Solid State Ionics 178 (2007) 1235 – 1241 www.elsevier.com/locate/ssi

Poly(ethylene oxide)-based polymer electrolyte incorporating room-temperature ionic liquid for lithium batteries Jae-Won Choi a , Gouri Cheruvally a , Yeon-Hwa Kim a , Jae-Kwang Kim a , James Manuel a , Prasanth Raghavan a , Jou-Hyeon Ahn a,⁎, Ki-Won Kim b , Hyo-Jun Ahn b , Doo Seong Choi c , Choong Eui Song c a

b

Department of Chemical and Biological Engineering and ITRC for Energy Storage and Conversion, Gyeongsang National University, 900 Gajwa-dong, Jinju 660-701, South Korea School of Nano and Advanced Materials Engineering and ITRC for Energy Storage and Conversion, Gyeongsang National University, 900 Gajwa-dong, Jinju 660-701, South Korea c Institute of Basic Science and Department of Chemistry, Sungkyunkwan University, 300 Cheoncheon-dong, Jangan-gu, Suwon City, Gyeonggi-do, South Korea Received 29 March 2007; received in revised form 29 May 2007; accepted 12 June 2007

Abstract The effect of incorporating a room temperature ionic liquid, 1-butyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide (BMITFSI), in the polymer electrolyte (PE) based on poly(ethylene oxide)-(lithium bis(trifluoromethanesulfonyl) imide) [PEO-LiTFSI] was investigated. BMITFSI content was varied between 20 and 80 parts by weight (pbw) in 100 pbw of PEO-LiTFSI and the influence on ionic conductivity, electrochemical stability and interfacial properties on lithium electrode was studied. A remarkable increase in ionic conductivity was achieved with BMITFSI addition, the effect being most pronounced at lower temperatures. Compared to PEO-LiTFSI, the PEs containing BMITFSI exhibited well-defined redox peaks corresponding to stripping and deposition of lithium. The PEs containing BMITFSI exhibited good electrochemical stability and significantly low interfacial resistance with the lithium electrode. Good discharge performance with 82% active material utilization and stable cycling property was achieved when the PE containing 60 pbw of BMITFSI was evaluated in Li/LiFePO4 cells at 40 °C. © 2007 Elsevier B.V. All rights reserved. Keywords: Room temperature ionic liquid; Polymer electrolyte; Lithium battery; Ionic conductivity; Imidazolium salts

1. Introduction Rechargeable lithium metal polymer battery (LMPB) that employs lithium metal as anode and a polymer electrolyte (PE) for charge transportation is considered to be an ideal power source for a number of applications including portable electronic devices and electric vehicles. For attaining a high and reversible specific energy from a LMPB, it is inevitable that the repetitive deposition and stripping of lithium remains highly reversible during the electrochemical process. Since cycling of lithium metal is known to result in deposition of lithium dendrites that can decrease cycle life of the cell and cause safety concerns, development of suitable ⁎ Corresponding author. Fax: +82 55 753 1806. E-mail address: [email protected] (J.-H. Ahn). 0167-2738/$ - see front matter © 2007 Elsevier B.V. All rights reserved. doi:10.1016/j.ssi.2007.06.006

electrolytes that can suppress the dendrite growth and improve plating morphology has been pursued actively [1]. Poly(ethylene oxide) (PEO)-based electrolyte is one of the most promising and widely studied solid PE, mainly because of the good mechanical and thermal properties and interfacial stability with lithium metal. The prototypical solid PE is PEO-LiX, prepared by blending PEO with lithium salt (LiX) of a large anion [2,3]. The transport of Li+ ions in these electrolytes has been associated with the local relaxation and segmental motion of the amorphous regions in the PEO chains. These polymers often show higher crystallinity at lower temperatures and the electrolytes exhibit low room temperature ionic conductivity (typically ≤10− 5 S/cm). This necessitates operation at higher temperatures (generally, N70 °C) for successful utilization of them in practical applications. With PEO-based gel electrolytes formed by

