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Preparation of Li3V2(PO4)3 as cathode material for aqueous zinc ion batteries by a hydrothermal assisted sol–gel method and its properties

Shiyu Caoa, Yanhong Xiang*a, Qiuling Zoua, Youliang Jiang*b, Hanzhang Zenga, Jian Lia, Jianhua Wua, Xiangsi Wuc, Xianwen Wuc and Lizhi Xiong*d
aSchool of Physics and Electrical Engineering, Jishou University, Jishou 416000, P. R. China. E-mail: yhx@jsu.edu.cn
bLoudi Technician Institute, Loudi 417100, P. R. China
cSchool of Chemistry and Chemical Engineering, Jishou University, Jishou 416000, P. R. China
dSchool of Pharmacy, Jishou University, Jishou 416000, P. R. China

Received 20th March 2023 , Accepted 7th August 2023

First published on 14th August 2023


Abstract

To alleviate the depletion of lithium resources and improve battery capacity and rate capacity, the development of aqueous zinc-ion batteries (AZIBs) is crucial. The open channels monoclinic structure Li3V2(PO4)3 is conducive to the transfer and diffusion of guest ions, making it a promising cathode material for AZIBs. Therefore, in this study, nanoneedles and particles Li3V2(PO4)3 cathode materials for AZIBs were prepared by a hydrothermal assisted sol–gel method, and the effect of synthesized pH values was studied. XRD results show that all samples had the monoclinic structure, and the Li3V2(PO4)3 sample prepared at pH = 7 exhibits (LVP-pH7) the highest peak tips and narrowest peak widths. SEM images demonstrate that all samples have the morphology character of randomly oriented needles and irregular particles, with the LVP-pH7 sample having more needle-like particles that contribute to ion diffusion. EDS results show uniform distribution of P, V, and O elements in the LVP-pH7 sample, and no obvious aggregation phenomenon is observed. Electrochemical tests have shown that the LVP-pH7 sample exhibits excellent cycling performance (97.37% after 50 cycles at 200 mA g−1) and rate ability compared to other samples. The CV test results showed that compared with other samples, the LVP-pH7 sample had the most excellent ionic diffusion coefficient (2.44 × 10−12 cm2 s−1). Additionally, the Rct of LVP-pH7 is the lowest (319.83 Ω) according to the findings of EIS and Nyquist plot fitting, showing a decreased charge transfer resistance and raising the kinetics of the reaction.


1. Introduction

With the continued use of fossil fuels and the slow intensification of the greenhouse effect, energy scarcity and environmental pollution have become two major challenges for the survival and development of human society, and people are increasingly interested in novel energy sources.1,2 Currently, lithium-ion batteries (LIBs) occupy the commercial market of rechargeable batteries and have become the main mobile energy source.3,4 However, in recent years, with the rise in the price of lithium metal sheets and the frequent occurrence of safety problems in LIBs, the future market of LIBs is worrying.5 At the same time, AZIBs are considered as the ideal green energy system for the next generation due to their advantages such as safe water-based systems, low price of zinc sheets (negative electrodes), abundant resources, low redox potential (−0.76 V vs. standard hydrogen electrode, SHE), and high energy density.5–7 Therefore, the development of alternative water energy storage systems is crucial.3 The cathode material is a key factor in determining the final performance of AZIBs.8 The de-insertion process of zinc ions in AZIBs will interact with the cathode materials, so suitable embedding materials are rare. Since its conception, finding the cathode materials that can match the zinc anode is the key and difficult point of research.9 So far, manganese-based oxides,9 vanadium-based materials,10 Prussian blue analogs,11 polyanion compound,12,13 chevrel phase compound,14 and organic compound15 have been reported as cathode materials for AZIBs. The vanadium-based materials are not limited by low specific capacity and deliver excellent electrochemical performance.9 Among them, phosphate (such as polyanionic type and NASICON type phosphate) has the advantages of high structural strength and interconnected three-dimensional channels, which can form flexible active sites conducive to the internal transport of Zn2+.1 More importantly, there is enough space in the structure of the monoclinic Li3V2(PO4)3 compound to conduct Zn2+.16,17 Therefore, Li3V2(PO4)3 can be used to prepare AZIBs.

