- Research Article
- 10.1149/ma2025-022298mtgabs
Electrochemical and Physicochemical Properties of LiFSI/γ-Butyrolactone (GBL)-Based Electrolytes for Li-Ion Batteries
- Nov 24, 2025
- Electrochemical Society Meeting Abstracts
- Yuiko Koitabashi + 1 more +1
Liquid electrolytes in Li-ion batteries have been extensively developing to improve ionic conductivity, electrochemical stability, thermal stability, and safety by using various solvents, high concentration electrolytes, electrolyte additives, and lithium imide salts such as lithium bis (trifluoromethanesulfonyl)imide (LiTFSI) and lithium bis(fluorosulfonyl)imde (LiFSI). The electrolytes extensively used in commercial Li-ion batteries are LiPF6 dissolved in some carbonate solvents such as propylene carbonate (PC), ethylene carbonate (EC), dimethyl carbonate (DMC), methyl ethyl carbonate (MEC), and diethyl carbonate (DEC). Therefore, the optimal temperature range of the Li-ion batteries is a narrow range of 15℃-35 ℃ since Li-ion battery operated in the out of the comfortable temperature range will accelerate to degrade with serious risks of safety problems such a fire and explosion. The carbonate solvents occur the oxidation with CO2 gas generation on high-voltage cathodes such as LiCoO2, LiNi1-x-yCoxMnyO2, and LiNi0.5Mn1.5O4 under high-temperature conditions.In this work, we investigated the electrochemical and physicochemical properties of LiFSI/GBL-based electrolytes and effects of additives into the electrolytes on application to Li-ion batteries using LiNi0.8Co0.1Mn0.1O2 (NCM) cathode and TiNb2O7 (TNO) anode [1]. GBL has attractive properties of a low melting point of -43.6℃, a high boiling point of 204℃, and a high flash point of 98℃. However, Li-salt used for GBL-based electrolytes was not LiPF6 but LiBF4 [2] because LiBF4 is significantly chemical stable in GBL solvent. LiPF6 decomposes GBL, which is caused by HF generation from decomposition of LiPF6. Therefore, we have focused on LiFSI with chemical stability and high conductivity for the GBL-based electrolytes. Furthermore, we investigated the cosolvents for the GBL-based electrolyte for a decrease in the viscosity. Propyl propionate (PP) was used as the cosolvent because it has advantageous properties of only a low viscosity but also a very low melting point of -76℃ and a high boiling point of 122℃ compared to DMC and MEC. This paper reports on ionic conductivity, viscosity, self-diffusion coefficient (D Li) of Li+ ion of LiFSI/GBL-based electrolytes, and the performance of fabricated TNO/NCM pouch cells using the LiFSI/GBL/PP electrolytes with additives.Fig.1(a) and (b) show ionic conductivity of GBL electrolytes and other solvent electrolytes dependent on Li-salt concentration. The conductivity of LiFSI/GBL electrolyte was higher than that of LiTFSI/GBL and LiBF4/GBL electrolyte in all the concentration. A low-concentration LiFSI/GBL (1:10 by mol) electrolyte at a LiFSI molar fraction (XLiFSI) of 0.091exhibited the highest conductivity of 12.3 mS cm-1 at 25℃ compared to LiBF4/GBL, LiTFSI/GBL, and LiFSI-based electrolytes with other solvents of PC, DMC, DEC, and PP. Electrochemical stability of TNO and NCM electrode in the low-concentration LiFSI/GBL at XLiFSI=0.111 electrolyte was investigated by AC-impedance and liner sweep voltammetry (LSV) measurement. Impedance spectra as shown in Fig.2 indicated that a large interface resistance of the TNO electrode in the GBL electrolyte was significantly decreased by adding 2wt% fluoroethylene carbonate (FEC). The anodic dissolution of Al current collector for the NCM cathode in the electrolyte by LSV measurement was effectively suppressed by adding 2wt% lithium difluoro(oxalate)borate (LiDFOB), which overcame the strong corrosion of Al. Adding PP cosolvent into the LiFSI/GBL electrolyte decreased the viscosity and increased D Li in the electrolyte. We fabricated TNO/NCM pouch cells (70 ×100 ×1.2 mm) using LiFSI/GBL/PP and LiFSI/other solvent electrolytes at XLiFSI=0.111 with the additives. Charge-discharge cycling tests were conducted between 1.5 V and 3.0 V. The nominal capacity and voltage at 0.2 C were 900 mAh and 2.25 V, respectively. Fig.3 shows charge-discharge rate cycle performance at -20℃ of the cells with various electrolytes. Low-temperature rate capability of the cells using the LiFSI/GBL/PP electrolytes was superior to that using the DMC, PP, GBL, and PC electrolyte. It was demonstrated that the cells using the LiFSI/GBL/PP (1:2:6) electrolyte maintained high capacity with less gas generation by charge-discharge cycle tests between -20℃ and 45℃ compared to the cell using the LiFSI/DMC electrolyte. Fig.4 shows the amount and composition of each gas generated from the cells after 400 cycles at 45℃. The amount of CO2 generated from the LiFSI/GBL/PP electrolyte was 1/10th smaller than that from the DMC electrolyte, indicating that the LiFSI/GBL/PP electrolyte is electrochemical stable under a high-potential condition of the charged NCM cathode. We propose that low-concentration LiFSI/GBL/PP electrolytes with the additives of FEC and LiDFOB are promising electrolytes with high-rate, low-temperature performance, and good electrochemical stability with less gassing for wide temperature operation in Li-ion batteries.
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