Open Access Article
Vladislav Y. Shevtsov†
ab,
Francesco Gambino†
cd,
Daniil R. Nosov
a,
Jérôme Guillot
e,
Silvia Porporato
cd,
Giuseppe A. Elia
cd,
Claudio Gerbaldi
*cd and
Alexander S. Shaplov
*a
aFunctional Polymeric and Particulate Materials Unit, Luxembourg Institute of Science and Technology (LIST), 28 avenue des Hauts-Fourneaux, L-4362 Esch-sur-Alzette, Luxembourg. E-mail: alexander.shaplov@list.lu
bDepartment of Physics and Materials Science, University of Luxembourg, 2, avenue de l'Université, L-4365 Esch-sur-Alzette, Luxembourg
cGAME Lab, Department of Applied Science and Technology (DISAT), Politecnico di Torino, Corso Duca degli Abruzzi 24, 10129 Torino, Italy. E-mail: claudio.gerbaldi@polito.it
dNational Reference Center for Electrochemical Energy Storage (GISEL) - INSTM, Via G. Giusti 9, 50121, Firenze, Italy
eAdvanced Analyses and Support Unit, Luxembourg Institute of Science and Technology (LIST), 28 avenue des Hauts-Fourneaux, L-4362 Esch-sur-Alzette, Luxembourg
First published on 27th April 2026
High crystallinity in PEO-based solid polymer electrolytes limits ion transport and stability in Li-metal batteries. Two asymmetric, low-melting thioether-TFSI Li salts were synthesized via a thiol–ene route and incorporated into PEO. They suppress crystallinity while maintaining conductivity and electrochemical performance, and reduce Al corrosion via stable passivation layer formation. The resulting SPEs have improved Li compatibility and enable stable Li||LiFePO4 cells cycling with high capacity retention and coulombic efficiency.
Because safety is critical for market deployment, a major breakthrough was the introduction of lithium bis(trifluoromethylsulfonyl)imide (LiTFSI, Scheme 1), featuring a weakly coordinating, highly charge-delocalized TFSI− anion.2 Weak coordination enhances Li+ mobility, enabling high ionic conductivity (3.9 × 10−4 S cm−1 at 70 °C,3 the typical operating temperature of LiMP batteries), together with excellent thermal and chemical stability, prompting efforts to replace the less thermally stable and more hazardous LiPF6.3–5 However, LiTFSI exhibits several well-known drawbacks in PEO-based SPEs (Table 1), including a low Li+ transference number (TLi+ = 0.22),6 lower ionic conductivity than LiPF6/PEO systems,7 poor long-term interfacial stability toward Li metal due to unstable SEI formation, and pronounced corrosion of aluminum current collectors.4,8 These limitations have driven intensive research into TFSI− anion modification and the development of new weakly coordinating anions to achieve higher ionic conductivity, improved Li-anode interfacial stability, and better cycling performance with aluminum current collectors.6,9–12 One promising strategy involves Li salts that are liquid at battery operating temperatures, as reduced melting points (Tm) can plasticize the PEO matrix, suppress crystallization, and broaden the operational temperature window of SPEs.
