Guanzhou Zhua,
Michael Angella,
Chun-Jern Panab,
Meng-Chang Linc,
Hui Chenc,
Chen-Jui Huangb,
Jinuan Lina,
Andreas J. Achazidf,
Payam Kaghazchie,
Bing-Joe Hwangb and
Hongjie Dai*a
aDepartment of Chemistry, Stanford University, Stanford, California 94305, USA. E-mail: hdai1@stanford.edu
bDepartment of Chemical Engineering, National Taiwan University of Science and Technology, Taipei 10607, Taiwan
cCollege of Electrical Engineering and Automation, Shandong University of Science and Technology, Qingdao 266590, People's Republic of China
dPhysikalische und Theoretische Chemie, Freie Universität Berlin, Takustr. 3, D-14195 Berlin, Germany
eForschungszentrum Jülich GmbH, Institute of Energy and Climate Research (IEK-1), Materials Synthesis and Processing, Wilhelm-Johnen-Straße, 52425 Jülich, Germany
fDepartment of Chemistry, University of South Dakota, 414 E. Clark St., Vermillion, SD 57069, USA
First published on 11th April 2019
Room temperature ionic liquids (RTILs) are solvent-free liquids comprised of densely packed cations and anions. The low vapor pressure and low flammability make ILs interesting for electrolytes in batteries. In this work, a new class of ionic liquids were formed for rechargeable aluminum/graphite battery electrolytes by mixing 1-methyl-1-propylpyrrolidinium chloride (Py13Cl) with various ratios of aluminum chloride (AlCl3) (AlCl3/Py13Cl molar ratio = 1.4 to 1.7). Fundamental properties of the ionic liquids, including density, viscosity, conductivity, anion concentrations and electrolyte ion percent were investigated and compared with the previously investigated 1-ethyl-3-methylimidazolium chloride (EMIC-AlCl3) ionic liquids. The results showed that the Py13Cl–AlCl3 ionic liquid exhibited lower density, higher viscosity and lower conductivity than its EMIC-AlCl3 counterpart. We devised a Raman scattering spectroscopy method probing ILs over a Si substrate, and by using the Si Raman scattering peak for normalization, we quantified speciation including AlCl4−, Al2Cl7−, and larger AlCl3 related species with the general formula (AlCl3)n in different IL electrolytes. We found that larger (AlCl3)n species existed only in the Py13Cl–AlCl3 system. We propose that the larger cationic size of Py13+ (142 Å3) versus EMI+ (118 Å3) dictated the differences in the chemical and physical properties of the two ionic liquids. Both ionic liquids were used as electrolytes for aluminum–graphite batteries, with the performances of batteries compared. The chloroaluminate anion-graphite charging capacity and cycling stability of the two batteries were similar. The Py13Cl–AlCl3 based battery showed a slightly larger overpotential than EMIC-AlCl3, leading to lower energy efficiency resulting from higher viscosity and lower conductivity. The results here provide fundamental insights into ionic liquid electrolyte design for optimal battery performance.
The electrolyte lies at the heart of a battery. With the advances in battery technology, the development of a safe and stable electrolyte is critically important. Room temperature ionic liquids (RTILs) are safe and sufficiently conducting, useful as battery electrolytes.10–14 Various ionic liquids have been investigated for different types of batteries, including LIB and AIB.2,15,16 Our group has developed rechargeable Al–graphite battery based on two types of electrolytes, an IL electrolyte made by mixing 1-ethyl-3-methylimidazolium chloride (EMIC) and AlCl3 and an quasi IL or deep-eutectic solvent (DES) by mixing urea with AlCl3.7–9 The batteries operate by reversible redox of Al at the negative Al foil electrode, and reversible carbon redox through chloroaluminate anion intercalation and de-intercalation at the graphite positive electrode.7–9,17–19 Still, much room exists in developing new IL electrolytes to improve Al battery, and especially, to understanding the relations between the composition, physical properties of IL electrolytes and battery performance.
