Kun
Yin
a,
Zhengxi
Zhang
*a,
Xiaowei
Li
a,
Li
Yang
*ac,
Kazuhiro
Tachibana
b and
Shin-ichi
Hirano
c
aSchool of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, PR China. E-mail: zhengxizhang@sjtu.edu.cn; Fax: +86 21 54741297; Tel: +86 21 54748917
bDepartment of Chemistry and Chemical Engineering, Faculty of Engineering, Yamagata University, Yamagata 992-8510, Japan
cHirano Institute for Materials Innovation, Shanghai Jiao Tong University, Shanghai 200240, PR China. E-mail: liyangce@sjtu.edu.cn
First published on 5th November 2014
Polymeric ionic liquids (PILs) have stirred up great interest for their potential applications as electrolyte hosts in lithium metal batteries (LMBs) because of their desirable performance. In this work, PIL-based gel polymer electrolytes applied in lithium metal batteries (LMBs) at low–medium temperatures (25 °C, 30 °C and 40 °C) are first reported. A novel imidazolium-tetraalkylammonium-based dicationic polymeric ionic liquid, poly(N,N,N-trimethyl-N-(1-vinlyimidazolium-3-ethyl)-ammonium bis(trifluoromethanesulfonyl)imide) is successfully synthesized, and its structure and purity are confirmed by 1H NMR, FTIR and elemental analysis. Subsequently, the ternary gel polymer electrolytes are prepared by blending the as-synthesized dicationic PIL as the polymer host with 1,2-dimethyl-3-ethoxyethyl imidazolium bis(trifluoromethanesulfonyl)imide (IM(2o2)11TFSI) ionic liquid and LiTFSI salt in different weight ratios. The PIL-LiTFSI-IM(2o2)11TFSI electrolytes reveal low glass transition temperatures around −54 °C and high thermal stability to about 330 °C. Moreover, the ternary gel polymer electrolytes show good ion conductivity around 10−4 S cm−1 at low–medium temperatures, high electrochemical stability and good interfacial stability with lithium metal. Particularly, the Li/LiFePO4 cells assembled with polymer electrolytes at a rate of 0.1 C are able to deliver discharge capacities of about 160 mA h g−1, 140 mA h g−1 and 120 mA h g−1 at 40 °C, 30 °C and 25 °C, respectively, with excellent capacity retention, as well as exhibiting acceptable rate capability. These findings reveal that dicationic PIL-based electrolytes have great potential for use as safe electrolytes in LMBs.
Gel polymer electrolytes (GPEs), which use polymer hosts to immobilize liquid electrolytes, combine the advantages of polymer materials (avoiding liquid leakage, no separator needed) with those of liquid electrolytes (good electrochemical properties).5,6 Furthermore, it has been confirmed that compared to liquid electrolytes, dendrite formation could be suppressed in GPEs because of the immobility of electrolyte molecules.7–10 In view of these superior properties, GPEs have attracted great attention as promising safe electrolytes in recent years. To date, two types of host polymers are introduced for GPE preparation. The first one is the conventional polymer materials, including poly(ethylene oxide) (PEO), poly(vinylidene fluoride) (PVdF), poly(methyl methacrylate) (PMMA), poly(acrylonitrile) (PAN), and co-polymers or blends of these systems.11–13 However, GPEs based on the conventional polymer hosts mentioned above still encounter a lack of stability with time due to the leaching of liquid from GPEs.5,14 The second species is polymeric ionic liquids (PILs), in which ion species remain covalently bound to the polymer backbone.15 PILs represent a significant class of materials as they show interesting properties, such as high thermal stability, good film forming ability and chemical compatibility with ionic liquids (ILs).16,17 In spite