Yanqiong Shi,
Rongrong Miao,
Lei Li*,
Jun Yang*,
Jiulin Wang and
Yanna Nuli
Shanghai Electrochemical Energy Devices Research Centre, School of Chemistry & Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, China. E-mail: lilei0323@sjtu.edu.cn; yangj723@sjtu.edu.cn; Fax: +86-21-54747667; Tel: +86-21-54747667
First published on 9th May 2016
A novel LiFSI/TEGDME-DX electrolyte with good compatibility to a lithium anode is firstly proposed for the rechargeable non-aqueous Li–O2 battery, in which an improved performance with longer cycle life was achieved when compared with the conventional LiTFSI/TEGDME electrolyte.
Many lithium salts, such as LiPF6, Li[N(SO2CF3)2] (LiTFSI), LiCF3SO3, LiClO4, LiBF4, LiCl, and Li[B(C2O4)2] (LiBOB), have been employed in electrolytes for the non-aqueous Li–O2 batteries;13,14 nevertheless, lithium bis(fluorosulfonyl)imide (Li[N(SO2F)2], LiFSI), which possesses high ionic conductivity and excellent chemical stability,15 has not yet been reported. It has been used as a lithium salt in Li–metal battery16 and Li–S battery17 system to modify the solid electrolyte interphase (SEI) with a higher LiF content than that in LiTFSI solution and mitigate the lithium dendrite formation. Qian et al.18 also reported a electrolyte composed of LiFSI and 1,2-dimethoxyethane (DME) achieving a high rate and stable cycling of a lithium anode at high coulombic efficiency without dendrite growth. However, the practical application of DME used in the above electrolytes will be restricted in Li–O2 cells due to its high volatility (boiling point: 83 °C). Herein, a new electrolyte system with LiFSI as the lithium salt is designed for the non-aqueous Li–O2 battery, in which less-volatile and frequently used TEGDME (boiling point: 275 °C) is chosen as the basic solvent, and 1,4-dioxan (DX, boiling point: 101.3 °C), (a symmetrically structured cyclic ether for its probably improved chemical stability) as the 2nd solvent. The electrochemical performance and morphological evolution of a lithium anode in this electrolyte are investigated, and the reversible and improved cycling behaviour of a non-aqueous Li–O2 cell based on a typical air cathode is demonstrated.
Lithium stripping–plating experiments in a symmetric Li|Li cell subjected to galvanostatic cycling at room temperature were performed to evaluate the compatibility between the electrolyte and lithium anode. Fig. 1a and b show the voltage responses of the cells with different electrolytes at a constant current density of 0.25 mA cm−2. The overvoltage profile corresponding to the commonly used electrolyte is unstable and shows a tendency to higher voltage, which finally fails after the cycling operation of ∼230 h (reaching voltage upper-limit of 3 V). In contrast, the voltage is still below 0.06 V when LiFSI replaces LiTFSI. Moreover, the addition of DX solvent further reduces the overvoltage and improves the cycling performance (Fig. 1a). The coupling effect of solvent/salt enables the cell with LiFSI/TEGDME-DX electrolyte to cycle reversibly for 850 h below the voltage of 0.15 V, extending the life cycle nearly 3-fold (Fig. 1b). Fig. S1† further proves the positive effect of DX solvent on prolonging cycling life. Fig. 1b presents the enlarged voltage trends in different electrolytes. In LiTFSI/TEGDME, the voltage fluctuation related to lithium deposition and dissolution is notable for each process; this fluctuation can be explained by the non-uniform current and voltage distribution caused by the uneven morphology and solid electrolyte interphase (SEI) layer on the lithium electrode.19 However, the voltage trends in LiFSI/TEGDME-DX are more stable, and the voltage remains below 0.06 V even after a long time cycling for ∼550 h. Fig. 1c exhibits digital photos of lithium anodes taken after cycle operation. A thick and dark resultant layer adheres to the reaction zone of the lithium disc (Fig. 1c-α) when a conventional electrolyte is used, which could lead to a high interfacial resistance and cell failure. However, the lithium anode in the proposed electrolyte remains neat with metallic brightness, even after long-term cycling of 1000 h (Fig. 1c-β).