Herein, we report a new series of ionic liquids formed by mixing 1-methyl-1-propylpyrrolidinium chloride and AlCl3 at various ratios (AlCl3/Py13Cl ratios: 1.4, 1.5, 1.6, 1.7). The electrolytes exhibited different physical and chemical properties compared to the widely used EMIC-AlCl3 ionic liquids. We devised an approach to probe and quantify the species in both ionic liquids containing monomeric AlCl4− anion and dimeric Al2Cl7− anion. We found that larger AlCl3 related species in the form of (AlCl3)n existed only in Py13Cl–AlCl3 ionic liquid and were absent in EMIC-AlCl3. In addition, the overall concentration of AlCl4− and Al2Cl7− and ion percent were lower in the Py13Cl–AlCl3 system. The difference in cation size (Py13+: 142 Å3 versus EMI+: 118 Å3) was likely responsible for the differences in the physical properties of Py13Cl–AlCl3 and EMIC-AlCl3 ILs. Batteries using Py13Cl–AlCl3 electrolyte showed lower energy and voltage efficiency as a result of their larger overpotential resulted from higher viscosity and lower ionic conductivity with the presence of large (AlCl3)n species in the ionic liquid. Our results help to shed light into electrolyte design for Al batteries.
We first measured the density of ionic liquids formed by mixing AlCl3 with Py13Cl and EMIC respectively at various molar ratios (Fig. 1b). The EMIC-AlCl3 ionic liquid density increased linearly with the AlCl3/EMIC ratio in the 1–1.7 range, in close agreement with literature reported results.20 A comparison between our experimental results and those calculated from literature was shown in Fig. S2† (temperature used for density calculation was 25 °C).20 A significant difference between the two ionic liquids was that well behaved liquids for the Py13Cl–AlCl3 system could not form for AlCl3/Py13Cl < 1.4, unlike the homogeneous clear liquids formed for AlCl3/EMIC ≥ 1. For the Py13Cl–AlCl3 system, a gel like mixture was formed with visible precipitates when AlCl3/Py13Cl = 1–1.3. Also different was that for AlCl3/Py13Cl > 1.3, the change in density of Py13Cl–AlCl3 ionic liquid did not follow a linear trend with the increase in AlCl3/Py13Cl molar ratio. Density decreased first from AlCl3/Py13Cl = 1.4 to 1.5 and then increased as AlCl3/Py13Cl further increased (Fig. 1b black curve).
We also measured viscosity of the two ionic liquid systems at temperature of 23 to 24 °C. The viscosity of Py13Cl–AlCl3 ionic liquid was about 3 times higher than that of EMIC-AlCl3 ionic liquid (Fig. 1c), with its viscosity decreased as the AlCl3/Py13Cl ratio changed from 1.4 to 1.6 and then slightly increased as the AlCl3 ratio further increased to 1.7. Conductivity measurements of these ionic liquids found that, corroborated with the higher viscosity of Py13Cl–AlCl3 ionic liquid, its ionic conductivity, measured at 25 °C, was about 3 times lower than that of EMIC-AlCl3 (Fig. 1d).
AlCl3 + EMIC → EMI+ + AlCl4− (AlCl3 ratio ≤ 1) | (1a) |
AlCl3 + Py13Cl → Py13+ + AlCl4− (AlCl3 ratio ≤ 1) | (1b) |
AlCl3 + AlCl4− → Al2Cl7− (1 < AlC3 ratio < 2) | (1c) |
Three peaks unique to the Py13Cl–AlCl3 ionic liquids were observed at ∼270 cm−1, 377 cm−1 and 495 cm−1 (Fig. 3). These peaks were assigned to be neutral-like AlCl3 species in the form of aggregates, dimers, multimers and (AlCl3)n species. Peaks near 280 cm−1 were assigned to neutral aluminum chloride in the literature depending on the experimental conditions and chemical environment.26–28 The peak at 377 cm−1 was assigned to Al3Cl10− by Dymek et al. in their spectral study of Al3Cl10−, and the shoulder peak at 495 cm−1 was also observed by Rytter et al. in their Raman spectroscopic investigation of the melts of AlCl3 and AlkCl (Alk = Li, K, Cs).26,29 Peak at ∼495 cm−1 was present when AlCl3 concentration exceeded 66.7 mol% and the authors assigned it to higher polymeric AlxCl3x+1− ions, with the possibility of x > 3.26 The peak position was also likely to shift depending on the cation size.26 These peaks were also observed in the inhomogeneous 1.3 Py13Cl–AlCl3 mixture.