Currently, in order to solve the problems of poor electronic conductivity, low cycling stability, and structural degradation in aqueous electrolytes of Li3V2(PO4)3.18,19 A large number of researchers employed a lot of synthetic methods to promote the morphology of materials.18 Among them, although high temperature solid phase technology has the benefits of ease of use and cheap expense,20 it is more likely to generate pollutants. Although the coprecipitation technique has the benefits of a quick reaction time, customizable morphology, and low reaction temperature,21 it is challenging to prepare. The materials prepared by the sol–gel method have uniform particle size distribution, high purity, and can achieve molecular level mixing, and are widely used to prepare metal oxide materials. The hydrothermal technique is a way of producing materials in an enclosed pressure tank by dissolving and recrystallizing water as a solvent and powder.22 When compared to other powder preparation techniques, the hydrothermal method has the following advantages: full grain growth, small particle size, homogeneous distribution, light particle aggregation, inexpensive raw materials, and ease of obtaining suitable stoichiometry and crystal shape.23 Therefore, if the hydrothermal method is used to dissolve and recrystallize the aqueous materials first, and then combined with the sol–gel method to prepare the micro nano Li3V2(PO4)3 precursor materials. It makes the grain of Li3V2(PO4)3 develop completely and the structure is relatively stable, which can improve the cyclic stability of the material. Meanwhile, because Li3V2(PO4)3 materials may behave differently under varying pH conditions,24 so it is important to understand the effect of pH parameters in detail on the structure and performance of Li3V2(PO4)3. There has been no comprehensive investigation of the impact of pH on Li3V2(PO4)3.

As a result, the Li3V2(PO4)3 sample was generated using a hydrothermal aided sol–gel process in this research, and the effect of synthesized pH settings on the structural morphology and electrochemical performance of Li3V2(PO4)3 cathode materials was systematically studied during the synthesis process. This auxiliary method is expected to regulate the size and shape of Li3V2(PO4)3 powder, endowing the Li3V2(PO4)3 with a consistent nano size and a continuous electrons channel, so significantly improving the rate capability and cycle stability of Li3V2(PO4)3. This work has the potential to make Li3V2(PO4)3 a strong candidate for the positive electrode material of aqueous zinc ion batteries.

2. Materials and methods

As shown in Fig. 1, a new hydrothermal assisted sol–gel method was used to prepare monoclinic Li3V2(PO4)3 positive electrode materials. Lithium acetate dihydrate (CH3COOLi·2H2O), ammonium metavanadate (NH4VO3), ammonium dihydrogen phosphate (NH4H2PO4) were completely dissolved in deionized water according to the stoichiometric ratio to obtain 0.5 M metal ion mixed solution. Citric acid (C6H8O7) was used as binder to prepare 0.5 M solution. Secondly, add C6H8O7 solution slowly to the above mixed solution, and stirred at a constant temperature of 60 °C for 4 h. During this period, ammonia (NH3·H2O) was used to adjust the pH value of the solution. After stir, the solution is transferred to a 100 ml reactor and reacted at 180 °C for 12 h. The solution was removed and cooled naturally, and finally the cooled solution was stirred into a gel at 80 °C to obtain the precursor. All the chemicals used above are from Aladdin chemical reagents.
image file: d3ra01816d-f1.tif
Fig. 1 The illustration of synthesis processes for Li3V2(PO4)3 cathode materials.

To analyze the effect of pH (5, 6, 7, 8) on the material, the pH of the precursor was adjusted to pH 5, pH 6, pH 7, and pH 8 by NH3·H2O. The prepared gel precursor was then heated in a tubular furnace to 350 °C using a flowing N2 atmosphere and held for 5 h to remove H2O, NH3 and CO2 from the decomposition of the organic components, and then heated at 800 °C for 10 h. The Li3V2(PO4)3 cathode materials were obtained. We labeled the Li3V2(PO4)3 cathode materials obtained by calcination of different pH precursors as LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8, respectively.

2.1 Characterization

X-ray diffraction (XRD, Rigaku 2500, Japan) with Cu-Kα (λ = 0.15406 nm) radiation from 10° to 70° was used to examine the crystal structure of materials. Scanning electron microscopy was used to analyze the morphology and particle (SEM, Zeiss Sigma 300). An EDS (SEM-EDS, Oxford Xplore 30) was used to determine the element distribution of the prepared materials. The surface chemical composition and valence state of samples were investigated by X-ray photoelectron spectroscopy (XPS, Thermofisher Escalab 250Xi, USA).

