Open Access Article
Zhiming Zhou
abc,
Guojun Chenabc,
Guojun Yuabc,
Xiaohao Liu
*abc and
Shulei Chou
*abc
aInstitute for Carbon Neutralization Technology, College of Chemistry and Materials Engineering, Wenzhou University, Wenzhou, Zhejiang 325035, China. E-mail: liuxh@wzu.edu.cn; chou@wzu.edu.cn
bZhejiang Provincial Key Laboratory of Advanced Battery Materials and Technology, Wenzhou University Technology Innovation Institute for Carbon Neutralization, Wenzhou, Zhejiang 325035, China
cZhejiang-Australia International Joint Laboratory for Sodium-Ion Batteries, Wenzhou University Technology Innovation Institute for Carbon Neutralization, Wenzhou, Zhejiang 325035, China
First published on 29th May 2026
The increasing demand for high-energy-density lithium-ion batteries (LIBs) has intensified concerns regarding electrolyte flammability, interfacial degradation, and thermal runaway. Phosphazene-based compounds, particularly ethoxy(pentafluoro)cyclotriphosphazene (PFPN), have emerged as promising multifunctional electrolyte compounds that synergistically address these challenges. This review systematically summarizes the molecular design strategies and dual functional mechanisms of phosphazene-based compounds. Their flame-retardant capability operates through gas-phase radical scavenging and condensed-phase barrier effects. P- and N-containing fragments capture H˙ and OH˙ radicals to interrupt combustion chain reactions. Simultaneously, these compounds participate in constructing robust, inorganic-rich solid electrolyte interphase and cathode electrolyte interphase films, suppressing electrolyte decomposition and enhancing interfacial stability. The effectiveness of PFPN-based compounds is evaluated across diverse battery systems, including LiFePO4, LiNixCoyMnzO2, lithium metal, and SiOx/C anodes, demonstrating significant improvements in cycling stability, overcharge resistance, and thermal safety. Synergistic effects of PFPN with other functional components in composite additive systems are also discussed. Finally, future perspectives are outlined, encompassing advanced in situ characterization, machine learning-assisted electrolyte screening, and validation in large-format cells to accelerate commercial deployment.
To address these challenges, fluorocyclophosphazene compounds have emerged as promising functional components for constructing intrinsically safer electrolytes, owing to their unique structural tunability and multifunctional characteristics. Among them, PFPN stands out as a representative example, having been explored not only as a highly effective flame-retardant additive but also as a co-solvent and functional diluent in advanced electrolyte formulations.7,8 Whether utilized in trace amounts or as a major component, PFPN provides efficient flame retardancy in the gas phase owing to its high phosphorus content and fluorinated structure. More importantly, its electron-deficient P
N backbone and fluorinated substituents enable the regulation of Li+ solvation chemistry, promote the formation of robust, inorganic-rich cathode electrolyte interphase (CEI)/solid electrolyte interphase (SEI), and suppress transition-metal dissolution. These versatile roles allow PFPN to effectively address the long-standing trade-off between electrolyte flammability and interfacial instability (Fig. 1).
Based on these versatile properties, PFPN has demonstrated irreplaceable application value in various lithium-ion battery systems. This review aims to bridge the gap between intrinsic material characteristics and practical battery performance by systematically summarizing the structure–activity relationships in different cathode and anode systems. The dual mechanisms of flame retardancy and interfacial regulation are first analyzed, followed by a focused discussion on the practical performance of PFPN in typical battery systems, including lithium iron phosphate (LFP), high-nickel ternary (NCM), lithium metal batteries (LMBs), and SiOx/C system. By reviewing current research progress, this paper clarifies how PFPN can be employed for precise electrolyte engineering to target the specific issues of different battery systems, such as iron dissolution in LFP and oxidative decomposition in high-nickel cathodes. Finally, the challenges and opportunities for future commercial application are discussed.
