Svit
Menart
ab,
Klemen
Pirnat
*a,
David
Pahovnik
a and
Robert
Dominko
abc
aNational Institute of Chemistry, Ljubljana, Slovenia. E-mail: klemen.pirnat@ki.si
bFaculty of Chemistry and Chemical Technology, University of Ljubljana, Ljubljana, Slovenia
cALISTORE-European Research Institute, Amiens, France
First published on 4th May 2023
Aqueous zinc-ion batteries are one of the most promising candidates for large-scale energy storage applications. Herein, we report a rationally designed triquinoxalinediol (TQD) organic cathode material for aqueous zinc-ion batteries. Integration of hydroquinone units with hexaazatriphenylene (HAT) core enabled a high theoretical capacity of 669 mA h g−1 (based on a twelve-electron exchange reaction) and a practical reversible capacity of 503 mA h g−1 at 100 mA g−1. Both values are among the highest available in the literature. The charge storage mechanism was systematically studied using ex situ FT-IR and various electrochemical measurements revealing a co-insertion mechanism involving protons and zinc cations. The TQD suffers from significant capacity fading, which was attributed to the dissolution of active material in the electrolyte. That was supported by using in situ UV-vis spectroscopy. This work adds a promising material in a rapidly expanding mosaic of pyrazine/quinone organic cathode materials.
In recent years aqueous zinc-ion batteries have attracted a lot of attention as one of the most promising candidates for large-scale energy storage applications. The use of zinc metal offers advantages in terms of high specific capacity (820 mA h g−1), low toxicity, low cost, and high world resources, which are at least 20 times greater than Li. Its low redox potential (−0.76 V vs. SHE) and large overpotential for hydrogen evolution makes it one of the most suitable metal anodes for use with aqueous electrolytes typically showing much higher conductivities compared to nonaqueous electrolytes. Furthermore, aqueous zinc-ion battery components are stable in an ambient atmosphere, which simplifies production and decreases the cost per kW h of stored energy.1–3
The research of suitable zinc battery cathodes is predominantly focused on inorganic cathode materials such as manganese dioxides, Prussian blue analogs, and vanadium oxides. The mentioned cathode materials enable high capacities followed by fast capacity fading due to strong electrostatic interactions with a rigid lattice, large structural deformations, and material dissolution.4,5
Recently, several studies showed that organic cathode materials present a viable alternative to inorganic cathode materials. The flexibility of organic materials circumvents the slow solid-state diffusion limitations of inorganic cathode materials and enables efficient cycling even at higher rates. Organic cathode materials can accommodate different cations and have been proven to work in multivalent systems such as magnesium,6,7 aluminum,8,9 and zinc.10,11 Among many types of organic compounds tested in zinc batteries, such as stable organic radicals,12 conducting polymers,13 thiolates,14 triphenyl amines,15 dinitrobenzenes16 and phenothiazines,17 compounds based on carbonyls (CO)11 and imines (C
N)18 have attracted the most attention.
Hexaazatrinaphthalene (HATN), a small organic cathode material,19 and its derivatives have already been explored as cathode materials in aqueous zinc-ion batteries.20 Herein, we present a novel HATN-based small organic cathode material derived by a synergistic combination of hexaazatriphenylene (HAT) core21 and hydroquinone motif enabling an increased theoretical capacity of 669 mA h g−1. The material triquinoxalinediol (TQD) exhibited the highest reported initial reversible capacity of 503.4 mA h g−1 at a current density of 100 mA g−1 (Table S1†). The charge storage mechanism was systematically studied using ex situ FT-IR and various electrochemical measurements revealing a coordination of the reduced species with protons or divalent zinc cations. Similar to other small organic cathode materials it suffers from significant capacity fading, which was attributed to the dissolution of active material in the electrolyte.
