proposed. However, in the case of LVO, the direct synthesis of cation-disordered structures through calcination is restricted because of the formation of the thermodynamically stable γ-phase at high temperatures.46–49 Cation-disordered LVO has been synthesized through posttreatments for cation-ordered β-phase LVO, such as electrochemical (cycling between 2.5–0.1 V for 20 cycles)30 or mechanochemical (ball milling for 36 hours).31 However, these treatments require high energy consumption levels, extended processing times, and increased costs, making them impractical for large-scale commercialization (SI Table 1). Therefore, developing a novel synthesis technique capable of controlling the crystal phase of LVO while being energy efficient, eco-friendly, and cost effective for commercialization is essential.
The low-temperature synthesis methods for LVO with low energy consumption are summarized in Table 1. Conventional solid-state synthesis requires high temperatures above 600 °C for the reaction between lithium carbonate and vanadium oxide.32 In comparison, solution-based methods such as solvothermal37 or hydrothermal38 and precipitation39 methods have been reported to synthesize LVO at low temperatures without calcination. In particular, combining Li+ with VO43−, a structural component of the LVO crystal structure generated via high-pH dissolution of NH4VO3,38,39 is a rational approach. Among previous reports, the humidity-assisted solid-state method at 80 °C represents the lowest-temperature synthesis method, in which LVO is formed through reactions of the raw material mixture inside water droplets.45 This method involves low energy consumption, is eco-friendly and does not involve the use of byproducts. Although these efforts have resulted in low-temperature, eco-friendly reactions, the resulting LVO shows primarily the β-phase, whose rate performance is inferior to that of the cation-disordered structure. For LVO design strategies, the crystal phase is a key factor contributing to high-rate performance, and the use of VO43− is critical for eco-friendly reactions. Recently, Naoi's group demonstrated the direct synthesis of cation-disordered LVO at 90 °C from an aqueous solution of LiOH and V2O5 through instantaneous crystallization via a spray-drying technique without passing via β-phase LVO.50 A balance between excellent electrochemical performance and eco-friendly reactions has been achieved, and a spray dryer is also suitable for industrial applications, as it is highly scalable and has an extensive history of successful implementation in industry. However, very few reports on the synthesis of cation-disordered materials through solution-based reactions, including the present reaction, exist, and technical insights regarding the synthesis remain insufficient compared with those for solid-state reactions. For example, many cation-disordered oxide materials synthesized via solid-state routes do not require any quenching-type processes to stabilize disordering, suggesting that ultrafast drying alone cannot universally explain the emergence of metastable disordered phases.
| Methodology | Source | Temperaturea/°C | Energy costb/J g−1 | Reference | ||
|---|---|---|---|---|---|---|
| Li | V | Solvent | ||||
| a Temperature: the temperature refers to the reaction temperature used for the synthesis.b Energy cost: the energy cost refers to the energy necessary to raise the reaction environment to the reaction temperature from room temperature (25 °C); this evaluation does not take into account factors such as the power consumption of the apparatus employed for the synthesis. The calculation formula is given below: (energy cost) = (specific heat capacity of the reaction environment) × (temperature difference between the reaction temperature and room temperature). Herein, the specific heat capacities (J g−1 K−1) used in the calculation are as follows: air: 1.0; H2O + acetone: 3.1; H2O: 4.2; and ethylene glycol: 2.4. | ||||||
| Solid-state | Li2CO3 | V2O5 | — | 900 | 875 | 32 |
| Solvothermal | Li2CO3 | V2O5 | H2O + acetone | 300 | 853 | 37 |
| Hydrothermal | LiOH (excess) | NH4VO3 | H2O | 180 | 651 | 38 |
| Precipitation | LiOH (excess) | NH4VO3 | Ethylene glycol | 120 | 228 | 39 |
| Humidity-assisted solid-state | LiOH | V2O5 | H2O (droplet) | 80 | 231 | 45 |
| Spray-drying | LiOH | V2O5 | H2O | 90 | 65 | 50 |
| This work | LiOH | V2O5 | H2O | 40 | 63 | |
In this study, we demonstrate green one-pot synthesis of cation-disordered LVO below 40 °C with high-rate performance through a low-temperature solution reaction with strictly controlled drying processes using a rotary evaporator—which offers significantly slower drying than spray-drying—and a vacuum dryer, which are standard laboratory apparatuses. We experimentally and theoretically reveal that this cation-disordered structure is a kinetically stabilized metastable phase, and this phase readily transitions to the thermodynamically stable β-phase under catalytic action by moisture. This finding clarifies the key factors in the drying process required to obtain the metastable phase, highlighting the critical role of moisture control. In recent years, recycling technologies for lithium-ion batteries have been actively studied,51,52 and by exploiting the water solubility of LVO, facile resource recovery is anticipated, making it a promising recyclable and high-performance next-generation anode material.