1236

J.-W. Choi et al. / Solid State Ionics 178 (2007) 1235–1241

incorporating molecular solvents that can compete with ether “O” atoms of polymer for Li+ coordination, a significant increase in room temperature ionic conductivity has been reported [4]. However, the reactivity of such solvents leads to poor interfacial stability with lithium metal and their volatile nature causes safety concerns in case of an unexpected short circuit in the battery. Another approach recently adopted has been to incorporate a room temperature ionic liquid (RTIL) in PEO-LiX solid PE. RTILs are molten salts having a low melting point and exist as liquids at or below room temperature [5]. Unlike molecular solvents, RTILs are nonflammable and nonvolatile and hence cause no detrimental effect on the safety aspects of the battery. In addition, RTILs generally possess high ionic conductivity, high chemical and thermal stability, a wide electrochemical window and low toxicity [5]. Different types of RTILs such as those with cations based on imidazolium [6–8], pyrrolidinium [9–13], piperidinium [14,15], morpholinium [16] and quarternary ammonium [17] have been investigated as electrolytes for battery/capacitor applications either solely [6,14] or as the solvent when incorporated in gel/polymer electrolytes [7,9–13,16]. Shin et al. studied the suitability of PEOLiTFSI electrolyte incorporating the RTIL based on pyrrolidinium cation, PYR13TFSI {N-methyl-N-propylpyrrolidinium bis(trifluoromethanesulfonylimide)} for LMPB [9–13] and reported good compatibility with lithium electrode, enhanced ionic conductivity and satisfactory performance at a moderate rate (0.05 C) and temperature (40 °C). 1-butyl-3-methylimidazolium (BMI+)-based RTILs have been less explored as electrolytes [18–20]. Nevertheless, a comparison of the following properties reported for the two RTILs, BMITFSI and PYR13TFSI respectively [5] leads one to expect a better performance from BMITFSI: melting point: −4 °C vs. 12 °C; ionic conductivity: 3.9 mS/cm at 20 °C vs. 1.4 mS/cm at 25 °C; molar conductivity: 1.14 cm2/Ω mol vs. 0.39 cm2/Ω mol; viscosity: 52 cP at 20 °C vs. 63 cP at 25 °C; cathodic limit −2 V vs. −1.5 V; anodic limit 2.6 V vs. 2.2 V; electro-chemical window: 4.6 vs. 3.7 (with Pt working electrode, Ag|Ag+ in DMSO reference electrode). In an earlier study we compared the electrochemical properties of PEO-LiTFSI electrolyte incorporating three RTILs based on BMI cation, and achieved enhanced performance; the best results were with BMITFSI [21]. In the present study, the effect of varying the content of BMITFSI in PEO-LiTFSI electrolyte on the electrochemical and interfacial properties of LMPB has been evaluated. 2. Experimental 2.1. Preparation of PEs The RTIL, BMITFSI was synthesized by a procedure reported by Farmer et al. [22], by the reaction of 1-butyl-3-methylimidazolium chloride with LiTFSI. PEO (Aldrich, Mw = 2 × 106) and LiTFSI (Aldrich) were vacuum dried for 20 h at 50 °C and 110 °C respectively before use. PEs were prepared by a solvent-free, hotpressing procedure. PEO-LiTFSI electrolyte was made by blending PEO corresponding to 20 mol of EO (ethylene oxide) units with 1 mol of Li salt. For preparing PEs incorporating BMITFSI, 100 parts by weight (pbw) of PEO-LiTFSI was blended

with BMITFSI of 20, 40, 60 and 80 pbw. The PEs containing BMITFSI are designated as PEO-LiTFSI-BMITFSI(X), where X denotes 20, 40, 60 or 80. For example, PEO-LiTFSI-BMITFSI(20) denotes mixing of 100 pbw of PEO-LiTFSI with 20 pbw of BMITFSI (i.e. 100 mg of PEO-LiTFSI with 20 mg of BMITFSI). The ingredients were initially mixed at room temperature in a ball mill at 100 rpm for 1 h. For this, a ball-to-powder ratio of 10:1 was employed and hardened stainless steel (SS) balls of 10 mm and 5 mm diameters were used. The homogenous mixture so obtained was placed between two plastic sheets and hot pressed in an aluminum mold at 100 °C for 30 min, applying a pressure of ∼0.5 MPa. PE membranes of average thickness 200 μm with good homogeneity and mechanical strength were obtained with this procedure. PEs were prepared in an argon-filled glove box with a moisture level b10 ppm. For the ball-milling step, which required operation in open air, the materials were first housed in sealed vials and then removed from the dry-box. After completing the ball-mill mixing, it was put back in dry box for further processing. 2.2. Measurements The ionic conductivities of the PEs were measured by the AC impedance method using SS Swagelok® cells with an IM6 frequency analyzer. The electrolyte sample was sandwiched between two SS electrodes and the impedance measurements were carried out at 10 mV amplitude over the frequency range 100 mHz to 2 MHz. The ionic conductivity as a function of temperature was determined in the temperature range 25 to 80 °C. The cell was kept at each measuring temperature for a minimum time of 30 min to ensure thermal equilibration of the sample at that temperature before measurement. The ionic conductivity (σ) was calculated as σ =t/RA; where t and A denote the thickness and area respectively of the PE and R denotes the bulk resistance of the electrolyte obtained as the x-axis intercept of the AC impedance response, when it showed no change in shape with frequency. Thermal properties were evaluated by differential scanning calorimetry (DSC) using TA 2040 instrument at a heating rate of 10 °C/min. The interfacial resistance between the PE and lithium metal electrode was measured at room temperature by the impedance response of Li/PE/Li cells over the frequency range 10 mHz to 2 MHz. Cyclic voltammetry (CV) of the electrolyte sandwiched between lithium electrodes was measured at room temperature at a scan rate of 1 mV/s between −1 and +1 V. Two-electrode cells were assembled by sandwiching PE between lithium metal anode (300 μm thickness, Cyprus Foote Mineral Co.) and carbon-coated lithium iron phosphate (LiFePO4) cathode in SS Swagelok® type, circular cells of 23 mm diameter. LiFePO4 was prepared in-house by mechanical activation followed by solid state reaction at high temperature [23]. Electrochemical performance tests were carried out using an automatic galvanostatic charge-discharge unit, WBCS3000 battery cycler (WonA Tech. Co.), between 2.0 and 4.2 V at 25 and 40 °C, at a current density of 0.05 C. 3. Results and discussion Ball-milling method is known to be an effective way to prepare PE based on PEO-LiX since it results in higher amorphous