of extensive research into the synthesis and properties of PILs over the past decade,15,18–24 few PILs as hosts in GPEs have been applied in LMBs. Appetecchi et al.25 first explored the application of GPEs with the pyrrolidinium-based PIL as the host in LMBs. The Li/LiFePO4 cells at 40 °C can deliver a discharge capacity of 144.1 mA h g−1 at a rate of 0.1 C. Later, Li et al.26,27 prepared GPEs based on guanidinium-based PILs as polymer hosts, and studied their performance in LMBs. It was found that although the Li/LiFePO4 cells export discharge capacities of about 140 mA h g−1 at a rate of 0.1 C at a high temperature (80 °C), they are not able to permit operation at the lower temperature. Subsequently, Li et al.28,29 further synthesized homo tetraalkylammonium-based PILs as hosts in GPEs, and the Li/LiFePO4 cells containing such GPEs are capable of properly operating at 60 °C. Recently, imidazolium-based PIL electrolytes applied in LMBs have been reported by our group,30 and the cell test revealed that Li/LiFePO4 cells containing GPEs with the imidazolium-based PIL host obtained by the desirable synthetic route can achieve discharge capacities of about 160 mA h g−1 at a rate of 0.1 C and 60 °C. According to these previous works, we could find that PILs commonly have monocationic center repeating units, i.e. monocationic PILs. Moreover, most of the monocationic PIL-based electrolytes applied in LMBs are operated only at/above 60 °C, while quite few monocationic PIL-based electrolytes could be performed well in LMBs at 40 °C. Whether LMBs assembled with PIL-based electrolytes exhibit satisfactory performance at low–medium temperatures, i.e. from room temperature to 40 °C, remains an unanswered issue that must be addressed in promoting the practical use of LMBs. In order to respond effectively to this challenge, it is imperative and important to explore PILs with new structures, other than monocationic PILs, as hosts in GPEs.
Inspired by the above analysis, in this article we synthesized a novel dicationic PIL, that is imidazolium-tetraalkylammonium-based PIL, poly(N,N,N-trimethyl-N-(1-vinlyimidazolium-3-ethyl)-ammonium bis(trifluoromethanesulfonyl)imide) (poly[VIm][TMEN][TFSI]), as outlined in Fig. 1(a). At the same time, GPEs with different weight compositions were obtained by incorporating the PIL (poly[VIm][TMEN][TFSI]) as the polymer host, a 1,2-dimethyl-3-ethoxyethyl imidazolium bis(trifluoromethanesulfonyl)imide (IM(2o2)11TFSI) ionic liquid shown in Fig. 1(b) and the LiTFSI salt. The thermal and electrochemical properties for as-obtained ternary GPEs were investigated, and their potential application in LMBs at low–medium temperatures (25 °C, 30 °C and 40 °C) were evaluated.
Fig. 1 (a) Synthetic route of the imidazolium-tetraalkylammonium-based PIL. (b) Structure of IM(2o2)11TFSI. (c) Picture of a PIL-LiTFSI-IM(2o2)11TFSI electrolyte (PVImN-95 sample). |
Sample | Weight composition (wt%) | ||
---|---|---|---|
Poly[VIm][TMEN][TFSI] (host) | IM(2o2)11TFSI (ionic liquid) | LiTFSI (Li salt) | |
PVImN-90 | 100 | 90 | 30 |
PVImN-95 | 100 | 95 | 30 |
PVImN-100 | 100 | 100 | 30 |
The intrinsic viscosity ([η]) of poly[VIm][TMEN][TFSI] was measured by employing an Ubbelohde dilution viscometer at 25 °C in acetone. The value of the viscosity-average molecular weight (Mv) of poly[VIm][TMEN][TFSI] was calculated using the Mark–Houwink–Sakurada equation [η] = KMva, wherein K = 6.76 × 10−3 cm3 g−1 and a = 0.71, which were determined in a PMMA/acetone solution at 25 °C.32 The result showed that [η] = 113.9 cm3 g−1, and Mv = 1.13 × 106 g mol−1.