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| Fig. 2 Schematic of (a) combustion mechanism in commercial carbonate electrolyte and (b) flame retardant mechanism in electrolyte with PFPN. | ||
Experimental studies have demonstrated the remarkable flame-retardant efficiency of PFPN.9–12 For example, incorporating merely 5 vol% PFPN into a conventional carbonate-based electrolyte reduces the self-extinguishing time (SET) from 144.89 to 12.38 s g−1 while increasing the critical oxygen index (COI) from 16.9% to 22.9%, effectively transforming the electrolyte from highly flammable to flame-retardant. Notably, fluorine substitution further enhances flame-retardant performance through synergistic interactions with phosphorus species. Fluorine-derived radicals react with H˙ radicals to form thermodynamically stable HF, reinforcing radical quenching and chain-termination effects. Additionally, fluorinated substituents improve the compatibility of the additive with electrolyte solvents, alleviating the deterioration of electrochemical performance that is often associated with conventional flame-retardant compounds.13
More importantly, the flame-retardant role of PFPN extends beyond its application as a minor additive in conventional electrolyte formulations. When used in large quantities as a co-solvent or functional diluent, the intrinsic nonflammability of PFPN fundamentally reconstructs the solvent environment of the electrolyte, endowing the entire system with inherent flame resistance.14–18 This design strategy transcends the traditional additive-based approach, which often suffers from a trade-off between flame retardancy and electrochemical performance at high additive loadings.19 As such, PFPN provides a viable pathway to simultaneously achieve enhanced safety and favorable electrochemical properties.20,21 PFPN compounds can significantly optimize interfacial stability by actively participating in the formation of both the SEI and the CEI.19
On the anode side, the P–F and P
N bonds in PFPN molecules are prone to reductive decomposition on the surface of graphite (Gr) or lithium metal.22,23 These bonds cooperate with the decomposition products of other electrolyte components (e.g., LiPF6) to form an inorganic-rich SEI film abundant in LiF and phosphate species.24,25 This robust SEI film exhibits high ionic conductivity and structural stability, which inhibits the co-intercalation of solvent molecules, suppresses the growth of lithium dendrites, and thereby reduces charge-transfer impedance. For instance, in LMBs, electrolytes containing PFPN can form an SEI film with a gradient structure, wherein inorganic components (e.g., LiF, Li2S) are predominantly distributed near the electrode surface, while organic components reside in the outer layer. This unique architecture effectively improves the reversibility of lithium deposition/stripping, maintaining a coulombic efficiency above 99.2%.
On the cathode side, fluorinated cyclophosphazene compounds mitigate the oxidative decomposition of the electrolyte under high voltage by facilitating the formation of a dense CEI film. For cathode materials such as LFP, LCO, and high-nickel NCM, this CEI film prevents the dissolution of transition-metal ions (e.g., Fe and Ni) and avoids interfacial degradation and short-circuit risks caused by anodic deposition.26 XPS and TOF-SIMS analyses demonstrate that the CEI film derived from PFPN is rich in P and N species.27–29 This specific composition inhibits the excessive accumulation of LiF and alleviates HF-induced corrosion of the cathode, thereby enhancing the overall cycling stability of the battery.30
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| Fig. 3 (a) Long-term cycling performance and (b) rate performance of LFP‖Gr full cells. Reproduced with permission.29 Copyright 2024, The Royal Society of Chemistry. (c) Rate performance of Gr‖Li cells. (d) Rate performance, (e) charge/discharge curves and (f) long-term cycling performance of LFP‖Gr full cells. (g) Long-term cycling performance of LFP‖Gr pouch cells at 1C. (h) Photograph showing an LED array powered by the LFP‖Gr pouch cell. Reproduced with permission.34 Copyright 2024, The Royal Society of Chemistry. | ||
In practical applications, electrolytes containing PFPN have demonstrated excellent long-term cycling stability in 2 Ah LFP‖Gr pouch cells, maintaining a capacity retention of 99.2% after 500 cycles (Fig. 4a).35 Moreover, under thermal abuse conditions, compared with single-component flame-retardant systems, the composite system combining PFPN with other functional components (e.g., DFEC, HTCN) can delay the occurrence of internal short circuits by nearly 50 minutes (Fig. 4b and c), effectively suppress gas evolution (Fig. 4d), and exhibit superior interfacial stability, while maintaining excellent electrochemical performance (Fig. 4e–g).36 This approach provides a robust safety guarantee for the application of LFP batteries in large-scale energy storage.