2.2 Electrochemical test

The preparation process of Li3V2(PO4)3 positive plate mainly includes the following steps: first, Li3V2(PO4)3 powder, acetylene black and polyvinylidene fluoride (PVDF) were mix and grind according to the mass ratio of 7[thin space (1/6-em)]:[thin space (1/6-em)]2[thin space (1/6-em)]:[thin space (1/6-em)]1 to obtain the mixed slurry. Then the slurry is applied to a 14 mm stainless steel wire disc. Finally, the discs are dried at 80 °C for 12 h to obtain 14 mm Li3V2(PO4)3 cathode sheets. Zn foil was used as the anode and Li3V2(PO4)3 as the cathode for the CR-2016 coin-type cells, which were then separated by a glass fiber separator with an aqueous electrolyte (2 M ZnSO4 + 1 M Li2SO4). At room temperature, the CT2001A LAND (Wuhan, China) battery test system was used to test the rate performance, cycle performance and charge–discharge performance of the material. The voltage range of the test is 0.7–1.7 V, and the method of discharging before charging is adopted. Cyclic voltammetry (CV) and electrochemical impedance spectroscopy (EIS) were tested using an electrochemical workstation (CH1660E, Shanghai). The scan rate of CV was 0.5, 0.3, 0.2, 0.1 mV s−1, and the voltage window range was 0.7–1.7 V. The frequency range of EIS was 0.01 Hz–100 kHz.

3. Results and discussion

The crystal structures of Li3V2(PO4)3 are monoclinic and rhombic, but the thermodynamic instability of the rhombic crystal structure makes it difficult to create. The monoclinic Li3V2(PO4)3 is thermodynamically stable, its synthesis is relatively simple, and it also has a large capacity.25 At present, monoclinic Li3V2(PO4)3 cathode materials have emerged as a research focus. Fig. 2a displays the X-ray diffraction (XRD) patterns of the acquired Li3V2(PO4)3 samples at various pH levels. The NASICON Li3V2(PO4)3 structure is an open framework made up of VO6 octahedral and PO4 tetrahedral sharing oxygen vertex, as shown in Fig. 2b. XRD results demonstrated that the main characteristic peaks of the all samples at around 20.9°, 24.5° and 29.5° are indexed to (020), (121), (220) facets of Li3V2(PO4)3 (JCPDS no. 72-7074), which reflects a high degree of preferred orientation along c axis.26 All of the diffraction peaks belong to the P21/n space group of monoclinic Li3V2(PO4)3.27 The peak shape of the materials is sharp, and there is no obvious secondary phase or impurity phase in the XRD spectrum, thus indicating that all the samples synthesized are of high purity. It shows that we have successfully prepared Li3V2(PO4)3 materials. In addition, it was found that the crystallinity of Li3V2(PO4)3 gradually increases with the increase of pH value. Among them, the LVP-pH7 sample is demonstrated by the narrowed full width half maximum of peaks and by the increased peak intensity. The Li3V2(PO4)3 samples showed higher peak tips and narrower peak widths at pH = 7. This shows that the Li3V2(PO4)3 material synthesized under neutral conditions has higher purity and better crystal structure. When the pH value reaches up to 8, thanks to the increase in NH4+ ion in mixed solution, the reaction rate of citric acid complexing with metal ions decrease, so it may lead to poor crystallinity. In addition, based on the XRD data of the samples, the average crystallite sizes of all samples were calculated using the Debye Scherrer formula (as shown in eqn (1)).28 The average crystallite sizes of all samples were DLVP-pH5 = 99.48 nm, DLVP-pH6 = 14.75 nm, DLVP-pH7 = 24.43 nm, and DLVP-pH8 = 26.37 nm, respectively. It can be seen that materials prepared under nearly neutral conditions have smaller grain sizes.
 
image file: d3ra01816d-t1.tif(1)
Parameter meaning: D: crystallite sizes, nm; K: Scherrer constant, K = 0.89; λ: the X-ray wavelength, for Cu·Kα, λ = 0.15406; β: half peak width of diffraction angle; θ: diffraction angle.

image file: d3ra01816d-f2.tif
Fig. 2 (a) The X-ray diffraction (XRD) pattern of LVP-pH5, LVP-pH6, LVP-pH7, and LVP-pH8. (b) Schematic illustration of Li3V2(PO4)3 crystal structure.