J.-W. Choi et al. / Solid State Ionics 178 (2007) 1235–1241

domains of PEO with small spherulitic morphology leading to enhanced ionic conductivity, especially at lower temperatures [3]. In the present study, a solvent-free method consisting of ballmilling and hot-pressing steps has been adopted to prepare the PEs. The method results in getting thin and homogenous electrolyte films. PEs containing 0 to 60 pbw of BMITFSI are free-standing, non-tacky films (slightly tacky with 60 pbw of BMITFSI) that are easy to handle. With 80 pbw of BMITFSI, the film becomes highly tacky, looses mechanical integrity and handling becomes difficult. Hence, compositions with N 80 pbw of BMITFSI have not been considered worthy of evaluation for developing solid PEs. Fig. 1 presents the DSC traces of PEO, BMITFSI and the PEs with and without RTIL. PEO exhibits a crystalline melting transition, starting at 60 °C, with a melting peak (Tm) at 74 °C. The polymer is predominantly crystalline since a well-defined glass transition (Tg) corresponding to the amorphous phase is absent. PEO-LiTFSI electrolyte has a Tm at 63 °C, lower than that of pure PEO. This implies the existence of interactions between ether “O” atoms of PEO and Li+ ions that lead to an inhibition of the effective reorganization of PEO chains for crystallization to occur [24]. A weak Tg at − 30 °C, indicating the presence of amorphous phase is observed for PEO-LiTFSI. BMITFSI has an endothermic transition at − 3 °C, corresponding to its Tm. Incorporation of BMITFSI in PEOLiTFSI results in a further decrease of Tm of PEO. For e.g., the Tm of PEO-LiTFSI-BMITFSI(80) is 55 °C, lower than that of PEO-LiTFSI by 8 °C. The amorphous phase becomes more predominant in the electrolyte containing BMITFSI and a stronger, well-defined Tg occurs at − 60 °C. Thus, it is inferred that PEO-LiTFSI-BMITFSI consists of a significant amorphous phase which is formed by the interaction of BMITFSI, LiTFSI and a portion of PEO, and the remainder of PEO forms the crystalline phase. Shin et al. have also observed similar DSC results by incorporating a pyrrolidinium-based RTIL in PEOLiTFSI [9,13]. The temperature dependence of ionic conductivity of the PEs has been studied by AC impedance spectroscopy. Fig. 2(a) shows the impedance response of PEO-LiTFSI at 25 °C and 80 °C (the minimum and maximum temperatures studied here). At 25 °C, the impedance response is in the form of a semicircle observed at

Fig. 1. DSC traces of PEO, PEO-LiTFSI, BMITFSI and PEO-LiTFSI-BMITFSI (80).

1237

Fig. 2. AC impedance spectra at 25 °C and 80 °C of (a) PEO-LiTFSI, (b) PEOLiTFSI-BMITFSI(80).