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| Fig. 4 (a) Electrochemical performance of 2 Ah LFP‖Gr pouch cells under 4.5 V overcharge limit. Reproduced with permission.35 Copyright 2025, Elsevier. (b) Time-voltage profiles of pouch cells filled with RCE and RDF electrolytes during heating in a thermal abuse chamber. (c) Time-temperature profiles of pouch cells filled with RCE and RDF electrolytes during heating in a thermal abuse chamber. (d) SEM images of Gr anodes after thermal abuse for pouch cells along with corresponding optical photographs of the pouch cells. (e) Impedance spectra of Li‖Gr half cells at the 700th cycle. (f and g) HRTEM images of graphite anodes after cycling. Reproduced with permission.36 Copyright 2026, American Chemistry Society. | ||
High-voltage layered cathodes have emerged as the mainstream choice for electric vehicles owing to their high energy density, yet they suffer from severe transition-metal ion dissolution and electrolyte oxidative decomposition under high-voltage operation.37–42 Concurrently, lithium metal batteries face the dual challenges of lithium dendrite growth and electrolyte flammability. PFPN compounds can significantly enhance the stability of these high-energy-density systems through synergistic interfacial regulation and flame-retardant mechanisms.25,28
Upon the introduction of PFPN, the electrolyte undergoes preferential oxidation and decomposition, simultaneously generating linear polymers, polycyclic polymers, LiNO3, RONO2Li (RONO2: nitrate ester functional group, with R standing for any organic residue), Li3PO4, and ROPO3Li (ROPO3: monoester phosphate) (Fig. 5a). The resulting species form a dense, uniform, and thin protective layer on the surface of the cathode material, which suppresses electrolyte decomposition and electrode corrosion, thereby safeguarding LiNi0.5Mn1.5O4 against structural degradation.26 In addition, the results of NMR and pH reveal that during cycling, PFPN retains its molecular structure in FEC-based electrolytes while enhancing SEI/CEI stability by acting as a scavenger for the Lewis acidic PF5 and HF, thereby significantly suppressing the continuous decomposition of FEC and the LiPF6 salt (Fig. 5b–f).24
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| Fig. 5 (a) Illustration of the mechanism of PFPN additive decomposition on the surface of the electrode. Reproduced with permission.26 Copyright 2018, Elsevier. (b) Photographs and pH of FF and FFP before and after storage at 60 °C for 48 h. (c and d) 19F NMR spectra of FF and FFP after storage at 60 °C for 48 h. (e) 13C NMR spectra of FFP and PFPN. (f) 19F NMR spectra. Reproduced with permission.24 Copyright 2025, Elsevier. | ||
Furthermore, ultrasonic imaging reveals that the PFPN-containing electrolyte exhibits significantly better wettability than the baseline electrolyte (Fig. 6a). Consequently, a 3 Ah, 4.4 V Li‖NCM811 pouch cell employing an FEC/LiPF6-based electrolyte containing 3 wt% PFPN and 2 wt% LiDFOB exhibits stable cycling over 100 cycles at 0.33C charge and 0.5C discharge, with excellent capacity retention (Fig. 6b).30 In thermal abuse tests, the thermal runaway trigger time of batteries using PFPN-containing electrolytes was delayed by approximately 2 h compared with that of batteries using conventional electrolytes, and the onset temperature of thermal runaway increased by 69 °C (Fig. 6c and d).43 When subjected to nail penetration tests, the 2 Ah pouch cells with PFPN-containing electrolytes exhibited no thermal runaway events, such as fire or explosion (Fig. 6e and f). LiNi0.8Mn0.1Co0.1O2‖Gr pouch cells employing PFPN-containing electrolytes achieved a capacity retention of 94.43% after 600 charge–discharge cycles at 1C.