To further study the elemental compositions of LVP-pH7 sample, XPS test was adopted. Fig. 3 shows the XPS image of the LVP-pH7 sample. The signals of carbon, vanadium, phosphorus, lithium and oxygen elements can be clearly detected in the XPS curve (Fig. 3a). The C-spectrum of LVP-pH7 material is shown in Fig. 3b. The C1s spectrum at binding energy value of 284.8 eV is corresponded to sp2 C–C bonds, This indicates that citrate decomposes into carbon during the calcination process, and there is residual carbon present in Li3V2(PO4)3.29 The V2p spectrum presented in Fig. 3c possesses two obvious peaks located at around 517.5 and 524.7 eV, representing the V2p3/2 and V2p1/2 respectively,16 The observed binding energy values correspond to V3+ in LVP-pH7 sample, suggesting the successful reduction of V5+ to V3+.25


image file: d3ra01816d-f3.tif
Fig. 3 (a) XPS survey curves of the fabricated LVP-pH7 sample; XPS spectra of LVP-pH7 samples: (b) C1s, and (c) V2p.

To study the morphology of all samples, the morphology of the Li3V2(PO4)3 materials are investigated by using a scanning electron microscope (SEM). Fig. 4 (a–d) shows the SEM images of LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8 samples, respectively. All samples displayed randomly oriented needles and irregular particles. The morphology of this composite is not only conducive to the contact between electrolyte and particles, but also accelerate electron transport through randomly oriented needles along nanorods simultaneously.30 Further observations revealed, with the increase of pH value, the material particles gradually become smaller, and the number of needles changed obviously as the pH value increased. Especially, there are quite a multiple randomly oriented needles with a diameter of 50 to 100 nm in the LVP-pH7 sample Fig. 4c, but when the pH increased to 8, the number of such needles decreased instead. These special needles are conducive to electrolyte penetration and rapid ion diffusion, which can overcome the problem of poor ion diffusion of phosphate compounds, reduce charge transfer resistance, reduce the transmission distance of lithium ions, and increase the diffusion rate of lithium ions, which is conducive to improving electrochemical performance. Fig. 4e and f shows the EDS element mapping of the LVP-pH7 sample. O, P, and V elements were uniformly distributed in the cathode material.


image file: d3ra01816d-f4.tif
Fig. 4 The scanning electron microscopy (SEM) images of (a) LVP-pH5, (b) LVP-pH6, (c) LVP-pH7, and (d) LVP-pH8. (e and f) EDS element mapping of LVP-pH7.

In order to further explore the influence of pH value of synthesis conditions on the electrochemical properties of Li3V2(PO4)3 in AZIBs, the constant current charging–discharge test is carried out under a current density of 2C (200 mA g−1) in a potential voltage range of 0.7–1.7 V (vs. Zn2+/Zn). As shown in Fig. 5a–d, the charge and discharge plateaus of sample occur at 1.38 V, 1.33 V and 1.47 V, 1.41 V correspond to a series of phase transitions of Li3V2(PO4)3 ↔ Li2V2(PO4)3 ↔ LiV2(PO4)3, resulting in a V3+/V4+/V5+ ordering state.31 The initial discharge capacities of the LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8 samples are 52.81 mA h g−1, 53.43 mA h g−1, 68.35 mA h g−1 and 45.42 mA h g−1, respectively. Different from LIBs, during the initial charge, few Li+ are de-intercalated into the electrolytes, while Zn2+ are plated in the anode. During the discharge, Li+ in electrolytes can provide an additional part of capacity. Due to the use of 2 M ZnSO4 + 1 M Li2SO4 as the electrolyte, the Li+ of electrolyte can provide additional partial capacity during the discharge process. The results of the second charge–discharge also verify this viewpoint. In Fig. 5a and b, the discharge specific capacity of the LVP-pH7 sample was significantly improved compared with the other samples. Which may be due to the presence of more randomly oriented needles in the LVP-pH7 sample, thereby increasing the contact area between the positive electrode material and the electrolyte. This can accelerate the ion removal/insertion, increase the active reaction sites, and thus increase the discharge specific capacity.


image file: d3ra01816d-f5.tif
Fig. 5 (a) The initial charge/discharge curves of LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8. (b) The second charge/discharge curves. (c) The CV curves of LVP-pH7 at different scan rates of 0.1–0.5 mV s−1. (d) The operating principle of aqueous zinc ion battery.