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| Scheme 1 TFSI and asymmetric derivatives: reference structures and synthesis of thioether-TFSI Li salts. | ||
| Li salt | Neat Li salt | Li salt/PEO polyelectrolytea | |||
|---|---|---|---|---|---|
| Tmb (°C) | Tonsetc (°C) | σ 70 °C (S cm−1) | LSVd 70 °C (V) | TLi+e 70 °C | |
| a The Li salts/PEO blends composition was fixed at [EO]/[Li+] = 20 (note: PEO with different molecular weights may be used).b Melting point (Tm) determined by DSC under N2 (note: heating rates of 5 or 10 °C min−1 may be employed).c Onset weight loss temperature determined by TGA in air (note: heating rates of 5 or 10 °C min−1 may be employed).d Anodic stability by linear sweep voltammetry (LSV) at 70 °C.e Li-ion transference number measured at 70 °C. | |||||
| Li TFT-TFSI | 136 | 240 | 2.1 × 10−4 | 4.4 | 0.23 |
| Li MET-TFSI | 71 | 235 | 3.0 × 10−4 | 4.1 | 0.29 |
| For comparison: | |||||
| Li TFSI6,14 | 233 | 356 | 3.9 × 10−4 | 4.6–5.1 | 0.22 |
| Li BETI13 | 328 | n.d | 5.0 × 10−4 | n.d | 0.24 |
| Li C4C414 | 352 | 334 | 2.2 × 10−4 | 5.3 | 0.29 |
| Li FTFSI6 | 110 | 150 | 9.7 × 10−4 | 5.2 | 0.17 |
| Li sTFSI18 | 118 | 300 | 7.5 × 10−4 | 5.4 | 0.29 |
| Li DFFSI19 | n.d. | 184 | 6.6 × 10−4 | n.d | 0.23 |
| Li DFTFSI20 | 194 | 242 | 5.7 × 10−4 | 5.2 | 0.35 |
| Li EFA23 | 112 | 308 | 2.7 × 10−4 | 4.0 | 0.43 |
| Li TFEMSI24 | 181 | 318 | 3.5 × 10−4 | n.d | 0.64 |
| Li BTFSI11,25 | n.d. | 352 | 3.6 × 10−4 | 4.0 | 0.69 |
Early studies in this field examined how the length and symmetry of fluoroalkyl chains in TFSI-like anions affect the properties of Li salts and their SPEs (Scheme 1; e.g., LiBETI,13 LiFTFSI,6 LiC4C4,14 LiC1C4,15 etc.). Increasing perfluoroalkyl chain length (LiTFSI-LiBETI-LiC4C4) was shown to improve SPE interfacial compatibility with both anode and cathode materials (Table 1).14 However, this modification increased Tm of salts melting points, exerted opposing effects on ionic conductivity of Li salt/PEO materials, and does not enhance Li+ transport, as highly fluorinated groups interact only weakly with PEG chains.6,13,14,16 In contrast, introducing asymmetry into the TFSI anion substantially reduces Tm while improving other SPE properties.17–20 Consequently, recent research has focused on asymmetric weakly coordinating anions, with several TFSI-type systems showing attractive features (Scheme 1). Lithium super-TFSI (sTFSI17,18) exhibits a markedly lower melting point (118 °C18 vs. 233 °C for LiTFSI). This reduction, together with enhanced salt solubility, allows PEO SPEs to achieve approximately doubled ionic conductivity at 70 °C and a slightly increased TLi+ without compromising electrochemical stability (Table 1).18 However, stable cycling of Li||LiFePO4 cells with LisTFSI has been demonstrated only in ionic liquid (IL) electrolytes, requiring combination with ILs such as [N-alkyl-N-methylpiperidinium+ sTFSI−].21
Building on anion asymmetry, several studies introduced a positive dipole into the anion structure, leading to DFTFSI7,20,22 and DFFSI19 anions, where one fluorine atom was replaced by hydrogen. This modification caused only a modest reduction in Tm of Li-salt; however, LiDFTFSI/PEO20 and LiDFFSI/PEO19 SPEs showed ∼1.5 fold higher ionic conductivity than LiTFSI/PEO, reduced interfacial resistance, improved compatibility with metal Li, and strongly suppressed Al corrosion. LiDFTFSI/PEO20 exhibited increased TLi+ (0.22 to 0.35), attributed to –CF2H⋯PEO hydrogen bonding. As a result, LiDFFSI/PEO enabled Li||LiFePO4 cycling at 70 °C for up to 125 cycles at C/10,19 while LiDFTFSI/PEO, benefiting from higher anodic stability, supported Li||Li-S cells at similar rates, albeit with capacity fading.22
A related strategy combining anion asymmetry with stronger polymer interactions was applied in EFA23 and TFEMSI24 anions, where a tertiary amine is directly attached to the sulfonyl group. Incorporation of short PEG chains lowers the Tm of LiEFA to 112 °C (Table 1) and increases the TLi+ to 0.43 via segmental entanglement and hydrogen bonding with PEO.23 However, this design reduced electrochemical stability toward Li (≈4 V) and slightly lowered thermal stability.23 Nevertheless, LiEFA/PEO SPEs enabled stable Li°||LiFePO4 cycling for 30 cycles at C/3, attributed to (i) suppressed anion mobility, reducing concent-ration polarization and dendrite formation, and (ii) formation of a stable SEI that facilitates Li+ transport across the interface.