TQD material was obtained through a multi-step synthesis (Fig. 2a and S1†) starting from a widely available 1,4-dimethoxybenzene precursor, which was first nitrated using nitric acid and afterward reduced to a diamine precursor using metallic tin. The synthesis of the HAT core was achieved through a condensation reaction between 3,6-dimethoxybenzene-1,2-diamine and hexaketocyclohexane octahydrate, a reaction analogous to the synthesis of HATNQ (Fig. S1†).20 In the last step of the synthesis, methyl ethers were deprotected using boron tribromide yielding the final hydroquinone TQD material. The structure of the TQD was confirmed with the use of various techniques. 1H NMR spectrum revealed two singlets with equal integral areas at 9.79 and 7.32 ppm, corresponding to –OH and aromatic protons, respectively. A small peak at 4.13 ppm is attributed to residual O–CH3 groups due to the incomplete deprotection of aromatic methyl ethers (Fig. 2b). The comparison between the integral area for –OH protons and –OCH3 revealed that only around 5% of the ethers remained protected. In the 13C NMR spectrum four distinguishable peaks at 146.4, 142.5, 133.6, and 113.6 match with four types of C atoms in TQD (Fig. 2c). Additionally, the synthesis of TQD is confirmed with MALDI-TOF mass spectrometry, which revealed two major sets of mass peaks corresponding to the [TQD + H]+ at 480.98 Da (calculated exact mass 481.09) and [TQD–CH3 + H]+ (TQD with one methyl-ether protecting group) at 494.99 Da (calculated exact mass 495.10 Da) (Fig. 2d). Smaller distributions belong to the same species ionized with Na+ instead of H+. The peaks corresponding to [M + 2H]+, [M + 3H]+, etc. species are observed due to the laser-induced photoreduction.26 Fourier transform infrared spectra (FT-IR) exhibited a broad peak between 3600 cm−1 and 3000 cm−1, which is attributed to O–H stretching and H2O vibrations. FT-IR spectrum exhibits a strong sharp peak at 1135 cm−1 attributed to C–O stretching vibration (Fig. 2e).
We obtained the electronic structures of TQD, oxidized TQD, and HATNQ with the use of the density functional theory (DFT) computational methods (Fig. 3). The pristine state of TQD represents a half-reduced state, which makes the comparison with HATNQ in its fully oxidized state irrelevant. To obtain a meaningful comparison, we calculated the electronic structure of hypothetical fully oxidized TQD. The comparison between the electronic structure of oxidized TQD and HATNQ shows a slightly lower energy gap (Eg) between HOMO and LUMO orbital (3.51 eV vs. 3.65 eV, respectively), suggesting that the intrinsic electronic conductivity of oxidized TQD is higher. The calculations showed that the LUMO energy of the oxidized TQD is lower (−3.88 eV) than that of HATNQ (3.48 eV) indicating greater electronic affinity corresponding to a higher reduction potential, which could also be explained by lower aromaticity of oxidized TQD in comparison with HATNQ. Similar observations have been shown in the literature, where LUMO differences between benzoquinone, naphthoquinone, and anthraquinone were correlated to aromaticity.27 The greater electronic affinity of oxidized TQD has been observed in galvanostatic measurements, where it delivered a higher initial discharge voltage than HATNQ (Fig. 4a).
The use of highly concentrated 4 M ZnSO4 electrolyte enabled slightly better cycling stability. In the comparison, the use of more diluted 1 M ZnSO4 caused faster capacity fading (Fig. 5a). A similar effect has already been observed in lithium organic batteries, where the use of concentrated electrolytes suppressed the dissolution of small organic cathode materials.28,29 The cycling stability of small organic cathode materials is influenced by the depth of discharge, which influences the amount of active material dissolution.22 To improve the cycling stability different cutoff voltages of 0.8 V, 0.6 V, 0.4 V, and 0.25 V were tested. After 150 cycles at 100 mA g−1 the capacity retention reached the values of 89.1%, 74.5%, 71.4%, and 36.2%, respectively (Fig. 5b and c). We have chosen a cutoff voltage of 0.4 V as the best compromise between capacity retention and specific capacity. The rate performance of TQD was performed in the cutoff voltage of 0.4 V, where the material reached capacities of 346 mA h g−1, 310 mA h g−1, 273 mA h g−1, 238 mA h g−1, 222 mA h g−1, 195 mA h g−1, 84 mA h g−1 at currents of 50 mA g−1, 100 mA g−1, 200 mA g−1, 500 mA g−1, 1 A g−1, 2 A g−1, and 5 A g−1 respectively (Fig. 5d and e). Many reports show long-term cycling stability at higher rates, which are of limited application for stationary grid storage, where moderate rates between 0.25C and 2C are needed.1 The use of higher rates can mask the instability of the material by utilizing a lower depth of discharge and shortened time period, which can lead to less dissolution.22 In comparison with the lower rate, the cycling stability of TQD at 1 A g−1 is expectedly better, reaching 70.7% capacity retention after 400 cycles (Fig. 5f).