Fig. 6 shows the cycling performance and rate characteristics of LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8 samples in AZIBs. The rate capacity test was increased by varying from 2C to 20C, and then returned to 2C. All samples showed good capacity retention and good stability. This could be due to the use of a hydrothermal aided sol–gel preparation technique, which results in a material with improved electrochemical performance. The discharge specific capacities of LVP-pH7 sample at different rates of 2C–20C are 65.91, 56.35, 50.57, 46.64, and 40.77 mA h g−1, respectively. It is obvious that the LVP-pH7 sample shows the highest discharge specific capacity at all rates. Meanwhile, the samples capacity gradually increases when the pH increases from 5 to 7, but when the pH increased to 8, the capacity decreased instead, even lower than the LVP-pH5 sample. This may be due to the fact that neutral conditions are more conducive to the complexation reaction between citric acid and metal ions, thereby improving the crystallinity of the material, as well as produces more needles that contribute to ion transport. On the other hand, when the pH increases to 8, excessive NH4+ can lead to a decrease in the reaction rate of citric acid complexing with metal ions, leading to a decrease in crystallinity. Moreover, when the rate returned to 2C, the specific capacity of LVP-pH7 could still recover to 52.39 mA h g−1, which was 80.77% of the initial capacity, much higher than the 42.61 mA h g−1 of LVP-pH5, the 41.87 mA h g−1 of LVP-pH6 and the 33.65 mA h g−1 of LVP-pH8. It can be seen from the figure that under the high current density of 2C, after 50 cycles, the specific capacity attenuation of LVP-pH7 is very small, and the capacity retention rate is high (remains at 97.37%). A large number of randomly oriented acicular and irregular particles in LVP-pH7 sample, which can improve the diffusion coefficient of guest ions in the material, and the unique structure can effectively alleviate the volume expansion of the material in the process of charging and discharging. And quickly provide a certain amount of space for the guest (ion/electron), thus enhancing the rate characteristics and cycle performance of the material. In addition, compared with other AZIBs Li3V2(PO4)3 cathode materials, the discharge performance of Li3V2(PO4)3 materials prepared by hydrothermal assisted sol–gel method has been improved.32–35


image file: d3ra01816d-f6.tif
Fig. 6 The rate capabilities and cycle performances of LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8.

Electrochemical impedance spectroscopy (EIS) was used to assess the kinetic characteristics of all Li3V2(PO4)3 samples. Fig. 7 shows the EIS plots for all samples. Use Zview fitting software to establish equivalent circuit. The Nyquist diagram of the electrode material consists of a semicircle in the high-frequency region and a slash line in the low-frequency region. The semi-circle in the high frequency region corresponds to the electrochemical reaction resistance and the double-layer capacitance of the electrode material, while the slash line in the low frequency region corresponds to the diffusion of ions, namely, Warburg diffusion. Charge-transfer resistance (Rct) may be calculated from the semicircle in the high-frequency region, which corresponds to the resistance between the electrolyte and the Li3V2(PO4)3 electrode.35,36 According to the fitting findings, the Rct value of the LVP-pH7 sample (319.83 Ω) was substantially lower than that of the LVP-pH5 sample (515.95 Ω), the LVP-pH6 sample (413.96 Ω), and the LVP-pH8 sample (598.37 Ω). This result demonstrates that guest ion transfer is much easier inside the LVP-pH7 sample between the electrode and electrolyte, which may profit from the special morphology and structure of Li3V2(PO4)3 sample, which is beneficial to enhance the electrical conductivity and zinc ion diffusion coefficient of the material. This is consistent with the results of rate and cycle properties.


image file: d3ra01816d-f7.tif
Fig. 7 The Nyquist plots of LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8.