The calorimetric measurements were made with a differential scanning calorimeter (DSC, TA Instruments Q2000) in the temperature range −80 °C to 200 °C. The PIL and electrolyte samples (about 15 mg) were sealed in aluminum pan, then heated and cooled at a scan rate of 10 °C min−1 under a flow of nitrogen. The thermal data were collected during heating in the second heating scan. The thermal stabilities were measured with TGA (TA Instruments Q5000) in the temperature range 40–600 °C, under N2 atmosphere at a heating rate of 10 °C min−1.
The ionic conductivity of the PIL-LiTFSI-IM(2o2)11TFSI electrolyte membrane was measured by impedance measurements using a CHI660B Electrochemical Workstation. The data were collected over the frequency range 0.1–100 kHz with amplitude 5 mV for an open circuit potential from 25 to 90 °C. The ionic conductivity (σ) of polymer electrolytes was calculated using the following equation:
The electrochemical stability of as-prepared dicationic PIL-based electrolytes was evaluated by linear sweep voltammetry (LSV) at 40 °C (scan rate 10 mV s−1) with a CHI660B Electrochemical Workstation. The cells used for this investigation were assembled by sandwiching dicationic PIL-based electrolyte between the stainless steel (SS) and the lithium metal, in which the stainless steel was employed as the working electrode and the lithium metal was employed as counter and reference electrodes. Separate tests were performed on each sample for the cathodic and anodic stability measurements by scanning the cell potential from open-circuit voltage to positive (anodic) or negative (cathodic) voltages.
Symmetric lithium metal coin cells (CR2016 stainless steel cell, 16 mm diameter disc of lithium metal and dicationic PIL-based electrolyte) were assembled in the glove box. After the cells had been kept at open circuit at 40 °C for 36 h, charge–discharge cycling was measured at the CT2001A cell test instrument (LAND Electronic Co., Ltd.) at 40 °C under two current densities, 0.05 mA cm−2 and 0.1 mA cm−2, for each polarization (16 min charge and 16 min discharge). Impedance spectroscopy of the symmetrical cell was undertaken on a CHI660B Electrochemical Workstation (0.1–100 kHz, amplitude voltage 5 mV) at 40 °C before and after cycling.
The cycling tests on Li/PIL-based electrolyte/LiFePO4 batteries were performed at low–medium temperatures (25 °C, 30 °C and 40 °C) using a CT2001A cell test instrument (LAND Electronic Co., Ltd.). The discharge current rates were varied from 0.1 C to 1 C, while the charge current rate was fixed at 0.1 C. Constant current charge–discharge cycles were tested between 2.5 and 4.0 V (vs. Li/Li+).
The thermal properties of the neat PIL polymer and PIL-based electrolytes were evaluated by DSC (Fig. 3(a)) and TGA (Fig. 3(b)) measurements. As clearly evidenced from Fig. 3(a), the neat PIL polymer only shows a glass transition temperature (Tg) at around 106.6 °C, indicating an amorphous polymer. According to our previous report,31 the neat IM(2o2)11TFSI ionic liquid does not exhibit any phase transition behavior until −60 °C during the second heating scan process, thus its melting point can be denoted as <−60 °C. Moreover, it can be seen that the addition of the IM(2o2)11TFSI ionic liquid to the PIL polymer could drastically decrease the glass transition temperature. This drop in Tg can be attributed to the fact that the IM(2o2)11TFSI IL as a plasticizer in the electrolytes increases the free volume of the PIL, and further helps the segmental motion of the PIL chains.35 When the IM(2o2)11TFSI content reaches 90 wt%, 95 wt% and 100 wt% (with respect to the host), the Tg of PIL-based electrolytes decreased to about −52 °C, −54 °C and −56 °C, respectively. The decrease in Tg with the slight increase in IM(2o2)11TFSI content demonstrates that the glass transition feature of the PIL-based electrolytes would be sensitive to the IM(2o2)11TFSI content change. In addition, no other endothermic peaks are observed in the DSC traces of PIL-based electrolytes, suggesting that a lithium salt/ionic liquid phase separation phenomenon does not occur. This result is similar to the investigation of the previously reported mono-guanidinium based PIL electrolytes containing a guanidinium IL,26 however it is different from that reported for mono-pyrrolidinium based PIL electrolytes incorporating a pyrrolidinium IL.25