(2) |
In eqn 2, I was the intensity of the AlCl4− peak at 350 cm−1, and x was the molar ratio of AlCl3/EMIC ranging from 1.1 to 1.7. The dimeric anion concentration was calculated by
(3) |
For the Py13Cl–AlCl3 ILs, quantitative analysis of the speciation was not as straightforward due to the inability in forming a AlCl3/Py13Cl = 1.0 ratio electrolyte. We analyzed the concentrations of AlCl4− and Al2Cl7− from their Raman peak intensities after normalizing the Raman spectra of the Py13Cl–AlCl3 and EMIC-AlCl3 electrolytes to the same Si reference placed into the two ionic liquids. By so doing we estimated the anions concentrations in the Py13Cl electrolytes through the normalized Raman intensities using
(4) |
(5) |
In eqn (4) and (5), I was the normalized intensity for AlCl4− and Al2Cl7− and y was the ratio of AlCl3 ranging from 1.4 to 1.7.
The ratios between [Al2Cl7−] to [AlCl4−] were similar in both Py13Cl–AlCl3 and EMIC-AlCl3 ionic liquids, especially at AlCl3/organic chloride = 1.4–1.6 (Fig. 4a). In both systems, the monomeric anion concentration decreased with increasing AlCl3 ratio, and was lower in the Py13Cl–AlCl3 system than that in EMIC-AlCl3 at AlCl3 ratio equals to 1.4–1.6. When AlCl3/organic chloride = 1.7, the monomer anion concentration in both ionic liquids was similar (Fig. 4b). As expected, the Al2Cl7− concentration increased as the AlCl3 ratio increased (Fig. 4c), and was always lower in the Py13Cl–AlCl3 IL than in the EMIC-AlCl3 IL (Fig. 4c). This made the overall concentrations of AlCl4− and Al2Cl7− lower in the Py13Cl–AlCl3 IL than that in the EMIC-AlCl3 IL at a given AlCl3 to organic chloride ratio (Fig. 4b and c).
We defined a term “ion percent” as the ratio between [AlCl4−] + 2 × [Al2Cl7−] and [AlCl3]. By so doing we only included [AlCl4−] and [Al2Cl7−] since they were the only electrochemically active species in our ILs for Al battery operation. If the ion percent was 1, it indicated that all AlCl3 were consumed for making monomers and dimers. When the ion percent was less than 1, larger (AlCl3)n could form. For EMIC-AlCl3 IL, the ion percent values were near 1.0 (Fig. 4d), suggesting anions in the electrolytes were mostly in the form of AlCl4− and Al2Cl7−. In the Py13Cl–AlCl3 system, however, this ion percent value was always lower. When the AlCl3 ratio to Py13Cl was 1.4 (the lowest required to form a liquid), the ion percent was at its lowest, 0.85, and increased slightly as more AlCl3 was added and was always lower than 1. This trend in ion percent was consistent with the observations of the three unique peaks (270 cm−1, 377 cm−1, 495 cm−1) in the Py13Cl–AlCl3 Raman spectra. As the AlCl3 content increased, all these peaks had their intensities decreased, with the peaks at 270 cm−1 and 377 cm−1 being the most obvious. This trend suggested reduced concentrations of (AlCl3)n species as AlCl3/Py13Cl increased, which was also reflected by the slight increase in ion percent for the Py13Cl–AlCl3 IL. In the EMIC-AlCl3 spectra, however, these three peaks were absent, which was consistent with its ion percent value always close to 1. The error bars in Fig. 4 were obtained using formulas from error propagation (eqn S1†).