medium-high frequencies and a straight line inclined with respect to the real axis at lower frequencies. This type of behavior is typical for a PE sandwiched between two quasi-blocking electrodes [2]. At 80 °C, the ionic resistance of PEO-LiTFSI decreases considerably with a shift of the semicircle to higher frequencies and hence shows only the straight line part of impedance in the spectrum. Such a behavior is observed at temperatures above 60 °C, where the crystalline segments of PEO melt, increasing the overall mobility of ions in the electrolyte. The impedance behavior of PEO-LiTFSI-BMITFSI(80) at 25 °C and 80 °C is shown in Fig. 2(b). For this system, the ionic resistance is seen to be low even at the minimum temperature of 25 °C and as a result the semicircle gets shifted to higher frequencies. Compared to PEOLiTFSI, the ionic resistance of PE containing BMITFSI is lower by 6790 Ω at 25 °C and by 25 Ω at 80 °C. Thus, the incorporation of BMITFSI in the solid PE significantly reduces the electrolyte resistance, and the effect is more pronounced at lower temperatures. The variation of ionic conductivity with temperature for PEOLiTFSI with varying BMITFSI content is presented in Fig. 3. The ionic conductivity of PEO-LiTFSI varies between 4.0× 10− 6 S/cm at 25 °C and 8.2 × 10− 4 S/cm at 80 °C. The RTIL, BMITFSI has an ionic conductivity of 3.9× 10− 3 S/cm at 20 °C [5]. The ionic conductivity of PEO-LiTFSI electrolyte with BMITFSI shows an increasing trend with the content of BMITFSI over the entire

1238

J.-W. Choi et al. / Solid State Ionics 178 (2007) 1235–1241

Fig. 3. Variation of ionic conductivity with temperature of PEO-LiTFSIBMITFSI electrolytes.

temperature range studied here. Thus, PEO-LiTFSI-BMITFSI(80) shows the highest ionic conductivities of 3.2 × 10− 4 S/cm at 25 °C and 3.2 × 10− 3 S/cm at 80 °C. The enhancement in ionic conductivity with RTIL addition is very much pronounced at lower temperatures: thus, addition of even 20 pbw of BMITFSI results in an increase by one order (i.e. ten times) at 25 °C, compared to an increase by two times at 80 °C. The trend in variation of ionic conductivity with temperature progressively changes from a well-defined, two-region behavior for PEOLiTFSI to an almost linear behavior for PEO-LiTFSI-BMITFSI (80). The change in slope of the curve at ∼60 °C is typical of PEObased electrolytes and has been attributed to the change in conduction mechanism of the electrolyte associated with the PEO crystalline-amorphous phase transition. The PEs containing 20– 60 pbw of BMITFSI also show a similar trend but with reduced slopes, indicating that the Li+ ions interact with the PEO chains in these cases as well, although less strongly. A similar observation of enhanced ionic conductivity of PEO-LiTFSI electrolyte with the addition of pyrrolidiniumbased RTIL has been reported and the effect was attributed to the formation of salt-containing amorphous phase of PEO at low temperatures with RTIL leading to an overall reduction of crystallinity of the system [9]. The Li+ ions that are coordinated with the “O” atoms of PEO segments could be freed partially or fully from that trap by coordinating with the anion of RTIL and hence could lead to larger number of charge carriers with improved charge migration. Thus, incorporation of RTIL is an effective way of enhancing the ionic conductivity of PEO-based PEs to an appreciable level which has hitherto been not possible by other modifications [9]. The CV data of the electrochemical cells can be useful for investigating the behavior of the electrodes in the electrolytes. The first cycle CV data obtained for lithium cells with PEOLiTFSI-BMITFSI electrolytes with varying BMITFSI content are compared in Fig. 4. The electrolytes containing BMITFSI exhibit well-defined processes corresponding to anodic oxidation at peak voltages (Ep) in the range 0.24 to 0.33 V, and cathodic reduction at Ep in the range − 0.53 to − 0.56 V. The peak currents (Ip) for the processes show a slight increasing

trend with the BMITFSI content; thus, Ip for oxidation process increases from 0.09 mA to 0.16 mA with an increase of RTIL content from 20 to 80 pbw; for reduction process the respective Ip values are − 0.16 mA and − 0.24 mA. The redox process is thus seen to occur efficiently in the PEs containing RTIL with an average peak separation of ∼0.8 V. The oxidation and reduction processes are less defined in PEO-LiTFSI compared to that of the PE with BMITFSI; they occur at 0.66 V and − 1.0 V respectively, with a peak separation of 1.66 V, double that for the electrolyte with RTIL. The redox current is also feeble in PEO-LiTFSI, ∼ 0.05 mA. The first cycle CV comparison indicates that BMITFSI incorporation in PEOLiTFSI substantially improves its redox behavior with lithium electrodes. BMITFSI is reported to have an electrochemical stability window of 4.6 V, with a cathodic limit of − 2 V and an anodic limit of 2.6 V vs. Ag|/Ag+ [25], which correspond to 1.2 V and 5.8 V respectively vs. Li/Li+. Some EMI-based RTILs have been reported to be unstable below 1 V and hence not suitable for applications in lithium batteries [7]. However, we observe from the present experiments that PEO-LiTFSI-BMITFSI system is able to provide good resolution for the lithium reduction process that occurs at ∼ − 0.5 V. Moreover, the electrolyte has a low reduction current of b0.25 mA at − 1.0 V (vs. Li/Li+). This suggests that the bulk reduction of BMITFSI has not progressed much even at − 1.0 V and thus the electrolyte might be assumed to have a cathodic stability up to − 1.0 V at least. The presence of LiTFSI salt in the electrolyte might help to suppress the reduction of imidazolium cation, similar to that observed for pyrrolidinium cation in an earlier study [9]. The enhancement of cathodic stability of RTIL below the plating potential of lithium by incorporating in PEO-LiX electrolytes is attributed to the formation of a stable passivation layer on the lithium electrode which conducts Li + ion effectively but prevents further reaction with RTIL [1]. Nevertheless, it should be noted that the cathodic current at − 1.0 V increases with BMITFSI content in the electrolyte and hence, the presence of an excess RTIL in the system is not advisable for good cathodic stability. Further studies have been performed with PEO-