Fig. 3 (a) DSC curves and (b) TGA curves of neat PIL polymer and PIL-LiTFSI-IM(2o2)11TFSI electrolyte samples with different IM(2o2)11TFSI contents. Scan rate: 10 °C min−1. |
Thermal stability is also an important parameter for evaluating PIL-based electrolytes. Fig. 3(b) displays TGA curves of neat PIL polymer and PIL-LiTFSI-IM(2o2)11TFSI electrolytes at different IM(2o2)11TFSI contents. The thermal decomposition temperatures (Td) are measured at 5% weight loss. It appears clearly that the neat PIL polymer and PIL-LiTFSI-IM(2o2)11TFSI electrolyte samples all exhibit one-step thermal decomposition behaviors, which are different from those obtained for the mono-guanidinium based PIL electrolytes containing a guanidinium IL. It has been reported that mono-guanidinium based PIL electrolytes undergo two-step thermal decomposition.26 Furthermore, the as-obtained neat PIL and PIL-based electrolyte samples have high thermal stability, and the decomposition temperatures of PIL, PVImN-90, PVImN-95 and PVImN-100 electrolytes are about 320 °C, 326 °C, 348 °C and 345 °C, respectively.
Considering that ionic conductivity is one of the crucial properties for the electrochemical applications of electrolytes, the ionic conductivity as a function of temperature for PIL-LiTFSI-IM(2o2)11TFSI electrolyte samples is evaluated, and the corresponding results are presented in Fig. 4(a). It is apparent that ionic conductivity increases with increasing temperature for the three investigated electrolyte samples, typically observed in polymer electrolytes. Faster migration of carrier ions and easier motion of PIL segments at higher temperatures are responsible for this phenomenon.36,37 All of the electrolyte samples exhibit Arrhenius behavior over the measured temperature range (25–90 °C). It can also be observed that the ion conductivity depends on the PIL host and ionic liquid ratio. The higher the ionic liquid content in the PIL-based electrolytes, the bigger the local space for the motion of polymer segments, as well as a larger microscopically liquid environment for carrier ions, which thus improves the ion-transporting property and consequently increases ion conductivity.29,38 This is consistent with DSC analysis from Fig. 3(a). The PVImN-100 sample exhibits an ionic conductivity of 0.46 × 10−4 S cm−1 and 1.37 × 10−4 S cm−1 at 25 °C and 40 °C, respectively. This result suggests that the as-prepared PIL-based electrolytes could be used as promising electrolytes for lithium metal battery applications at low–medium temperatures. It should be noted that as the content of the IM(2o2)11TFSI ionic liquid is increased above 100 wt%, the electrolyte membranes are sticky and difficult to handle.
Comparing the dicationic PIL (poly[VIm][TMEN][TFSI]) obtained in this work with the monocationic PIL, poly(1-ethyl-3-vinylimidazolium bis(trifluoromethanesulfonylimide)) (P(EtVIm-TFSI)), prepared in our previous work,30 obvious differences of IM(2o2)11TFSI ionic liquid incorporating ability can be observed. In the case of the monocationic PIL (P(EtVIm-TFSI)) as the polymer host, the maximum content of IM(2o2)11TFSI ionic liquid in the polymer electrolyte is about 65 wt% (with respect to host), which is far below that in the dicationic PIL (poly[VIm][TMEN][TFSI]) host (95–100 wt%). Considering that these two PILs are synthesized from the same homopolymer precursor (PVIm), the resulting dicationic PIL (poly[VIm][TMEN][TFSI]) and monocationic PIL (P(EtVIm-TFSI)) have the same degree of polymerization. Therefore, such differences of ionic liquid incorporating ability might be due to the different charge density and molecular structure between the dicationic PIL and monocationic PIL.