Cyclic voltammetry of the graphite electrodes (Fig. 5b) and aluminum electrode (Fig. 5c) in Al batteries were performed in 1.5 AlCl3:1.0 EMIC and 1.5 AlCl3:1.0 Py13Cl electrolytes respectively (scan rate = 0.58 mV s−1 with an Al metal reference electrode). The overall shapes of these two curves were somewhat similar, but obvious difference was observed. The 1.5 AlCl3/Py13Cl electrolyte showed a slightly higher voltage window. The irreversible reaction did not appear until a potential of 2.6 V, whereas in the 1.5 AlCl3/EMIC electrolyte the irreversible reaction appeared at 2.4 V. The overpotential (voltage difference in redox peaks) in the Py13Cl based electrolyte was higher than that in the EMIC based electrolyte, attributed to higher parasitic resistance due to the higher viscosity and lower conductivity of the Py13Cl system. The graphite side CVs had current normalized because the graphite electrodes loading for the two CVs were too low to keep the mass exact (Experimental methods section). Aluminum redox was clearly observed in both systems (Fig. 5c). It was observed that at the same voltage, the 1.5 EMIC battery showed higher current density than those in 1.5 Py13Cl battery, suggesting more facile Al redox reaction in the EMIC based electrolyte. The aluminum side CVs didn't need normalization as the size of the aluminum electrodes in the two CVs were kept the same (Experimental methods section).
The aluminum–graphite battery using 1.5 AlCl3:1.0 Py13Cl as electrolyte showed activation behavior during initial cycling (Fig. 5d), after which clear discharge voltage plateaus at around ∼2.2 V and ∼1.8 V appeared (Fig. 5e black curve). The battery was then cycled at various current densities (100 mA g−1 to 800 mA g−1) to investigate the rate performance, with high coulombic efficiency in the range of 99% to 100%. The battery at 100 mA g−1 current under a cutoff voltage of 2.4 V showed a capacity around 75 mA h g−1 with a coulombic efficiency about 99.2%. The discharging energy could be maintained at around 141 mW h g−1 (based on the graphite mass) with an energy efficiency about ∼89%. The aluminum–graphite battery using 1.5 AlCl3:1.0 EMIC as electrolyte could operate from 1 V to 2.4 V and no activation was needed in the beginning. Both batteries had similar stability over 100 cycles of charge–discharge (Fig. 5d). Comparison of the charge–discharge curves between 1.5 Py13Cl and 1.5 EMIC batteries at a current density of 100 mA g−1 (Fig. 5e) showed a larger overpotential in the 1.5 Py13Cl based battery, consistent with the cyclic voltammetry data (Fig. 5b).
We used Raman spectroscopy as a tool to probe and quantify chloroaluminate anionic species in different ionic liquids. In the EMIC-AlCl3 ILs, the peak at around 598 cm−1 assigned to be EMI+ was present in every spectrum. Therefore, besides the Si chip peak at around 520 cm−1, the EMI+ peak was also useful as an internal normalization factor to calculate AlCl4− and Al2Cl7− concentrations in EMIC-AlCl3 ILs for AlCl3/EMIC = 1.0–1.7. To this end, we first determined the concentration of EMI+ in every ratio of AlCl3 by the following equation.
(6) |
In eqn (6), x was the AlCl3 to EMIC ratio ranging from 1.0 to 1.7, and Vn was the molar volume of the IL, which could be determined from the average molecular weight dividing by the measured density. The EMI+ concentrations in different AlCl3 ratio ILs were different due to their difference in molar volume, originated from their difference in densities (Fig. 1b).
Next, the AlCl4− and Al2Cl7− intensity, normalized to EMI+, were calculated using the following equations.
(7) |
(8) |
In eqn (7) and (8), subscript x was the ratio of AlCl3 to EMIC ranging from 1.0 to 1.7. IAlCl4−,x and IAl2Cl7−,x were the EMI+ normalized intensity for AlCl4− and Al2Cl7− in xEMIC, respectively. IAlCl4−,raw,x, IAl2Cl7−,raw,x, and IEMI+,raw,x were the raw Raman intensity of AlCl4−, Al2Cl7− and EMI+ in xEMIC. Lastly, [EMI+]xEMIC and [EMI+]1.0EMIC were the EMI+ concentration in xEMIC and 1.0 EMIC, calculated from eqn (6), respectively. The ratio of was a correction factor for the EMI+ normalized intensity, due to the fact that EMI+ concentration were different in different AlCl3 ratio ILs.