Fig. 4. First cycle CV comparison of PEO-LiTFSI and PEO-LiTFSI-BMITFSI electrolytes (Li/PE/Li cells, scan rate 1 mV/s, voltage range −1 V to +1 V).

J.-W. Choi et al. / Solid State Ionics 178 (2007) 1235–1241

1239

LiTFSI-BMITFSI(60) that exhibits good mechanical integrity, high ionic conductivity and electrochemical stability. CV data on cycling of PEO-LiTFSI-BMITFSI(60) is presented in Fig. 5. A slight shift of anodic Ep to higher voltages is observed during the initial cycles, but soon the process gets stabilized. The cathodic process occurs at the same voltage on repeated cycling. After about 4 cycles, the cell shows overlapping CV curves, indicating the occurrence of highly reversible redox processes. The anodic and cathodic Ip values are also nearly the same, which is an indication of the high coulombic efficiency for the redox process. The formation of a compatible, Li+ ion conducting interface on lithium metal is essential for achieving good performance from a lithium cell on repeated cycling. Fig. 6 shows the change in impedance of PEO-LiTFSI electrolyte with storage time, evaluated up to 3 days. The impedance spectrum at each time interval consists of two semi-circles. The smaller semicircle at high frequencies results from the contribution of the resistance of the bulk electrolyte (Re) and the larger semicircle at lower frequencies results from the contribution of electrode/electrolyte interface resistance (Rf). The larger semicircles grow in size during the initial period and then show a decreasing trend. Thus, from an initial value of 10,230 Ω, Rf reaches a maximum of 24,320 Ω after 20 h and then reduces to 18,390 Ω after 72 h. The initial increase in Rf is inevitable in lithium batteries due to the formation and growth of the passivation layer on the lithium surface. A reduction in Rf after an initial period of about a day indicates the stabilization of the electrode/electrolyte interface. Re varies from 1970 Ω to 2310 Ω during this time of storage (the small semicircles are shown magnified in the inset of the figure). The variation of Re with storage time is less significant compared to that of Rf for PEO-LiTFSI electrolyte. The impedance behavior of PEO-LiTFSI-BMITFSI(60) under identical conditions is shown in Fig. 7. Unlike PEO-LiTFSI, the spectrum of PEO-LiTFSI-BMITFSI contains only one semicircle over the whole frequency range. Such a pattern is generally shown by liquid/gel electrolytes that have high ionic conductivity (i.e. low Re). The real axis intercept at the high frequency end corresponds to Re of the system. Re remains nearly constant in the range 75–

83 Ω, over the time of study. The presence of BMITFSI in the PE thus helps to reduce Re very significantly (compare 75 Ω for PEOLiTFSI-BMITFSI(60) with 1970 Ω for PEO-LiTFSI). This is an expected behavior since the electrolyte with BMITFSI has a higher ionic conductivity at room temperature, almost 2 orders of magnitude higher than that of PEO-LiTFSI. The variation in Rf of PEO-LiTFSI-BMITFSI(60) with storage time follows a similar trend to that of PEO-LiTFSI; thus, Rf increases from an initial 3547 Ω to a maximum of 5690 Ω after 4 h and then continues to decrease reaching 3615 Ω after 72 h. It can be noticed that the incorporation of BMITFSI in PEO-LiTFSI electrolyte leads to a lithium electrode interface having a significantly lower initial Rf as well as a faster stabilization of the interface (4 h vs. 20 h). Thus, after 3 days, Rf is only ∼2% higher than the initial value for PEOLiTFSI-BMITFSI(60), whereas, for PEO-LiTFSI, Rf after 3 days is higher than its initial value by ∼80%. Lower Rf and its fast stabilization attained for the electrolyte containing RTIL indicates its better compatibility with lithium electrode and the formation of a stable, Li+ ion conducting film on the electrode surface. This passivation layer prevents further reaction of RTIL with lithium

Fig. 5. CVof PEO-LiTFSI-BMITFSI(60) during cycling (Li/PE/Li cell, scan rate 1 mV/s, voltage range −1 V to +1 V).