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| Fig. 6 (a) Wettability and contact angle tests of electrolytes with Celgard 2400 polypropylene (PP) separator. (b) Cycling performance of 3 Ah pouch cell in the optimized electrolyte with electrolyte/capacity of 2.5 g Ah−1. Reproduced with permission.30 Copyright 2022, Elsevier. (c) Thermal runaway temperature profiles of SC-NCM811‖Gr 1 Ah cells under different electrolytes. (d) Thermal runaway temperature profiles of 2 Ah Ni90‖SiC cells under different electrolytes. (e) Temperature profiles during nail penetration test for Ni90‖SiC cells with FPN electrolyte and conventional electrolyte. (f) Nail penetration test of 2 Ah Ni90‖SiC cells. Reproduced with permission.43 Copyright 2024, Elsevier. | ||
Particularly in localized high-concentration electrolyte (LHCE) systems, PFPN plays a pivotal role as a functional diluent. While traditional high-concentration electrolytes exhibit excellent performance, they are often limited by high costs and excessive viscosity. Acting as a functional diluent, PFPN effectively reduces both the cost and viscosity of the electrolyte without disrupting the unique solvation sheath structure that is responsible for superior interfacial properties. Simultaneously, it actively participates in interfacial film formation and provides essential flame-retardant protection. With the combination of a carbonate-ether mixture solvent and PFPN as a diluent, the NCM811‖Gr cells employing E-PFPN exhibit outstanding cycling performance, with a capacity retention of 82.0% after 1000 cycles at 4.5 V (Fig. 7a and b) and 89.8% after 300 cycles at 4.6 V (Fig. 7c).16 Moreover, the cells also achieve superior cycling stability at elevated temperature (50 °C), retaining 82% capacity after 250 cycles at 4.5 V (Fig. 7d). When PFPN is used as a diluent in a methyl acetate (MA)-based electrolyte, it synergizes with anions to form a protective LiF-rich SEI, which effectively prevents continuous solvent decomposition (Fig. 7e).15 It enables LiNi0.65Co0.15Mn0.2O2 (NCM65)‖Gr full cell to maintain 94.6% capacity retention after 300 cycles at 1C and −20 °C (Fig. 7f). Moreover, it allows NCM65‖Gr full cell to operate at a high voltage of 4.6 V and −60 °C (Fig. 7g).
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| Fig. 7 (a) Cycling stabilities and (b) charge–discharge curves of NCM811‖Gr cells at a cut-off voltage of 4.5 V. (c) Cycling stabilities at a cut-off voltage of 4.6 V. (d) Cycling stabilities with 1/3C rate at 50 °C at a cut-off voltage of 4.5 V. Reproduced with permission.16 Copyright 2023, The Royal Society of Chemistry. (e) F 1s spectra of cycled Gr anodes. (f) Cycling performance of NCM65‖Gr cells at −20 °C with potential range from 2.8 to 4.5 V. (g) Charge–discharge curves of NCM65‖Gr full cell at −60 °C at a potential range of 2.8–4.6 V. Reproduced with permission.15 Copyright 2023, Elsevier. | ||
When PFPN, trioxane, and triethyl phosphate (TEP) are mixed, an SEI is formed that exhibits an outer layer of interwoven trioxane-derived polymers and N/P/F-rich inorganic species, along with a deeper region enriched with LiF (Fig. 8a).23 This SEI inhibits unwanted TEP decomposition at the anode, enabling NCM811‖Li full cells to cycle steadily at up to 4.5 V, with an outstanding capacity retention of 92% after 300 cycles (Fig. 8b). In addition, the 1.1 Ah NCM811‖Li pouch cells show no signs of thermal runaway upon heating to 250 °C, demonstrating exceptional safety (Fig. 8c). Specifically, the combination of PFPN and ethyl 1,1,2,2-tetrafluoroethyl ether (ETE) enables outstanding performance with LiNi0.5Co0.2Mn0.3O2 (NCM523) cathodes (23.5 mg cm−2). This is attributed to the hydrogen bonding between ETE and DME, along with the coordination of PFPN with Li+, which weakens the Li+-DME interaction and promotes an anion-enriched solvation structure (Fig. 8d–f), thereby facilitating the Li+ desolvation process and forming an inorganic-rich solid electrolyte interphase.17 As a result, 80% capacity retention is achieved after 430 cycles at 4.3 V and 84% after 310 cycles at 4.5 V (Fig. 8g), while a 331 mA h pouch cell achieves 148 cycles with 94.9% capacity retention (Fig. 8h).