After obtaining the EMI+ normalized peak intensity for AlCl4− and Al2Cl7− from eqn (7) and (8), these two quantities were plugged into eqn (2) and (3) to determine the AlCl4− and Al2Cl7− concentrations, similar to the Si normalization case. Ion percent could also be easily calculated using these newly obtained AlCl4− and Al2Cl7− concentrations. These results obtained by EMI+ normalization were compared with the Si normalization results (Fig. S4†), showing a high degree of agreement. This confirmed that the validity of the normalization method using Si as an external Raman reference. We believe that this method could be broadly applicable to facilitate quantitative anion speciation comparisons of a wide range ILs that lack a common cation Raman signature.
The Py13Cl–AlCl3 ionic liquids exhibited different properties (higher viscosity, lower conductivity, lower overall monomeric and dimeric anion concentrations and formation of large (AlCl3)n species) from the EMIC-AlCl3 ionic liquid, originated from the larger cationic size of Py13+ than the EMI+ cation (DFT calculated size of the Py13+ and EMI+ ∼142 Å3 and 118 Å3, respectively, Fig. S1†).31 When the cation size changed in an ionic liquid, it could greatly affect the chemical environment around it and its solvation shell. Bigger size cations could stabilize and favored the formation of larger species such as (AlCl3)n. In addition, the pi-system and the Brønsted acidic set of hydrogen atoms, which were unique in the EMI+ and absent in the Py13+, helped with solubilizing and liquidizing of the ionic liquid. Larger (AlCl3)n species tend to form in the Py13Cl–AlCl3 system without forming a stable solvation shell.32 This trend was reported by several authors in the literature.26,29 Larger (AlCl3)n species were only observed in Py13Cl–AlCl3 ionic liquid, and their concentration decreased as we increased the AlCl3 concentration.
We also calculated the interaction energy and the Gibbs free energy change for de-solvation in these two ILs (Table S1†). Our results showed that the interactions between EMI+ and AlCl4− was always stronger than that between Py13+ and AlCl4−. Weaker interaction in the Py13Cl–AlCl3 electrolyte was mainly due to the larger size of Py13+, which decreased its effective positive charge and weakened its electrostatic interactions with AlCl4−. With a smaller interaction energy between Py13+ and AlCl4−, the equilibrium constant for eqn (1b), compared to eqn (1a), would be smaller. As a result, larger polymeric (AlCl3)n species were present in some of the lower ratios Py13Cl IL. Once enough AlCl3 was introduced to the system, the total number of ions in the IL increased and these polymeric species started to disappear, as suggested by the diminishing of the Raman peak at 270 cm−1 (Fig. 3). In addition, unlike the homogeneous AlCl3/EMIC = 1 ionic liquid, this weaker electrostatic interaction made the formation of stable solvation shell in Py13Cl IL more difficult, which led to the inability of forming an IL for AlCl3/Py13Cl = 1. This phenomenon also suggested mismatch of cation and anion sizes at the cation/anion ratio = 1 condition to keep charge-neutrality while forming stable solvation shells with the same coordination numbers with counter-ion as in the AlCl3-EMIC case. When larger dimeric ions increased in concentration above a threshold level for AlCl3/Py13Cl ≥ 1.4 electrolytes, the system evolves into a well solvated liquid.
The Py13Cl–AlCl3 contained large species and lower overall concentrations of dimeric and monomeric anions. This combined with the larger size cations in the electrolyte afforded ILs exhibiting greater viscosity and lower ionic conductivity than the EMIC counterparts. This led to a larger overpotential for battery charge and discharge, giving lower energy and voltage efficiency as observed. In addition, the lower conductivity of this electrolyte also limited the current at the negative electrode, at which aluminum redox happened (Fig. 5c). Even though the cations in our electrolytes did not directly participate in any actual electrochemical reaction, they could affect the performance of the battery by controlling the anionic species around it, which in turn affected the physical properties of the IL including viscosity and conductivity. From our results, smaller cations could have positive effects on the battery, by decreasing the viscosity and increasing the conductivity of the resulting electrolyte. This could provide a guide to the synthesis of new ionic liquids for optimized batteries in the future.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c9ra00765b |
This journal is © The Royal Society of Chemistry 2019 |