To date, one of the highest Li+ transference numbers reported for PEO-based SPEs (TLi+= 0.69) has been achieved using LiBTFSI.25 This high selectivity was attributed to π–π stacking between anion-attached benzene rings, promoting anion self-aggregation and suppressing negative-charge mobility. While the total ionic conductivity of LiBTFSI/PEO is comparable to LiTFSI/PEO, its anodic stability is reduced to ∼4.0 V, and aluminum corrosion was not evaluated.25 Nevertheless, the SPE showed excellent compatibility with Li metal, enabling stable solid-state Li°||LiFePO4 cycling with 86% capacity retention after 200 cycles at C/3 rate.
Despite these advances and other strategies, such as the incorporation of fillers,26,27 simultaneously improving ionic conductivity in PEO-based SPEs and mitigating interfacial instability in LiMP batteries remains challenging, as gains often compromise Li+ selectivity, thermal and electrochemical stability, moisture resistance, or aluminum compatibility. Moreover, reducing fluorine content in Li salts is increasingly important for large-scale deployment and regulatory compliance. To address the need for non-corrosive lithium salts with weakly coordinating anions, low Tm, and SPEs combining high ionic conductivity with elevated TLi+, we developed a simple synthetic strategy based on thiol–ene click chemistry (Scheme 1).28 This approach uses commercially available potassium vinyl-TFSI29 and enables modular access to a broad family of asymmetric anions through a two-step reaction with selected thiols. The method features operational simplicity, consistently high yields, facile product isolation, and high purity suitable for electrochemical applications.
In this work, vinyl-TFSI K was reacted with 2,2,2-trifluoro-ethanethiol and 2-(2-methoxyethoxy)ethane-1-thiol (Scheme 1). The former affords a minimal asymmetric anion bearing a fluorinated –CH2–CF3 group, while the latter introduces two ethylene oxide units expected to interact with PEO and reduce anion mobility. Subsequent cation exchange yielded the target thioether-TFSI lithium salts: lithium ((2-((2,2,2-trifluoroethyl)-thio)ethyl)sulfonyl)-N-(trifluoromethylsulfonyl)-imide (Li TFT-TFSI) and lithium ((2-((2-(2-methoxyethoxy)ethyl)thio)ethyl)-sulfonyl)-N-(trifluoromethylsulfonyl)imide (Li MET-TFSI). Structural integrity and purity were confirmed by 1H, 7Li, 13C and 19F NMR, IR spectroscopy, and elemental analysis (Fig. S1–S11, SI). 2D NMR experiments (HSQC, HMBC) enabled full proton and carbon assignment of Li MET-TFSI (Fig. S12 and S13, SI).
Differential scanning calorimetry (DSC) showed melting points (Tm, observed during the first heating) of 136 and 71 °C for Li TFT-TFSI and Li MET-TFSI, respectively (Fig. S14 and S15, SI), with the latter representing the lowest Tm reported for TFSI-type Li salts to date (Fig. 1a). This strong melting-point reduction is attributed to the methoxyethoxy-thioethyl substituent, whose steric and conformational effects disrupt anion packing and suppress crystallization. Consistently, the second DSC cycle showed no crystallization upon slow cooling and only a glass transition (Tg ≈ −3.0 °C) was detected. Thermogravimetric analysis (TGA) in air revealed an onset of weight loss above 235 °C (Fig. 1b), indicating sufficient thermal stability for practical application, as LiMP batteries typically operate below 100 °C.
