Lixin
Qiao
ab,
Zili
Cui
*b,
Bingbing
Chen
b,
Gaojie
Xu
b,
Zhonghua
Zhang
b,
Jun
Ma
b,
Huiping
Du
b,
Xiaochen
Liu
b,
Suqi
Huang
c,
Kun
Tang
ab,
Shanmu
Dong
b,
Xinhong
Zhou
*a and
Guanglei
Cui
*b
aCollege of Chemistry and Molecular Engineering, Qingdao University of Science & Technology, Qingdao, 266042, P. R. China. E-mail: zxhhx2008@163.com
bQingdao Industrial Energy Storage Research Institute, Qingdao Institute of Bioenergy and Bioprocess Technology, Chinese Academy of Sciences, Qingdao, 266101, P. R. China. E-mail: cuigl@qibebt.ac.cn; Tel: +86-532-80662746
cSchool of Chemistry and Chemical Engineering, Qingdao University, Qingdao, 266071, P. R. China
First published on 1st March 2018
A new salt of lithium trifluoro(perfluoro-tert-butyloxyl)borate (LiTFPFB) which possesses a bulky fluoroalkoxyl functional group in the borate anion has been synthesized for high energy lithium metal batteries. The presence of the bulky fluoroalkoxyl group in the borate anion of LiTFPFB can facilitate ion dissociation and in situ generate a protective film on the Li anode. As a result, LiTFPFB possesses a dramatically improved ionic conductivity and LiFePO4/Li cells using 1.0 M LiTFPFB/PC electrolyte exhibit improved capacity retention especially upon cycling at elevated temperature (60 °C). Ex situ surface analysis reveals that a protective film is formed on the lithium metal anode, which can inhibit further decomposition of the electrolyte. Furthermore, the LiTFPFB based electrolyte also imparts an excellent cycling performance to LiCoO2/Li metal cells for 500 cycles. The outstanding performance of the LiTFPFB salt demonstrates that it is a very promising baseline salt for next generation lithium metal batteries.
The introduction of a bulky electron-withdrawing group into the anion has been considered as one of the most promising strategies for improving the ionic conductivity of the lithium salt due to its weak coulombic interactions.7,8 For example, Ue and coworkers prepared lithium pentafluoroethyltrifluoroborate (LiFAB) by substituting one F− in LiBF4 by a bulky fluoric group.9 The ionic conductivity of 1.0 M LiFAB in EC/EMC (30:70 vol%) reaches 8.0 × 10−4 S cm−1 at room temperature, which is twofold higher than that of LiBF4 (3.6 × 10−4 S cm−1). However, LiFAB displays worse oxidation stability than LiBF4 and deteriorated battery performance at elevated temperature (higher than 60 °C). Alternatively, Zhang synthesized lithium difluoro(oxalate)borate (LiDFOB) by using one oxalate anion to substitute two F− in LiBF4.10 The ionic conductivity is enhanced and simultaneously a stable SEI is formed on the graphite anode. However, LiDFOB is less thermally stable than LiBF4.10
On the other hand, the fluoroalkoxyl functional group, usually existing in fluoric carbonate solvent, can decompose and in situ form an elastomeric polymeric matrix SEI on graphite,11 lithium silicon alloys,12 and Li metal surfaces.13 The as-formed SEI can effectively suppress Li dendrite growth and inhibit further decomposition of the electrolyte,11 making the fluoroalkoxyl functional group very attractive for next generation high energy lithium metal batteries. It is also noted that the introduction of the fluoroalkoxyl group into a lithium or/and magnesium salt anion can significantly improve the oxidation stability of the salt, as observed in Long's14 and our previous studies.15 However, to the best of our knowledge, there are relatively few studies devoted to the introduction of the electron-withdrawing fluoroalkoxyl group into the lithium salt anion to protect the lithium metal anode.