Fig. 7. Variation of impedance behavior of PEO-LiTFSI-BMITFSI(60) with storage time (Li/PE/Li cell, frequency range: 2 MHz–10 mHz).

Fig. 6. Variation of impedance behavior of PEO-LiTFSI with storage time (Li/ PE/Li cell, frequency range: 2 MHz–10 mHz). Inset shows magnification of the smaller semicircles.

1240

J.-W. Choi et al. / Solid State Ionics 178 (2007) 1235–1241

and thus helps to enhance the cathodic limit of the electrolyte and improve cycling properties as observed in CV studies. PEO-LiTFSI and PEO-LiTFSI-BMITFSI(60) electrolytes have been evaluated for performance in Li/ LiFePO4 cells. LiFePO4 has gained considerable attraction as a safe and non-toxic, 3.4 V cathode material for lithium batteries that can provide a high theoretical capacity of 170 mAh/g and excellent cycling properties [23,26,27]. A comparison of the discharge capacities of Li/ LiFePO4 cells at 25 °C and 0.05 C-rate using PEO-LiTFSI and PEO-LiTFSI-BMITFSI(60) is presented in Fig. 8. An increase in discharge capacity with cycle number is shown by both electrolytes, indicating the optimization/stabilization needed for achieving a compatible interface with the electrode. The electrolyte containing RTIL shows a better performance, nearly twice that of PEO-LiTFSI. Nevertheless, the discharge capacity realized at 25 °C is poor: i.e. a maximum of 32% of theoretical capacity only is delivered after 5 cycles. Although BMITFSI incorporation has resulted in a substantial increase in ionic conductivity of the electrolyte to 1.7 × 10− 4 S/cm at 25 °C, the performance is still not in a satisfactory level at room temperature. Nevertheless, at the moderate temperature of 40 °C, PEO-LiTFSI-BMITFSI performs better, as shown in Fig. 9. An initial discharge capacity of 90 mAh/ g is obtained which enhances to 140 mAh/g (corresponding to 82% utilization of active material) in 5 cycles. Thereafter, the discharge capacity remains stable with cycling, as shown in the inset of the figure. The enhanced performance at 40 °C compared to that at 25 °C is attributed mainly to the higher ionic conductivity of the electrolyte at 40 °C (5.7× 10− 4 S/cm). Increase of cell operation temperature also causes a reduction in the viscosity of the RTIL and facilitates easy wetting of the electrode surface by the electrolyte and better penetration of ions into the interior of the cathode resulting in enhanced performance of the cell. A similar, satisfactory performance of a PE incorporating pyrrolidiniumbased RTIL has been earlier reported for Li/V2O5 cells [9] and Li/ LiFePO4 cells [10] at moderate temperatures of 40–60 °C. The present study is the first one, to the best of our knowledge, which reports the suitability of PE containing BMI-based RTIL for application in LMPB. Properties such as high ionic conductivity,

Fig. 9. Discharge capacities during first and fifth cycles of Li/LiFePO4 cell at 40 °C using PEO-LiTFSI-BMITFSI(60) as electrolyte (voltage: 2.0–4.2 V). Cycle performance of the cell is shown in inset.

low interfacial resistance with lithium electrode and good electrochemical stability of PEO-LiTFSI-BMITFSI electrolyte make it a good candidate for use in LMPBs operating at moderately high temperatures. 4. Conclusions PEO-LiTFSI solid electrolyte has been modified by the incorporation of 20–80 pbw of the RTIL, BMITFSI. A decrease in Tm of the crystalline segments of PEO and the formation of an amorphous phase in the electrolyte has been observed by inclusion of BMITFSI in the system. BMITFSI addition results in a very significant increase in ionic conductivity of the electrolyte, the effect being more pronounced at lower temperatures. Ionic conductivity increases with the increase in RTIL content and reaches 3.2 × 10− 4 S/cm at 25°C with PEO-LiTFSI-BMITFSI(80). CV studies demonstrate the suitability of the PEs containing BMITFSI for lithium battery application with well-defined redox processes corresponding to lithium stripping and deposition. The presence of BMITFSI in the electrolyte significantly reduces Re and Rf and also helps to achieve a faster lithium electrode stabilization. The optimum electrolyte, PEO-LiTFSI-BMITFSI (60) with good mechanical integrity performs well in Li/LiFePO4 cells at the moderately high temperature of 40 °C, exhibiting an active material utilization of 82% and stable cycling properties. Acknowledgements

Fig. 8. Discharge capacities during first and fifth cycles of Li/LiFePO4 cells at 25 °C using PEO-LiTFSI and PEO-LiTFSI-BMITFSI(60) as electrolytes (voltage: 2.0–4.2 V).