To analyze the redox process and ion diffusion rate in electrode reactions, the cyclic voltammetric tests were carried out on all samples between 0.7 V and 1.7 V (the scanning rates were 0.1, 0.2, 0.3 and 0.5 mV·s−1, scanning direction is positive scanning). The CV curves of LVP-pH5, LVP-pH6, and LVP-pH8 at different scanning rates are shown in Fig. 8, while the CV curves of LVP-pH7 are shown in Fig. 5c. We can clearly see that the CV curves of all samples show similar profiles with two reduction peaks and two oxidation peaks. The first oxidation peak of around 1.39 V during charge can be assigned to the extraction of first lithium ion with the oxidation of vanadium from V3+ to V3+/V4+. The second oxidation peak of around 1.48 V derived from the extraction of second lithium ion with the entire vanadium oxidation from V3+/V4+ to V4+ in reaction.37 In the subsequent discharge process, the first reduction peak of around 1.40 V can be detected, which is due to the initial re-insertion of lithium ion into LiV2(PO4)3, but the re-insertion of zinc ion into the surface of the cathode electrode.38 The second reduction peak near 1.33 V is attributed to the second lithium ion insertion.39 This corresponds to the first charge/discharge curve in Fig. 5a. The CV curves of all samples show that as the scanning speed increases, the voltage difference between redox peaks gradually increases,40 the height and size of redox peaks also increase, and the peak current also increases.40 This means that irreversible behavior becomes more and more apparent at larger scanning rates. This is because lithium ions cannot be fully extracted/inserted/entered from the electrode during the time interval of high rate scanning, resulting in irreversible behavior.37 In addition, the redox peaks of LVP-pH5, LVP-pH6, and LVP-pH8 samples had similar variation characteristics. Compared with LVP-pH7, the oxidation peaks of the other three samples significantly shifted towards higher potentials, while the corresponding reduction peaks shifted towards lower potentials. This would result in the LVP-pH7 sample having the smallest potential difference between oxidation peak and reduction peaks, which is related to the polarization and electrochemical reversibility of cathode materials.41 This suggests that the LVP-pH7 sample have lower polarization and better electrochemical reversibility.42,43 This result is consistent with the previous electrochemical performance analysis. The results indicate that Li3V2(PO4)3 has an interactive transformation mechanism, and lithium ions migrate reversibly into the cathode along with zinc ions platting/stripping at the anode during charge and discharge, to realize the reversible de-insertion/insertion of zinc ions. Zinc diffusion in the electrode is the rate-limiting step if the charge transfer at the interface is quick enough, and Randle–Sevcik36 (2) may be used to compute the ion diffusion coefficient:

 
ip = 2.69 × 105 × n3/2A × D1/2C0 × V1/2 (2)
where ip is the peak current, n is the number of electrons per reactive species, A is the surface area of the electrode (here the geometric area of electrode 1.5385 cm2), D1/2 is the diffusion coefficient (cm2 s−1) of Zn2+, C0 is the concentration of zinc ions (2 M) and V1/2 is the scanning rate. According to the linear fitting results of cyclic voltammetry in Fig. 9, the corresponding slope was calculated, and then the zinc ion diffusion coefficients are 1.92 × 10−13, 1.37 × 10−12, 2.44 × 10−12 and 1.17 × 10−12 (cm2 s−1) for the LVP-pH5, LVP-pH6, LVP-pH7 and LVP-pH8 samples respectively. By comparing the CV results of all samples, it is found that LVP-pH7 sample have a good ion diffusion rate, which is consistent with the morphological characteristics and EIS results.


image file: d3ra01816d-f8.tif
Fig. 8 The CV curves of (a) LVP-pH5, (b) LVP-pH6, (c) LVP-pH8 at different scan rates of 0.1–0.5 mV s−1.

image file: d3ra01816d-f9.tif
Fig. 9 The relationship between the current peaks and scan rate is based on the CV curves. (a) LVP-pH5, (b) LVP-pH6, (c) LVP-pH7 and (d) LVP-pH8.