Converting the Li salts into PEO-based SPEs with an [EO]/[Li+] ratio of 20 yielded self-standing, semi-transparent membranes, whose thermal properties were analyzed by DSC (Fig. 1c and Fig. S16, S17, SI). Fig. 1c shows first-heating DSC traces of Li TFT-TFSI/PEO and Li MET-TFSI/PEO SPEs, benchmarked against LiTFSI/PEO. All samples exhibited a glass transition (Tg = −37.4 to −29.6 °C) and a PEO melting transition (Tm = 57.3–60.5 °C). The Tg values decrease in the order: −29.6 °C (Li TFT-TFSI/PEO) > −35.7 °C (LiTFSI/PEO) > −37.4 °C (Li MET-TFSI/PEO), indicating a stronger plasticizing effect of Li MET-TFSI. Analysis of the melting transition showed Tm values of 60.5 °C (LiTFSI/PEO) > 58.0 °C (Li MET-TFSI/PEO) > 57.3 °C (Li TFT-TFSI/PEO), consistent with melting enthalpies ΔHm of 68.5, 66.2, and 54.1 J g−1, respectively. These results demonstrate reduced PEO crystallinity in Li MET-TFSI/PEO and Li TFT-TFSI/PEO compared to LiTFSI/PEO. This reduction arises from both the lower intrinsic melting points of the new salts and their enhanced plasticizing efficiency. Additionally, suppressed PEO recrystallization can be attributed to the increased flexibility and larger substituents of the modified TFSI anions,6,18,22 which enhance segmental mobility and hinder crystallization.
Fig. 1d presents Arrhenius plots of total ionic conductivity (σ), reflecting combined Li+ and anion transport, for Li TFT-TFSI/PEO, Li MET-TFSI/PEO, and LiTFSI/PEO SPEs. In the near-ambient range (20–30 °C), Li MET-TFSI/PEO shows the highest conductivity (5.4 × 10−7 S cm−1), exceeding LiTFSI/PEO (4.7 × 10−7 S cm−1) and Li TFT-TFSI/PEO (2.0 × 10−8 S cm−1). However, conductivities of all systems remain insufficient for LiMP batteries, mainly due to crystalline PEO domains that strongly impede ion transport. Upon heating above 60 °C, conductivity increased sharply for all SPEs, reaching ∼10−4 S cm−1 (Fig. 1d), attributed to melting-induced amorphization of the PEO matrix that enables continuous ion-conducting pathways and enhances ion mobility.1 At 70 °C, ionic conductivity increased with decreasing effective anion volume in the order (Table 1): 2.1 × 10−4 S cm−1 (Li TFT-TFSI/PEO) < 3.0 × 10−4 S cm−1 (Li MET-TFSI/PEO) ≤ 3.9 × 10−4 S cm−1 (LiTFSI/PEO).
To evaluate the suitability of thioether-TFSI lithium salts for application in LiMP batteries, the electrochemical properties of Li TFT-TFSI/PEO and Li MET-TFSI/PEO were systematically investigated with particular attention to the TLi+, anodic stability, compatibility with the Li metal electrode, and cycling performance in Li°||Lix/PEO||LiFePO4 (LFP) cells. The Li-ion transference number of the SPEs was determined using the Evans–Vincent–Bruce method (Fig. S18). Notably, Li MET-TFSI/PEO exhibited a higher TLi+ value (0.29) compared to LiTFSI/PEO (0.22) and Li TFT-TFSI/PEO (0.23). This enhanced TLi+ can be attributed to a combination of two effects: (i) increased mobility of Li+-containing species resulting from the lower Tg of the SPE, enabled by the stronger plasticizing effect of Li MET-TFSI, and (ii) reduced mobility of the MET-TFSI anions due to their stronger interactions with the PEO matrix.