Herein, we for the first time intend to introduce a bulky fluoroalkoxyl functional group to substitute one F− in LiBF4 inspired by the aforementioned advantages of the fluoroalkoxyl group in ionic conductivity and oxidation stability improvement as well as its function in lithium metal protection. As a result, a novel lithium salt, namely the trifluoro(perfluoro-tert-butyloxyl)borate (LiTFPFB) salt (shown in Scheme 1), has been synthesized by a one-step reaction. The effective species of the salt have been analyzed by high resolution mass spectrometry (HR-MS), and 7Li, 11B and 19F NMR. The stability of the LiTFPFB salt to the Al current collector as well as the ionic conductivities has been studied. Moreover, the elevated temperature (60 °C) battery performance of LiFePO4/Li cells and high-voltage performance of LiCoO2/Li cells have also been studied to investigate the feasibility of the salt in high energy lithium metal batteries. Finally, the morphologies and compositions of the cycled Li metal were investigated by SEM imaging and XPS methods to elucidate the compatibility between the LiTFPFB based electrolyte and the lithium metal anode.
The compatibility of LiTFPFB with the Al current collector was characterized by cyclic voltammetry compared with LiBF4. As a reference, the fluoroalkyl-containing salt lithium bis(trifluoromethane-sulphonyl)imide (LiTFSI) in PC solvent was also evaluated (Fig. 3a). For the LiTFSI based electrolyte, the current increases markedly when the applied potential exceeds 4.5 V vs. Li+/Li and persists during the negative sweep down to 3.7 V. Hysteresis in the cyclic voltammogram is an indicator of Al corrosion, which is consistent with the result obtained by Evans et al.19 The low corrosion potential of Al at around 3.7 V may be due to the strong interaction between TFSI− and the cation in the passivation film of Al, which may lead to higher solubility of the passivation species. In sharp contrast, the corresponding current responses of LiBF4 and LiTFPFB electrolytes are much smaller than that of LiTFSI. Furthermore, the cathodic current of the LiTFPFB based electrolyte is smaller than that of LiBF4, as shown in the inset of Fig. 3a. These results indicate that LiTFPFB possesses the best compatibility with the Al current collector among the three measured salts. Moreover, chronoamperometry was further used to evaluate the compatibility of LiBF4 and LiTFPFB with Al (Fig. 3b and S4†).20,21 As depicted in Fig. 3b, the initial rapid decrease of the anodic current on a fresh Al surface indicates instant formation of the passivation layer.22 The LiTFPFB based cell shows no sign of corrosion until the potential reaches ca. 4.5 V, which is consistent with the CV results described above, indicating enhanced Al current collector stability up to 4.5 V versus Li+/Li.21 In addition, the corrosion current collected at t = 103 s vs. the applied potential is plotted in the inset of Fig. 3b. It is noted that the LiTFPFB based electrolyte shows lower current density than that of LiBF4 even above 4.5 V. These results indicate that the LiTFPFB based electrolyte is more compatible with the Al current collector than that of LiBF4.
The oxidation behaviors of both electrolytes were investigated by linear sweep voltammetry (LSV) using Pt as the working electrode. As shown in Fig. 3c, the anodic current of the LiBF4 based electrolyte is very low below 4.5 V (vs. Li+/Li) and then increases distinctly when the voltage exceeds 4.6 V corresponding to the known electrolyte decomposition.23 For the LiTFPFB based electrolyte, the initial oxidation potential is observed at 4.5 V, followed by a slight increase. All these observations above verify that the oxidation decomposition of the electrolyte can be effectively suppressed and the Al current collector can be well passivated with LiTFPFB, which is well in agreement with the calculation result (Table 1).
Moreover, coin-type Cu/Li cells were also used to investigate the cycling stability of Li plating/stripping. As shown in Fig. S8,† the coulombic efficiency of the LiTFPFB based cell is 80.6% after 50 cycles, which is higher than that of the LiBF4 based one (60.3%), indicating improved stability of the LiTFPFB based electrolyte.
