Zhendong Guoa,
Yingjin Weia,
Dong Zhang*a,
Xiaofei Biea,
Yongquan Zhanga,
Kai Zhua,
Rongyu Zhanga and
Gang Chenab
aKey Laboratory of Physics and Technology for Advanced Batteries (Ministry of Education), College of Physics, Jilin University, Changchun 130012, P. R. China. E-mail: dongzhang@jlu.edu.cn; Fax: +86-431-85155126; Tel: +86-431-85155126
bState Key Laboratory of Superhard Materials, Jilin University, Changchun 130012, P. R. China
First published on 18th November 2014
Tavorite LiFeSO4F cathode material is prepared by the solvothermal method. The thermal stability of delithiated LixFeSO4F is characterized by X-ray diffraction, differential scanning calorimetry and thermogravimetric analysis. It shows that the side reactions between the cathode material and the electrolyte are moderate, which involves the decomposition of LixFeSO4F forming Fe2(SO4)3 and Li2SO4 phases and F2 gas. The onset temperature of the exothermal process is 358 °C with a minimal heat release of 79.4 J g−1. The material undergoes further decomposition above 500 °C, which forms Fe2O3, Fe3O4 and Li2O, associated with the release of SO2 gas.
Recently, a new polyanion material, tavorite LiFeSO4F, has been reported as a potential cathode material for Li-ion batteries.8,9 The material has a theoretical capacity of 151 mA h g−1 and a working voltage of 3.6 V versus Li+/Li. It could be a strong contender to LiFePO4 because of a greater cell voltage (150 mV), even though the theoretical energy density is 5% lower than that of LiFePO4. This slight drawback can be counter balanced by the better ionic conductivity of LiFeSO4F, which obviates the need for resorting to nanoparticles thus increases the material packing density.8 Given these advantages, it is important to characterize the thermal stability of the LiFeSO4F cathode. In this communication, we report our new findings on the thermal stability of delithiated LixFeSO4F cathode. The results show that the material has extremely high thermal stability which implies its potential uses in high safe lithium ion batteries.
Electrochemical experiments were carried out using 2032-type coin cells. A metallic lithium foil served as the anode electrode. The cathode electrode was composed of LiFeSO4F active material (70 wt%), carbon black conductive additive (20 wt%), and poly (vinylidene fluoride) binder (PVDF, 10 wt%). Each electrode was 8 × 8 mm2 in size and contained about 2 mg of active material. The cathode and anode electrodes were separated by Celgard 2320 membrane. The electrolyte was a 1 mol L−1 lithium hexafluonophosphate (LiPF6) dissolved in ethylene carbonate (EC), dimethyl carbonate (DMC), and ethyl methyl carbonate (EMC) with EC:
DMC
:
EMC = 1
:
1
:
8 by v/v ratio. Galvonostatic charge–discharge cycling was performed on a Land automatic battery tester at 25 °C and 60 °C, respectively.
After the first charge process completed, the battery cell was disassembled in glove box. The cathode composite was scrapped from the electrode and washed in DMC for several times. The delithiated LixFeSO4F powders were then used for in situ heat treatment X-ray diffraction (XRD) study on a Rigaku D/max-2550 diffractometer with Cu Kα radiation. The differential scanning calorimetry (DSC) of the material was studied on TA-Q2000 between room temperature and 450 °C with a heating rate of 10 °C min−1. Thermogravimetric analysis (TGA) was performed on a SDTA851E thermo analyzer between room temperature and 800 °C with a heating rate of 10 °C min−1.
Galvanostatic charge–discharge cycling is performed at room temperature in the voltage window of 2.5–4.5 V at the C/10 rate (I = 15.1 mA g−1). As shown in Fig. 2, the first charge profile of the material shows a voltage plateau at around 3.6 V. About 0.65 mol of Li ions are removed from the material, associated with an initial charge capacity of 98 mA h g−1. However, only 0.52 mol of Li ions can be inserted in the subsequent discharge, corresponding to a small columbic efficiency of 80%. The irreversible capacity could be due to the difficulty in insertion more Li ions into the crystal structure. Also, a part of the irreversible capacity is caused by the formation of solid electrolyte interface (SEI) film which has been reported by J. M. Tarascon et al.11 The irreversible capacity is immediately minimized after the first cycle, resulting in a stable columbic efficiency of 96%. The material is also charge–discharged at 60 °C as shown in Fig. 2. At this elevated temperature, the initial charge and discharge capacities are increased to 120 mA h g−1 and 110 mA h g−1, respectively. A discharge capacity of 80 mA h g−1 is obtained after 50 cycles, which is much larger than the 60 mA h g−1 that measured at room temperature. Here it should be noted that the electrochemical performance of the as-prepared LiFeSO4F is not as good as expected which could be due to several reasons such as (1) the electronic conductivity of the material is low because it is not carbon coated; (2) the particle size of the material is too large for a polyanion cathode material (ESI Fig. S1†); (3) the upper cutoff voltage is high enough to cause electrolyte decomposition. (4) The SEI film formed during the initial charge–discharge cycle (Fig. S2†). (5) The LiF impurity is not only electrochemical inactive but also electronic insulative. Future work should be done to resolve the above problems for preparing high performance LiFeSO4F cathode.