The electrochemical stability is also an important parameter to evaluate the potential applications of electrolytes. The results of linear sweep voltammograms of PIL-LiTFSI-IM(2o2)11TFSI electrolytes at 40 °C are shown in Fig. 4(b). It is clear that the current potential curves display almost no residual current between the cathodic and anodic decomposition voltages, indicating high purity of the PIL-based electrolytes, because the electrolyte system is electrochemically sensitive to impurities. In all cases, the cathodic and anodic decomposition voltages of PIL-based electrolytes are about 1.3 V (vs. Li/Li+) and 4.5 V (vs. Li/Li+), respectively. These results make the as-obtained PIL-based electrolytes promising candidates for LMBs.
In order to study the interfacial characteristics of the PIL-based electrolyte/lithium metal, charge–discharge cycling tests of lithium symmetrical cells containing the PVImN-95 electrolyte were performed, and electrochemical impedance spectroscopy (EIS) before and after the cycling was also measured. Fig. 5(a) and (b) show that the voltage–time (V–t) profiles of lithium symmetrical cells underwent 100 charge–discharge cycles at 0.05 mA cm−2 and 0.1 mA cm−2 at 40 °C, respectively. As expected, the voltage profiles do not exhibit huge random fluctuations and a sudden voltage drop with continued cycling, indicating that a stable SEI film formed on the lithium metal and no short-circuit effect occurred, as mentioned by previous reports.39–42 This finding confirms that the PVImN-95 electrolyte is efficient in promoting uniform Li electrodeposition on the lithium metal and possesses the advantage of suppressing the dendritic growth of lithium. In addition, it can be found that the overvoltage of the cell cycled at a current density of 0.05 mA cm−2 almost keeps a stable value, while a slight increase in overvoltage comes along with the cycling for the cell cycled at 0.1 mA cm−2, which can be explained by the fact that the polarization effect is more intensive at higher charge–discharge current density. Fig. 5(c) and (d) show the EIS results before and after the cycling test. The intercept of the impedance response with the real axis at high frequency represents the electrolyte bulk resistance (Rb), and the diameter of the semicircle reflects the interfacial resistance (Ri) of the PVImN-95 electrolyte/lithium metal.43 It is obvious that Rb for the PVImN-95 electrolyte tested at 0.05 mA cm−2 and 0.1 mA cm−2 remains constant before and after the cycling, which indicates that the PVImN-95 electrolyte has excellent stability itself. Moreover, Ri for the PVImN-95 electrolyte had only little changes after the cycling tests, implying good compatibility between the PVImN-95 electrolyte and the lithium metal.
Fig. 6 depicts the cycling performance of Li/LiFePO4 cells containing PIL-LiTFSI-IM(2o2)11TFSI electrolytes at 40 °C. The cells with PVImN-100, PVImN-95 and PVImN-90 electrolytes all deliver initial discharge capacities of about 140 mA h g−1 at a current rate of 0.1 C. Also, in all cases, the discharge capacities steadily increase with ongoing cycling, which can be ascribed to the optimization of the electrode–electrolyte interfaces,44 as commonly observed in monocationic PIL-based electrolytes.28,30 As for PVImN-100 and PVImN-95 electrolytes, the discharge capacities increase to approximately 160 mA h g−1 after 20 and 25 cycles, respectively, which is very close to the theoretical capacity (170 mA h g−1), and then discharge capacities of 161.5 mA h g−1 and 161.1 mA h g−1 can still remain after 50 cycles, respectively. This result shows that the cells with as-prepared polymer electrolytes exhibit high discharge capacity and excellent capacity retention. Owing to the fact that both the PVImN-95 electrolyte and the PVImN-100 electrolyte possess very similar cell performance, as well as the fact that the PVImN-95 electrolyte consumes a smaller amount of ionic liquid, in the following we select the PVImN-95 electrolyte as a representative of dicationic PIL-based electrolytes to be further evaluated in Li/LiFePO4 cells.