The interfacial property was further investigated via EIS measurements. As shown in Fig. 2a, with the increase in cycle number, the interfacial resistance with a LiTFSI-based electrolyte initially decreases due to the activation of the cell, and reaches a minimum and then increases quickly upon cycling until cell failure. In contrast, in the LiFSI based electrolyte, the resistance decreases and then stabilizes at a low value during cycling, which suggests that a relatively stable SEI film is formed, leading to the improved electrochemical stability and long cycle life. Moreover, Fig. 2b indicates that the addition of DX solvent contributes to the formation of a more stable SEI film with a lower resistance, which may be associated with DX for its extremely low reduction potential (−1.95 V vs. Li/Li+), implying a low tendency of a direct reaction between DX solvent and lithium metal. Based on the advantages obtained in the LiFSI/TEGDME-DX electrolyte, extending investigations will be focused on the comparison between this electrolyte system and the conventional LiTFSI/TEGDME system.
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| Fig. 2 Nyquist plots of Li|Li cells, (a) as a function of cycling time; (b) as a function of storage time after 5 cycles. | ||
The surface morphologies of lithium electrodes cycled in Li|Li symmetric cells with different electrolyte solutions are shown in Fig. 3. In view of the fact that a high current density promotes lithium dendrite formation, a large current density of 2 mA cm−2 is applied in this experiment. The lithium metal deposit harvested from the LiFSI/TEGDME-DX electrolyte system presents a compact accumulation of smooth particles (Fig. 3a and b), while a coarse and dendritic Li deposit forms in the LiTFSI/TEGDME electrolyte (Fig. 3c and d). The dendrite-free lithium deposition is probably attributed to the high quality of the SEI film in the proposed electrolyte. The using of less-reactive DX solvent makes the composition of surface layer dominated by FSI−1 anion reduction which could mitigate the lithium dendrite formation as reported in previous research.16
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| Fig. 3 SEM micrographs of Li anode after 10 cycles with 7.2C per process at 2 mA cm−2, (a and b) in LiFSI/TEGDME-DX electrolyte; (c and d) in LiTFSI/TEGDME electrolyte. | ||
The coulombic efficiency was determined using the Li–stainless steel (SS) cells, with the experiment performed as described in the literature;20,21 the value was calculated from the following equation:
| CE = 100 × NQ1/(NQ1 + Q2) | (1) |
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| Fig. 4 (a) Voltage–time profiles of Li|SS cells for the cycling efficiency calculation; (b) steady-state cyclic voltammograms of the electrolytes with a three-electrodes system. | ||
In order to confirm the availability, the 2032-type coin cells were assembled for evaluating the Li–O2 cell performance. Fig. 5a and b exhibit the obvious difference in cycling stability of the cells using different electrolytes at a current density of 200 mA gCNT−1, where more than 45 cycles with fairly good reversibility are achieved by using the proposed electrolyte, in comparison with only 25 cycles for the conventional one. And a lower polarizing voltage was obtained when DX was used as co-solvent (Fig. S3†), which is in accordance with the EIS results mentioned above. Moreover, when a higher current density of 500 mA gCNT−1 was applied with a higher fixing capacity to 1000 mA h gCNT−1, more than 20 stable cycles have been achieved (Fig. 5c), demonstrating a good rate capacity of the Li–O2 cell with the proposed electrolyte. And the stable charge and discharge voltage trends for 20 cycles also indicate the good electrochemical reversibility and kinetics. The XRD pattern in Fig. 5d reveals that Li2O2 is the dominated discharge product, which is essential for the reversible reaction on the oxygen electrode. Although the proposed electrolyte offers a good solution for Li anode compatibility and reversible electrode reactions for Li–O2 cell, one has to be aware that the relatively high charging polarization for the Li–O2 cell might lead to the decomposition of liquid electrolyte and limit the long-term cycle performance. To overcome this problem, better oxygen (or air) cathodes or catalytic electrolyte additives must be developed.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c6ra08318h |
| This journal is © The Royal Society of Chemistry 2016 |