The linear sweep voltammograms (LSVs) of the SPEs are compared in Fig. 2a. All SPEs show anodic breakdown at ∼4 V vs. Li/Li+, attributed to oxidative degradation of the PEO matrix.30 Increasing the potential to ∼4.8 V resulted in a sharp rise in polarization current, indicating the onset of oxidative decomposition involving the thioether anions, possibly together with PEO. The oxidative stability of the Li salt/PEO blends at 70 °C follows the trend: Li TFSI (LSV = 4.6 V) > Li TFT-TFSI (4.4 V) > Li MET-TFSI (4.1 V). Nonetheless, both newly developed Li salts exhibit sufficient anodic stability for operation in LFP batteries. Anodic dissolution tests were performed using 1 M Li salt solutions in EC/DMC (1
:
1 v/v) with uncoated Al discs by holding the potential 1.3 V above the open-circuit potential of the corresponding half-cell (Fig. S19, SI). During first cycle, current densities of ∼0.9 and ∼0.1 µA cm−2 were recorded for Li MET-TFSI and Li TFT-TFSI, which are negligible compared to LiTFSI, for which a sustained current density of ∼15 mA cm−2 was observed (Fig. S19). This pronounced response for LiTFSI clearly indicates anodic dissolution of the Al° current collector.7 In contrast, the very low currents for Li MET-TFSI and Li TFT-TFSI are attributed to the formation of a highly resistive passivation layer on the Al surface, effectively suppressing anodic dissolution.7,31,32 XPS analysis revealed increased Li- and F-rich species on Al after anodic dissolution in Li MET-TFSI and Li TFT-TFSI electrolytes, compared to LiTFSI (Fig. S20 and S21), indicating a more fluoride-rich interphase with higher LiF and AlF3 content and improved corrosion protection (see SI). Strongly reduced corrosion was further confirmed by FESEM: severe pitting was observed for LiTFSI after cycling (Fig. S22, SI),31 whereas no pitting features were detected on Al discs from Li MET-TFSI or Li TFT-TFSI electrolytes (Fig. S23 and S24, SI). Fig. 2b shows the discharge capacity as a function of current density (C/20, C/15, C/10, C/5, and back to C/15) for Li°||Lix/PEO||LiFePO4 cells. SPEs based on Li TFT-TFSI and Li MET-TFSI display stable charge/discharge behavior across all C-rates, together with excellent cycling stability and high Coulombic efficiency. Both SPEs maintain capacities close to the theoretical value of LiFePO4 (≈160 mAh g−1), with Coulombic efficiencies above 98% at all tested rates (Fig. 2b and S25–S27, SI), whereas the conventional LiTFSI/PEO electrolyte delivers significantly lower capacities of ∼130–140 mAh g−1 under identical conditions (Fig. S28 and S29, SI). Fig. 2c presents galvanostatic lithium plating/stripping in Li° symmetric cells at 70 °C and different current densities. While LiTFSI/PEO exhibits pronounced voltage instabilities already at 0.1 mA cm−2, the TFT-TFSI- and MET-TFSI-based SPEs allow stable cycling at 0.2 mA cm−2 with lower overpotentials than the reference system. During long-term cycling at 0.05 mA cm−2 (Fig. 2d), the Li TFT-TFSI/PEO and Li MET-TFSI/PEO cells remained stable for over 600 h, whereas the LiTFSI-based cell short-circuited after ∼250 h, indicating markedly improved Li° electrode stability due to reduced concentration polarization and suppressed dendritic lithium growth. Moreover, Li TFT-TFSI and Li MET-TFSI SPEs sustain higher current densities compared to LiTFSI/PEO that short-circuits rapidly, as indicated by CCD tests (Fig. S30, SI).
In summary, two asymmetric thioether-TFSI lithium salts address key limitations of LiTFSI-based PEO electrolytes. Their low melting points suppress PEO crystallinity, enabling plasticization while maintaining ionic conductivity and Li+ transference number. Both salts inhibit aluminum corrosion via the formation of stable passivation layer. In PEO-based SPEs, this yields improved Li compatibility and stable long-term Li||LiFePO4 cells cycling with high capacity retention and Coulombic efficiency. The modular thiol–ene synthesis enables structural tunability with reduced fluorine content, supporting scalability and regulatory compliance.
:
1 v/v) liquid electrolytes; XPS analysis of aluminium disks after dissolution, specific capacity and coulombic efficiency as a function of cycle number for Li°||Li TFT-TFSI/PEO||LiFePO4 and Li°||Li MET-TFSI/PEO||LiFePO4 cells during galvanostatic cycling at C/15 and 70 °C as well as their potential vs. specific capacity profiles, and critical current density tests has been provided. See DOI: https://doi.org/10.1039/d6cc00051g.
Footnote |
| † V.Y.S and F.G. contributed equally to this work. |
| This journal is © The Royal Society of Chemistry 2026 |