To explore the feasibility of lithium metal batteries with the LiTFPFB based electrolyte, long-term cycling measurements of LiFePO4/Li cells using both electrolytes were carried out at room temperature. As shown in Fig. 4b, the initial discharge capacities of the cells using LiBF4 and LiTFPFB at a current rate of 0.2C are 151.4 and 151.9 mA h g−1, respectively. The corresponding coulombic efficiencies of the two cells are 98.1 and 97.3%, respectively. These relatively low coulombic efficiencies are apparently due to the significant decomposition of the electrolyte and SEI formation.22 After the first three cycles for SEI formation, the cells were cycled at a high current rate of 1C (160 mA g−1). As shown in Fig. 4b, after 200 cycles, the LiTFPFB based cell retains nearly 99.3% of its fourth cycle discharge capacity with a smaller overpotential of 0.1 V (Fig. S9a†), while the capacity retention of the LiBF4 based cell is 83.1% with a higher overpotential of 0.12 V (Fig. S9b†). Furthermore, an improved rate performance is also observed using 1.0 M LiTFPFB/PC electrolyte at room temperature (Fig. S10†). To better understand the excellent cell performance, the impedance spectra of the two cells were monitored during cycling and are shown in Fig. 4c and d. In general, the high-frequency intercept is attributed to the bulk resistance (Rb), and the two medium-frequency semicircles are associated with the interface resistance (RSEI) and charge transfer resistance (Rct), respectively. The equivalent circuit curve is shown in Fig. S11† and the values of the fitted impedance parameters are listed in Table S1.† Both the Rb values of the LiTFPFB and LiBF4 based cells remain relatively stable after 1, 50, 100, and 200 cycles (Fig. 4c). The RSEI of the LiTFPFB based cell is about 3.0 Ω after one cycle, and then increases to 3.4, 6.5, and 8.5 Ω, after 50, 100, and 200 cycles, respectively (Fig. 4d). As a comparison, the RSEI of the LiBF4 based cell is about 13.1 Ω after one cycle, and dramatically increases to 26.0, 31.8, and 41.8 Ω after 50, 100, and 200 cycles, respectively (Fig. 4d). The large initial and dramatic increase of RSEI with cycling for the LiBF4 based cell is because the lithium metal anode is continuously consumed by the electrolyte and a thick SEI layer is formed.27
The LiFePO4/Li cells with LiBF4 and LiTFPFB were also cycled at elevated temperature (60 °C), respectively. After three SEI formation cycles at 1C, the cells were cycled at a high current rate of 5C. As depicted in Fig. 5a, the LiTFPFB based battery delivers a superior cycling performance compared to that of the LiBF4 based cell. After 150 cycles, the former retains 98.3% of the fourth cycle discharge capacity, while the capacity retention of the latter is only 62.5%. It is worth noting that the LiFePO4/Li cell also operates well with the LiTFPFB based electrolyte compared with the LiBF4 based one at −5 °C (Fig. S12†). The rate performances of the LiBF4 and LiTFPFB based electrolytes were measured at different rates from 0.2C to 10C at 60 °C. As shown in Fig. 5b, the LiTFPFB based cell shows better rate capability than that of LiBF4 when the rate is varied from 0.2C to 10C. It is indicated that the former delivers a high reversible capacity of 145.8 mA h g−1 at 10C, while the corresponding capacity of the latter is only 116.5 mA h g−1. Furthermore, the selected charge/discharge curves of a LiTFPFB based LiFePO4/Li cell at 1C, 6C and 10C are plotted in the inset of Fig. 5b, demonstrating clear potential plateaus with a small overpotential, which indicates a highly reversible cycling process. The outstanding cycle and rate performance of the LiTFPFB based cells are closely related to the high ionic conductivity and the as-formed protective film on the Li metal anode, which can suppress further decomposition of the electrolyte. To evaluate the morphologies of the Li anodes after long-term cycling, the LiFePO4/Li batteries after 150 cycles were disassembled inside a glovebox with an Ar atmosphere and the obtained electrodes were washed with anhydrous DMC, dried and further analyzed by field emission scanning electron microscopy (FE-SEM). As shown in Fig. 5c–f, the Li surfaces of the LiBF4 and LiTFPFB based cells exhibit entirely different morphologies. It is noted that, for the LiBF4 based LiFePO4/Li cell after 150 cycles at 60 °C, the cycled Li metal exhibits dendritic features with a pulverized and porous morphology (Fig. 5c and d). A large amount of bulk Li was consumed during cycling due to the repeated breakage/repair of the SEI.26 In addition, a pulverized layer is also observed on the newly formed Li dendrite (Fig. 5d). In contrast, the cycled Li metal in the LiTFPFB based cell shows smooth features and absence of Li dendrites (Fig. 5f), although the surface looks rimous (Fig. 5e). These results indicate that the protective film on the Li anode can effectively suppress the parasitic reactions on the surface of the Li anode, thus improving the battery performance.