Fig. 6 Cycling performance of Li/LiFePO4 cells containing PIL-LiTFSI-IM(2o2)11TFSI electrolyte samples at 40 °C (2.5–4.0 V); the charge–discharge current rate is 0.1 C. |
The performance of the Li/LiFePO4 cell containing the PVImN-95 electrolyte at various temperatures (25 °C, 30 °C and 40 °C) is studied and the results are shown in Fig. 7. Fig. 7(a) reports the initial charge–discharge curves of the Li/PVImN-95/LiFePO4 cells. During the initial charge–discharge cycle at 25 °C, 30 °C and 40 °C, the cells deliver discharge capacities of 110.3 mA h g−1 with 83.9% coulombic efficiency, 124.4 mA h g−1 with 85.2% coulombic efficiency and 139.8 mA h g−1 with 87.3% coulombic efficiency, respectively. The irreversible capacity loss in the first cycle is attributed to the formation of a protective solid electrolyte interface (SEI) film at the lithium anode.45,46 In the case of the cells operating at 30 °C and 40 °C, the initial charge–discharge profiles show a flat plateau at 3.5 V (vs. Li/Li+) and 3.4–3.3 V (vs. Li/Li+), which is a typical feature of Li/LiFePO4 batteries.25,30,37 It can also be found that the voltage polarization effect between the charge and discharge plateaus becomes more intensive when the temperature decreases from 40 °C to 25 °C, suggesting an increase in the internal resistance of the lithium cell. Fig. 7(b) and (c) illustrate the cycle-number dependence of the discharge capacity and coulombic efficiency of Li/PVImN-95/LiFePO4 cells, respectively. As clearly evidenced from Fig. 7(b), the discharge capacity increase with increasing operational temperature, because the ion transfer in the PIL-based electrolyte becomes faster, and the extraction and insertion of the lithium ion into the LiFePO4 electrode become easier at higher temperature.47 As mentioned above, the Li/PVImN-95/LiFePO4 cell tested at 40 °C exhibits a high discharge capacity of 161.1 mA h g−1 (94.8% of the theoretical value) after 50 cycles. When the operational temperature decreases to 30 °C, the cell is capable of achieving a discharge capacity of approximately 140 mA h g−1 after the initial 10 cycles, and still maintains a discharge capacity of 141.7 mA h g−1 (83.4% of the theoretical value) after 50 cycles, indicating satisfactory discharge capacity and excellent cycling performance at 30 °C, which would meet the energy density requirement for battery applications. As the operational temperature further decreases to 25 °C, a stable discharge capacity of about 120 mA h g−1 (70.6% the theoretical value) can still be obtained after 50 cycles. In addition, from Fig. 7(c), we can observe that the coulombic efficiency approaches above 99% after several cycles for the cells, which reflects their highly reversible charge–discharge ability. Such findings reveal that the dicationic PIL-based electrolytes prepared in this work exhibit cell performances that are comparable to and, in some cases, even better than those for PIL-based electrolytes reported in recent literature.25,28–30 The rate performance of the Li/LiFePO4 cell containing PVImN-95 electrolyte is also preliminarily investigated to exploit the potential application in high-power lithium batteries, and the results are shown in Fig. 7(d). It can be seen that increasing the discharge current rate leads to a drop in the discharge plateau voltage, which is due to enhancement of the cell polarization. In the cases of 0.1 C and 0.5 C rates, the discharge processes are revealed by 3.4 V (vs. Li/Li+) and 3.2–3.1 V (vs. Li/Li+), respectively. While the rate is up to 1.0 C, the flat plateau is not clearly visible. This trend is similar to those reported in previous works.25,47 Despite all that, under these conditions, the cell still shows an acceptable rate capability with stable discharge capacities of about 160 mA h g−1 (0.1 C), 128.8 mA h g−1 (0.5 C) and 83 mA h g−1 (1.0 C) in this system.
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