This research was supported by funds from the Ministry of Information and Communication in Korea (the Information Technology Research Center (ITRC) support program supervised by the Institute of Information Technology Assessment (IITA)), the Division of Advanced Batteries in NGE Program (Project No. 10016439), and the Korea Research Foundation (KRF-2005-005J11901). G. Cheruvally is thankful to the KOFST for the award of Brain Pool Fellowship, and J. W. Choi, Y. H. Kim, J. K. Kim, J. Manuel, and P. Raghavan acknowledge a partial support by the Post Brain Korea 21 Project from Ministry of Education.

J.-W. Choi et al. / Solid State Ionics 178 (2007) 1235–1241

References [1] P.C. Howlett, D.R. MacFarlane, A.F. Hollenkamp, Electrochem. SolidState Lett. 7 (2004) A97. [2] G.B. Appetecchi, F. Croce, J. Hassoun, B. Scrosati, M. Salomon, F. Cassel, J. Power Sources 114 (2003) 105. [3] J.H. Shin, Y.T. Lim, K.W. Kim, H.J. Ahn, J.H. Ahn, J. Power Sources 107 (2002) 103. [4] L.R.A.K. Bandara, M.A.K.L. Dissanayake, B.-E. Mellander, Electrochim. Acta 43 (1998) 1447. [5] M. Galinski, A. Lewandowski, I. Stepniak, Electrochim. Acta 51 (2006) 5567. [6] B. Garcia, S. Lavallee, G. Perron, C. Michot, M. Armand, Electrochim. Acta 49 (2004) 4583. [7] H. Nakagawa, S. Izuchi, K. Kuwana, T. Nukuda, Y. Aihara, J. Electrochem. Soc. 150 (2003) A695. [8] Y.S. Fung, R.Q. Zhou, J. Power Sources 81-82 (1999) 891. [9] J.H. Shin, W.A. Henderson, S. Passerini, J. Electrochem. Soc. 152 (2005) A978. [10] J.H. Shin, W.A. Henderson, S. Scaccia, P.P. Prosini, S. Passerini, J. Power Sources 156 (2006) 560. [11] J.H. Shin, W.A. Henderson, S. Passerini, Electrochem. Solid-State Lett. 8 (2005) A125. [12] J.H. Shin, W.A. Henderson, G.B. Appetecchi, F. Alessandrini, S. Passerini, Electrochim. Acta 50 (2005) 3859.

1241

[13] J.H. Shin, W.A. Henderson, S. Passerini, Electrochem. Commun. 5 (2003) 1016. [14] L.X. Yuan, J.K. Feng, X.P. Ai, Y.L. Cao, S.L. Chen, H.X. Yang, Electrochem. Commun. 8 (2006) 610. [15] H. Sakaebe, H. Matsumoto, Electrochem. Commun. 5 (2003) 594. [16] K.S. Kim, S.Y. Park, S. Choi, H. Lee, J. Power Sources 155 (2006) 385. [17] T. Sato, T. Maruo, S. Marukane, K. Takagi, J. Power Sources 138 (2004) 253. [18] R. Marcilla, F. Alcaide, H. Sardon, J.A. Pomposo, C. Pozo-Gonzalo, D. Mecerreyes, Electrochem. Commun. 8 (2006) 482. [19] J. Fuller, A.C. Breda, R.T. Carlin, J. Electroanal. Chem. 459 (1998) 29. [20] A. Balducci, U. Bardi, S. Caporali, M. Mastragostino, F. Soavi, Electrochem. Commun. 6 (2004) 566. [21] Y.H. Kim, G. Cheruvally, J.W. Choi, J.H. Ahn, K.W. Kim, H.J. Ahn, D.S. Choi, C.E. Song, Macromol. Symp. 249-250 (2007) 183. [22] V. Farmer, T. Welton, Green Chem. 4 (2002) 97. [23] J.K. Kim, J.W. Choi, G. Cheruvally, J.U. Kim, J.H. Ahn, G.B. Cho, K.W. Kim, H.J. Ahn, J. Power Sources 166 (2007) 211. [24] J. Xi, X. Qiu, X. Ma, M. Cui, J. Yang, X. Tang, W. Zhu, L. Chen, Solid State Ionics 176 (2005) 1249. [25] A. Lewandowski, I. Stepniak, Phys. Chem. Chem. Phys. 5 (2003) 4215. [26] A.K. Padhi, K.S. Nanjundaswamy, J.B. Goodenough, J. Electrochem. Soc. 144 (1997) 1188. [27] K. Striebel, J. Shim, A. Sierra, H. Yang, X. Song, R. Kostecki, K. McCarthy, J. Power Sources 146 (2005) 33.