In order to investigate the composition of the protective film, the surface chemistry of the cycled Li anodes was surveyed using X-ray photoelectron spectroscopy (XPS). Fig. 6 shows the XPS spectra of B 1s, C 1s, O 1s, and F 1s for the cycled Li anodes with 1.0 M LiBF4 and 1.0 M LiTFPFB in PC, respectively. As shown in Fig. 6a, the XPS spectrum of B 1s for the LiBF4 based cell can be deconvoluted into two peaks at 192 and 194 eV, which can be assigned to B–O (reaction product of LiBF4 with ROCO2Li) and B–F species.23,27 In contrast, only B–O species can be observed in the LiTFPFB based cell, indicating the decomposition of TFPFB− on the Li anode. Fig. 6b displays the C 1s spectra, and the three peaks centered at 284.8, 286.2, and 287.9 eV correspond to C–C, C–O, and CO functional groups,27 respectively. The higher concentrations of C–O and CO groups in the LiBF4 based cell can be attributed to PC solvent decomposition, while the higher concentration of C–C combined with lower C–O and CO concentrations in the LiTFPFB based cells might be related to TFPFB− decomposition,28 consistent with the O 1s spectra in Fig. 6c. These results indicate the decomposition of the TFPFB− anion and the formation of a protective film on the Li anode, which can inhibit further decomposition of the electrolyte, coinciding with SEM imaging. Furthermore, as for the F 1s spectra (Fig. 6d), the three peaks located at 684.8, 685.6, and 686.8 eV for the LiTFPFB based cell can be assigned to LiF, C–F, and B–F compounds, respectively,23 which originate from the –CF3 (ref. 13) and –BF3 groups in the TFPFB− anion. Similarly, the LiF and B–F species in the LiBF4 based cell originate from the decomposition of LiBF4. In addition, comparing the Li anode after 1 and 100 cycles, the dramatic concentration increase of C species (from 8.9% to 45.0%) and sharp concentration decrease of F species (from 35.1% to 9.0%) may further verify the decomposition of the TFPFB− anion (Fig. S13, Table S2†), in agreement with the mechanism proposed by Abraham et al.12 Based on the above results, it can be concluded that the decomposition of LiTFPFB can form a protective film containing a large number of C–C groups on the Li anode, which can effectively prevent further corrosion of Li metal.
For practical application in high energy lithium batteries, the LiTFPFB based electrolyte should also be compatible with the LiCoO2 electrode, since it is most commonly used as the standard cathode in state-of-the-art Li ion batteries. To demonstrate the compatibility of LiTFPFB with the LiCoO2 cathode, LiCoO2/Li cells were assembled and evaluated at a current rate of 1C between 2.75 and 4.35 V. Fig. 7 shows the long-term cycling performance of the LiTFPFB and LiBF4 based cells. The initial discharge capacities of the LiTFPFB and LiBF4 based cells are 151.7 and 138 mA h g−1 at 0.2C, with the corresponding coulombic efficiencies of 99.6 and 99.2%, respectively. The former also exhibits a remarkably improved cycling performance compared to the latter at a current rate of 1C (140 mA g−1). The LiTFPFB based cell retains 91.1% of the fourth cycle discharge capacity after 500 cycles with a coulombic efficiency of 99.5%, while the capacity retention of the LiBF4 based cell is 89.2% with a coulombic efficiency of 99.3%. These results indicate that the LiTFPFB based electrolyte is more compatible with the LiCoO2 based cathode than the LiBF4 based one under a high voltage of 4.35 V, making LiTFPFB a promising candidate for practical application in high power and energy density rechargeable lithium batteries.
Fig. 7 Discharge capacities and coulombic efficiencies of the LiCoO2/Li cells using 1.0 M LiTFPFB/PC and 1.0 M LiBF4/PC at a current rate of 1C at room temperature. |
Footnote |
† Electronic supplementary information (ESI) available: Experimental method, synthetic procedure, lithium ion transference number, impedance spectra, equivalent circuit diagram and additional XPS data. See DOI: 10.1039/c8sc00041g |
This journal is © The Royal Society of Chemistry 2018 |