:
1 ratio (Fig. 2c and S4). In contrast, β-LVO also has a hexagonal close-packed oxygen framework, where Li and V are regularly accommodated in the Td site formed by four oxygen atoms, indicating a difference in each cation accommodation site. In the X-ray photoelectron spectroscopy (XPS), both the C-LVO and β-LVO showed the V 2p3/2 peak arising from the vanadium in the pentavalent state (SI Fig. 5). While both the C-LVO and β-LVO particles were µm in size according to the scanning electron microscopy (SEM) observations, the magnified images revealed distinct surface morphologies (Fig. 2d). The C-LVO crystallized with a rotary evaporator exhibited a surface comprising aggregated spherical nanoparticles approximately 50 nm in diameter, whereas the β-LVO prepared via high-temperature calcination exhibited a smooth and uniform surface. Detailed surface structure analysis was performed by N2 adsorption tests (Fig. 2e). In accordance with the International Union of Pure and Applied Chemistry (IUPAC) classification of N2 adsorption isotherms,57 C-LVO and β-LVO were categorized as types IV (H3 hysteresis loop) and III, respectively. Adsorption/desorption hysteresis observed in C-LVO above a relative pressure of 0.5 suggests the presence of mesopores. The type III isotherm for β-LVO suggests a nonporous structure, which is consistent with the SEM image. Pore size distributions calculated by the Barrett–Joyner–Halenda (BJH) method revealed that C-LVO has pores smaller than 10 nm (Fig. 2f). According to the Brunauer–Emmett–Teller (BET) method within the relative pressure range of 0.05–0.30, the specific surface areas of C-LVO and β-LVO were 12.63 and 0.89 m2 g−1, respectively, with C-LVO exhibiting a specific surface area more than 10 times greater than that of β-LVO (SI Fig. 6). The increased surface area due to the formation of nanoparticles and mesopores could increase electrolyte accessibility and facilitate fast Li+ insertion/extraction.
On the basis of these results, a comprehensive mechanism was proposed (Fig. 3e). When V2O5 is added to a high-pH LiOH aqueous solution, orthovanadate (VO43− oxyanion) forms. At this stage, the aqueous precursor solution contains the essential components of LVO (Li+ and VO43−). In the drying process involving the evaporator, water is expelled from the system through evaporation, resulting in Li+ and VO43− occurring in a minimally solvated state. Further enforced dehydration leads to the precipitation of crystals. This leads to the formation of a metastable cation-disordered structure since vanadium can exist in various coordination states. After the cation-disordered structure forms, promptly removing adsorbed water maintains the structure, resulting in a phase transition to the thermodynamically stable β-phase. Since the rotary evaporator alone does not sufficiently remove moisture at this stage, a rapid dehydration process using vacuum drying becomes a key factor in the synthesis technique. The C-LVO obtained by controlling the drying method is expected to exhibit favourable electrochemical properties because of its crystal structure and surface morphology.
In the initial discharge (Li+ insertion) process, a high irreversible capacity was observed, which is attributed to side reactions such as electrolyte decomposition and SEI film formation; however, stable curves were obtained during subsequent cycles. During the second cycle, both electrodes exhibited discharge capacities close to 200 mAh g−1, which matched the theoretical capacity (197 mAh g−1) associated with the single-electron reaction of LVO in the range of 0.76–2.5 V. The discharge/charge curve of β-LVO plateaued at 0.85 and 1.00 V, resembling typical battery-like curves. In comparison, C-LVO displayed capacitor-like sloped discharge/charge curves, revealing characteristic behaviour in cation-disordered LVO.29–31,50 dQ/dV analysis revealed broadened peaks for C-LVO, providing clear evidence of the slope behaviour (SI Fig. 10). The slope observed in the discharge/charge curve is believed to result from cation disordering in the structure.14,15 Furthermore, moisture-treated LVO displayed battery-like curves as well as β-LVO, indicating that the crystal structure affects the shape of the discharge/charge curves (SI Fig. 11). The following tests were conducted via stabilized cells (precycled cells) after the initial cycle. In our previous reports, we demonstrated that the discharge rate capability of LVO is lower than its charge rate capability.49 Therefore, to examine the rate performance in detail, the counter current density was fixed at 0.1 C-rate, and the discharge (Li+ insertion) and charge (Li+ extraction) processes were assessed separately by varying the current density (Fig. 4c and S12). In the discharge process, β-LVO maintained a high capacity retention at 1 C-rate; however, its capacity retention decreased significantly at higher current densities. The reason for this finding is that β-LVO exhibits a plateau at 0.85 V at 0.1 C-rate, and the discharge curve changes significantly with increasing current density and becomes more strongly affected by the cut-off voltage (0.76 V). Consequently, β-LVO did not demonstrate sufficient capacity within the voltage range of 0.76–2.5 V during the discharge process. The