To further elucidate the possible H+ and Zn2+ co-insertion mechanism three-electrode cyclic voltammetry (CV) measurements with Ag/AgCl reference electrode and Pt counter electrode were performed. Four aqueous electrolytes were tested, including 4 M ZnSO4 with a measured pH value of 3.3, 4 M ZnSO4 + H2SO4 (pH = 1), H2SO4 (pH = 1), and H2SO4 (pH = 3.3) (Fig. 7a, b and S3†). CV measurement in 4 M ZnSO4 showed four couples of distinguishable cathodic and anodic peaks located at −0.46/−0.68 V, −0.06/−0.22 V, 0.10/0.03 V, and 0.29/0.22 V, which roughly coincide with d(Q − Q0)/dE peaks obtained with galvanostatic cycling in Zn–TQD battery (Fig. 7c). The comparison showed differences in the peak intensities, which could arise due to the differences in the used scan rate (galvanostatic mode used approximately 110 times slower scan rate than CV). Solution of H2SO4 (pH = 3.3), which simulates the concentration of H+ ions in 4 M ZnSO4 was used to test the possibility of H+ insertion into TQD without the interference of Zn2+ ions. The measurement revealed that TQD can react with H+ ions even at very low H+ concentrations (Fig. 7b). On the other hand, it showed approximately much lower electroactivity in comparison with 4 M ZnSO4 electrolyte, which indicates the need of Zn2+ co-insertion for complete utilization (Fig. 7a, green). The use of more concentrated H2SO4 (pH = 1) electrolyte provided peak currents comparable to the 4 M ZnSO4 electrolyte (Fig. 7a, blue). The measurement exhibited four sets of cathodic and anodic peaks, which after shifting according to the Nernst equation for the conditions in H2SO4 (pH = 3.3) roughly coincide with CV peaks in 4 M ZnSO4 electrolyte further suggesting the possibility of H+ insertion in 4 M ZnSO4 electrolyte (Fig. S3a†).
Difference of CV curves in 4 M ZnSO4 (pH = 1) and H2SO4 (pH = 1) electrolytes with same H+ activity further indicate on Zn2+ co-insertion in electrolytes containing Zn2+ ions (Fig. 7a, red). To prove the possibility of Zn2+ insertion into TQD we employed Zn–TQD battery with water-free electrolyte 1 M zinc bis(trifluoromethylsulfonyl)imide Zn(TFSI)2 in diglyme (G2),22 which excluded the presence of H+ ions (Fig. 7d, blue curve). Although the system exhibited significantly lower capacity in comparison with 4 M ZnSO4 electrolyte (78.5 mA h g−1vs. 503.4 mA h g−1), it proved the possibility of Zn2+ insertion without H+ co-insertion. Because the choice of the electrolyte can have a profound effect on galvanostatic cycling additional “Zn2+ ion favoring” electrolyte 2.2 M zinc triflate (Zn(OTf)2) in 70% polyethylene glycol (PEG) was tested, where insertion of H+ ions is suppressed due to the strong interactions between PEG and H2O.30 In comparison with 1 M Zn(TFSI)2 in G2 the system exhibited a lot higher specific capacity of 324.8 mA h g−1, which was still significantly lower than the value obtained in 4 M ZnSO4. These results serve as additional proof of the synergistic role of the Zn2+ and H+ co-insertion mechanism. Although galvanostatic cycling of TQD in 2.2 M Zn(OTf)2 in 70% PEG in water exhibited lower specific capacity than in 4 M ZnSO4, it delivered a higher average voltage (0.83 V vs. 0.67 V, respectively) and higher capacity retention after 80 cycles at 100 mA g−1 (72.9% vs. 42.7%) (Fig. 7f). Utilization of water-suppressing electrolytes could therefore serve as another tool for the stabilization of cycling stability of small organic cathode materials, where a possible explanation could lie in a lower solubility of the discharged products in less polar PEG.
Based on the aforementioned results and results from the literature,20,22 we propose a redox mechanism where TQD is reversibly switching from a fully oxidized quinone state to a fully reduced state utilizing CN and C
O redox centers with H+ and Zn2+ co-insertion (Fig. 8).
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3ta01400b |
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