Poly(ethylene oxide)-based polymer electrolyte ...

Fax: +82 55 753 1806. .... PEs containing 0 to 60 pbw of BMITFSI are free-standing, ..... [1] P.C. Howlett, D.R. MacFarlane, A.F. Hollenkamp, Electrochem. Solid-.

451KB Sizes 3 Downloads 96 Views

Recommend Documents

B53-35H-011 Polyethylene Copolymer
B53-35H-011 is a high density polyethylene copolymer developed for blow molding applications. This product is recommended for use in applications which require a combination of high top load strength and good environmental stress crack resistance (ES

Ceramic electrolyte coating methods
Jul 2, 2001 - A cloud of ions and counter-ions surround the particle, creating the repulsive ?eld. Particle particle interactions can be manipulated by pH ...

EU - Countervailing Measures on Polyethylene ... - WorldTradeLaw.net
Nov 7, 2014 - EUROPEAN UNION – COUNTERVAILING MEASURES ON CERTAIN ... published as Council Implementing Regulation (EU) 857/2010 of 27 ...

EU - Countervailing Measures on Polyethylene ... - WorldTradeLaw.net
Nov 7, 2014 - EUROPEAN UNION – COUNTERVAILING MEASURES ON .... under EU law, including proceedings before the European Court of Justice.

Electrolyte-Imbalances-Study-Guide.pdf
LOOKING FOR EVEN MORE? LEARN THE. PICMONICS. TAKE A. QUIZ. VIEW A RECORDED WEBINAR. Images © Picmonic Inc 2016. Version 1.2 Page 1.

Electrolyte-Gated Organic Thin-Film Transistors - DiVA
Contribution: All experimental work except for the fabrication of the source ..... determine the shape and energy of the orbital: the principal quantum number n ...... electrode becomes less critical, which opens up for alternative transistor designs

Interaction energies in polymer/polymer mixtures
All rights reserved ... between the AP* values obtained from phase diagrams and from retention .... is the selection of the solvents with appropriate retention.

Electrolyte-Imbalances-Study-Guide.pdf
Page 1 of 8. Electrolyte Imbalances. Hi New Friend! In this guide you'll find brevity in only some of the highest yield “mustknow” content for. your exams for ...

pdf-1495\polymers-polymer-blends-polymer-composites-and-filled ...
... FROM OUR ONLINE LIBRARY. Page 3 of 8. pdf-1495\polymers-polymer-blends-polymer-composites- ... rties-and-applications-from-nova-science-pub-inc.pdf.

Polymer-Nanomaterials.pdf
Page 1 of 12. 1. Polymer Nanomaterials. W. Marshall Ming. Department of Chemistry, Georgia Southern University. Statesboro, GA 30460, USA.

Polymer Blends
where Bi 1- are the interaction energy densities of each polymer pair ... reproduced them using positive values of BI-EFF. This ..... SQL, 32, 3853 (1986). X. Yang.

Electrolyte-Gated Organic Thin-Film Transistors - DiVA
A Static Model for Electrolyte-Gated Organic Field-Effect Transistors. Deyu Tu, Lars ...... [50] In this circuit, CE and RE represent the dielectric capacitance and the.

Acidity of Frozen Electrolyte Solutions
Ice is selectively intolerant to impurities. A preponderance of implanted anions or cations generates electrical imbalances in ice grown from electrolyte solutions. Since the excess charges are ultimately neutralized via interfacial (H+/HO-) transpor

Polymer and Fiber.pdf
Whoops! There was a problem loading more pages. Whoops! There was a problem previewing this document. Retrying... Download. Connect more apps.

Polymer Origami Logo.pdf
Page 1 of 1. Polymer Origami Logo.pdf. Polymer Origami Logo.pdf. Open. Extract. Open with. Sign In. Main menu. Displaying Polymer Origami Logo.pdf.

Polymer and Fiber.pdf
Major POLYMER and FIBER RETP Pre-Engr**. F A L L S P R I N G. 1. st Year Prerequisites Subs Ar Cr Sem Gr 1. st Year Prerequisites Subs Ar Cr Sem Gr. MATH 1441 Calculus I MATH 1113 A 4 MATH 2242 Calculus II. MATH 1441. with C D 4. CHEM 1145 Principles