To get insight into the structural evolution process, in order to further discussed the effect of pH value on the crystal structure, morphology and electrochemical performance of the material. The cycling electrode were evaluated by ex situ XRD measurements. Fig. 10 shows the ex situ XRD patterns of LVP-pH7 sample under different charge states. Under different charge states, the characteristic peak strength of the LVP-pH7 sample after charging and discharging is slightly lower than that of the original LVP-pH7 material. However, the original monoclinic structure of the LVP-pH7 material basically maintains remains. Compared with the standard card, the peak values detected at 43° and 51° belong to the iron mesh current collector.40 Throughout the charging and discharging process, Li+ is embedded and detached from Li3V2(PO4)3, which leads to subtle structural changes of the material. As shown in Fig. 10b. For ex situ X-ray diffraction, no obvious Zn inserted diffraction peak can be detected in the charge or discharged electrodes. This ex situ XRD signal evolution of Li3V2(PO4)3 is similar to the observation in the LIBs.37 As shown in Fig. 10a. By comparing the XRD with the standard card, it was found that point a at 1.7 V in Fig. 10a coincides with LiV2(PO4)3, point b and c correspond to Li2V2(PO4)3 material, and point d corresponds to Li3V2(PO4)3 material. Point a–d corresponds to the discharge process of the battery, and is accompanied by the insertion of Li+. Similarly, point e and f correspond to Li2V2(PO4)3 material, and point g has the same structure as point a, which is LiV2(PO4)3. However, starting from d–g corresponds to the battery charging process, accompanied by the release of Li+. As expected, from a–g after the charging and discharging process, the diffraction peaks are able to fully recover in the initial (point a) state. This indicates that the migration process of Li+ is reversible. Furthermore, Li3V2(PO4)3 cathode material prepared by hydrothermal assisted sol–gel has good reversibility and structural stability.


image file: d3ra01816d-f10.tif
Fig. 10 The ex situ XRD patterns of LVP-pH7 at different charge state.

4. Conclusions

In conclusion, we effectively developed and manufactured Li3V2(PO4)3 materials using an unique hydrothermal aided sol–gel process to enhance both electronic conductivity and zinc ion diffusivity. In addition, the effect of pH value on the morphology and electrochemical properties of Li3V2(PO4)3 materials was systematically studied. The XRD and SEM results show that all the samples we prepared have high crystallinity and show randomly oriented needle and irregular particles. The morphology of this composite is not only conducive to the contact between electrolyte and particles, but also accelerate electron transport through randomly oriented needles along nanorods simultaneously. Electrochemical test results indicated that adjusting pH value during the synthesis has an important effect on rate capability and cyclability. The LVP-pH7 sample with the increasing number of needle-like has importantly enhanced electrochemical performance, compared to the LVP-pH5, LVP-pH6 and LVP-pH8 samples. The capacity retention of the LVP-pH7 remains at 97.37% after the 50th cycle at 2C. Besides, the EIS data show the LVP-pH7 sample had a relatively smaller charge transfer resistance value and thus alleviates the diffusion pathways of ions and electrons. The CV fitting result indicated that the LVP-pH7 had a relatively greater ions diffusion rate, which is will correspond with the rate capability and EIS test results. The improved performance can be mainly attributed to these needles and particles in the LVP-pH7 sample because the existence of needles may reduce aggregation between aside structures, increase the special surface area for holding electrolyte. In general, when the pH value increases from 5 to 7, the various properties of Li3V2(PO4)3 materials also become better, but when the pH value increases to 8, the various properties decrease rapidly. This study provides a method and idea for preparing new AZIBs cathode materials.

Author contributions

Shiyu Cao: methodology, investigation, writing – original draft; Yanhong Xiang: conceptualization, investigation, writing – review & editing; Qiuling Zou: investigation, writing – original draft; Youliang Jiang: resources, investigation; Hanzhang Zeng: data curation; Jian Li: visualization, writing – review & editing; Jianhua Wu: data curation; Xianwen Wu: resources, visualization; Lizhi Xiong: validation.

Conflicts of interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Acknowledgements

This research was financially supported by the National Natural Science Foundation of China (No. 52264037, No. 52064014, No. 52265019 and No. 52064013), the Young Scientific and Technological Talents (Hejian) Project of Hunan Province (No. 2022RC1087), and the Outstanding Youth Funding program of Hunan Province (No. 2023JJ10033, 2022JJ40341), the National innovation training program for undergraduate (No. 202110531002), which were greatly appreciated.

Notes and references

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