sloped curve for C-LVO was less affected by the cut-off voltage, and minimal changes in the discharge curve were observed, resulting in greater capacity retention. C-LVO exhibited a greater capacity retention than β-LVO did, with the capacity retentions of C-LVO and β-LVO being 60% and 16% at 10 C-rate (2 A g−1), respectively. Moisture-treated LVO exhibited a capacity approximately 10 mAh g−1 higher than that of β-LVO; however, similar to β-LVO, its capacity retention decreased significantly when the current density exceeded 1 C-rate (SI Fig. 13). In the charging process, these LVO materials showed greater capacity retention in the charging process than in the discharge process, with C-LVO and β-LVO retaining 66% and 51% of their capacities, respectively, at 50 C-rate (10 A g−1). Moisture-treated LVO also exhibited a high capacity retention, showing a charge rate capability comparable to that of C-LVO, with a retention of 64% at 50 C-rate. To reveal the improvement of rate capability, the apparent Li+ diffusion coefficient (DLi+) was estimated using the galvanostatic intermittent titration technique (GITT) (Fig. 4d and S14). In the discharge process, the DLi+ of β-LVO and moisture-treated LVO began to decline when x exceeded 0.3 in Li3+xVO4, while those of C-LVO remained relatively high throughout. This behaviour is consistent with the cation-disordered LVO induced by electrochemical activation.30 The DLi+ of C-LVO were enhanced up to 50-fold compared with those of β-LVO, indicating that cation disordering intrinsically contributes to the improvement of DLi+. In both processes, compared with β-LVO, C-LVO significantly improved the rate performance. This improvement is attributed not only to changes in curve shape but also to enhanced diffusion coefficients from the crystal structure, reduced Li+ diffusion length within particles due to size reduction, and increased electrolyte accessibility resulting from increased specific surface area. Cyclability of the precycled cells was assessed at a current density of 1 C-rate (0.2 A g−1) (Fig. 4e and S15). Each electrode has the same capacity, which is the value obtained at 1 C-rate in the charging rate test. This is attributed to the dependence of capacity on the charging process, which is the rate-limiting step at a constant current. Unlike β-LVO, C-LVO exhibited a capacity exceeding 30 mAh g−1. Both electrodes demonstrated stable cycling because of their high coulombic efficiency, and the capacities of C-LVO and β-LVO were 92.7% and 90.3%, respectively, after 1000 cycles. A comparison of the shapes of the discharge/charge curves from the 1st and 1000th cycles revealed minimal changes, demonstrating the high electrochemical stability of C-LVO.
| 6LiOH–H2O + V2O5 → 2Li3VO4 + 9H2O | (1) |
This reaction is an eco-friendly reaction that achieves many of the 12 principles of green chemistry.64 It involves the use of water as a solvent and consists of a simple synthesis process of dissolution and drying at 40 °C, resulting in high atom efficiency without the use of auxiliaries. Water as a byproduct is recovered during drying, so we can obtain only C-LVO. Interestingly, LVO is soluble in water, and dissolving it returns it to Li+ and VO43−. This suggests that easy resource recovery is feasible, making it a promising recyclable next-generation anode material (Fig. 5).
In synthesis methods such as hydrothermal reactions, crystals grow slowly in the long term while selecting thermodynamically stable orientations and thus yielding thermodynamically stable phases. In contrast, crystallization via evaporation using drying equipment forcibly separates solutes from the solution in a short time, which is believed to lead to kinetically stabilized metastable phases. Indeed, there have been reports showing that evaporation-driven crystallization induces metastable phases.65 Given that vanadium is a transition metal with various coordination structures, it is suggested that the evaporation process promotes the formation of cation-disordered LVO as a kinetically stabilized structure. Although cation-disordered LVO is readily transformed into thermodynamically stable phases because of water adsorbed on its surface, the spray-drying technique,50 which enables instantaneous crystallization and immediate separation from moisture, is suitable for synthesizing a kinetically stabilized structure. Moreover, spray dryers are scalable equipment widely used in industry, making large-scale commercialization highly promising. However, synthesis could also be achieved by combining drying with a rotary evaporator and subsequent vacuum drying for rapid moisture removal.
The synthesis method involving the preparation of components in aqueous solution followed by recovery through drying is rational and holds promise for application to a wide range of materials, not limited to LVO, since many transition metal species can form oxoanions in aqueous solutions at high pH.56 In addition, this methodology provides a broader community of researchers with the opportunity to discover high-performance next-generation materials with an eco-friendly method since kinetically stable metastable structures can be synthesised using a standard laboratory apparatus.
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