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Fig. 2 (a) Charge–discharge curves and (b) cycling performance of LiFeSO4F at room temperature and 60 °C. |
Fig. 3 shows the DSC curve of the electrochemically delithiated LixFeSO4F (x = 0.35) cathode, together with those of the LiPF6/EC + DMC + EMC electrolyte and the chemically delithiated LixFeSO4F powders (x = 0.35, which was prepared by soaking the LiFeSO4F powders in a NO2BF4 and acetonitrile oxidation agent). The DSC curve of the electrochemically delithiated LixFeSO4F shows an endothermic process in the temperature range of 248–280 °C and an exothermic process in the temperature range of 358–443 °C. The corresponding heat evolved in the above processes are – 25.4 J g−1 and 79.4 J g−1, respectively. Combining with the DSC curves of the electrolyte and chemically delithiated LixFeSO4F, the endothermic process is attributed to the decomposition of remaining electrolyte whose existence can be observed by fourier transform infrared spectroscopy (Fig. S3†), and the exothermic process is due to the LixFeSO4F phase. Additional experiments show that the fully chemically de-lithiated FeSO4F also have similar TG and DSC curves as those of Li0.35FeSO4F (Fig. S4 and S5†). This indicates that LiFeSO4F has excellent thermal stability not only in partially de-lithiated state but also in fully de-lithiated state. In addition, Fig. 3 shows that the electrochemically and chemically delithiated Li0.35FeSO4F have similar exothermic temperatures and thermal release. This indicates that the side reactions between the LixFeSO4F cathode and the electrolyte are moderate, which do not lower the exothermic temperature or bring additional thermal release in the battery system. In comparison, our recent study on another fluorine-based polyanion cathode material, LiVPO4F, exhibits more violent side reactions with the electrolyte. The exothermal peak of LixVPO4F itself is as high as 342 °C, but it decreases to 235 °C when coupled with a LiPF6/EC + EMC electrolyte.5 Additional DSC experiments show that LixFeSO4F have similar thermal behavior in different LiPF6 based electrolytes (Fig. S6†). This demonstrates the good thermal stability of LixFeSO4F in conventional electrolyte mixtures.
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Fig. 3 DSC curves of the chemically and electrochemically delithiated Li0.35FeSO4F, together with that of the LiPF6/EC + DMC + EMC electrolyte. |
Temperature dependent XRD are performed to study the phase transformations of Li0.35FeSO4F during heat treatment. A Pt holder is used as an internal standard for calibration of the XRD peaks. Both the chemically and electrochemically delithiated samples show similar XRD patterns (Fig. S7†) indicating that the phase transformation is only correlated with the structure properties of Li0.35FeSO4F itself. It is seen from Fig. 4a that the structure of Li0.35FeSO4F is well reserved before 360 °C. Thereafter, the Li0.35FeSO4F phase continuously decomposes between 360 °C and 500 °C, accompanied with the formation of Fe2(SO4)3 and Li2SO4 phases. Meanwhile, the TG curve of Li0.35FeSO4F (Fig. 4b) shows a weight loss about 2.6 wt% in the same temperature range. This suggests that the exothermic process is associated with the decomposition of Li0.35FeSO4F which forms Fe2(SO4)3 and Li2SO4 phases and F2 gas. With the heat temperature increasing to 700 °C, the XRD pattern mainly shows the co-existence of Fe2O3 and Fe3O4. In addition, the TG curve shows an abrupt weight loss about 42.4 wt% between 500 °C and 700 °C. Therefore, it is reasonable to say that the material undergoes further decomposition at high temperature, which forms metal oxides including Fe2O3, Fe3O4 and Li2O accompanied with the release of SO2 gas. Note that Li2O is not observed in the XRD patterns due to its small amount or amorphous state. According to the above phase transformations, the calculated weight losses for the F2 and SO2 evolutions are 7.3 wt% and 36.9 wt% respectively. The differences between the calculation and experimental values may be due to the thermal hysteresis effects of the TG experiment. In spite of this, the total experimental weight loss (45.0 wt%) is consistent well with that of the calculation result (44.2 wt%).
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Fig. 4 (a) Temperature dependent XRD patterns and (b) TG curve of the electrochemically delithiated Li0.35FeSO4F. |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c4ra08921a |
This journal is © The Royal Society of Chemistry 2014 |