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| Fig. 8 (a) TOF-SIMS depth profiles of C2H2O−, LiPN−, CNLiF−, Li3N−, LiF− and PO− species on the surface of Li anode after 10 cycles. (b) Cycling stability of NCM811‖Li coin cells. (c) Digital photos, and infrared thermographic images for NCM811‖Li pouch cells. Reproduced with permission.23 Copyright 2025, Wiley-VCH. Radial distribution functions calculated from MD simulation of (d) E-ETE and (e) E-ETE/PFPN. (f) Raman spectra. Cycling stability of (g) NCM523‖Li coin cells and (h) NCM523‖Li pouch cell. Reproduced with permission.17 Copyright 2025, Elsevier. | ||
SiOx@C anodes are regarded as promising candidates for next-generation lithium-ion batteries owing to their exceptionally high specific capacity. However, their practical application is severely hindered by massive volume expansion during cycling, which causes rupture of the SEI and rapid capacity fading.44–46 The incorporation of a composite additive system consisting of PFPN and other functional agents provides an effective solution to this challenge. Specifically, the combination of PFPN and FEC facilitates the formation of a dense, LiF-rich SEI film. This robust interphase prevents direct contact between the electrolyte and the SiOx@C anode, thereby mitigating the repeated rupture and reconstruction of the SEI layer. Excellent capacity retention of 87% after 200 cycles at 1C was achieved for NCM523‖SiOx@C pouch cells with a relatively high SiOx content of 10% (Fig. 9a).47 The mechanistic studies further reveal that PFPN cooperates with FEC to induce a unique molecular cling effect (MCE) on SiOx@C anodes (Fig. 9b). This effect enables PFPN to stably adsorb onto the electrode surface and participate in SEI formation, which cannot be achieved by PFPN alone. Meanwhile, PFPN reacts with key electrolyte intermediates, such as lithium ethyl methyl carbonate (LEMC) and lithium alkoxides, forming thermodynamically stable phosphorus-containing interphase species accompanied by LiF generation. This reaction pathway suppresses the formation of oligomeric hydrocarbon carbonate (OHC) byproducts, reduces parasitic reactions and gas evolution, and lowers cell polarization. As a result, the dual-additive system of FEC and PFPN constructs a uniform, inorganic-rich SEI that accommodates the large volume fluctuations of SiOx@C during cycling, significantly improving the long-term cycling stability and structural integrity of the electrode (Fig. 9c–h).
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| Fig. 9 (a) Long-term cycling of NCM523‖SiOx@C pouch cells. (b) Proposed reaction mechanism of LEMC with PFPN. SEM images after SEI formation with (c–e) the benchmark STD-FEC electrolyte blend and (f–h) the STD-FEC-PFPN electrolyte blend. Reproduced with permission.47 Copyright 2023, Wiley-VCH. (i) DSC curves (j) long-term cycling of SiO@C‖Li cells. EIS results of (k) before cycling and (l) after 100 cycles. Reproduced with permission.49 Copyright 2024, Elsevier. | ||
Thermal runaway and safety risks further restrict the application of SiOx@C anodes, and PFPN-based composite additives can effectively address these issues. PFPN possesses outstanding flame-retardant and thermal-stabilizing properties: at high temperatures, it decomposes to release fluorine and phosphorus radicals that interrupt combustion chain reactions, enabling self-extinguishing behavior and drastically reducing electrolyte flammability, thereby effectively suppressing thermal runaway and preventing fire/explosion hazards.48 Recent studies demonstrate that PFPN/tris(2,2,2-trifluoroethyl) borate (TTFEB) significantly enhances thermal stability.49 the initial exothermic temperature rises from 233.67 to 292.83 °C (Fig. 9i), and the apparent activation energy increases from 439.56 to 1090.01 kJ mol−1, strongly delaying thermal runaway. Meanwhile, this dual-additive system elevates capacity retention from 45.23% to 74.34% over 100 cycles in SiO@C‖Li half-cells (Fig. 9j), forms a thinner and more uniform LiF-rich SEI, reduces electrode impedance (Fig. 9k and l), accelerates Li+ transport, and reinforces electrode structural integrity.
Overall, the performance of PFPN-containing electrolytes is highly governed by PFPN molecular features, electrolyte formulation, and battery system chemistry. In conventional graphite- or LFP-based lithium-ion batteries, PFPN mainly acts as a low-dosage flame-retardant and film-forming additive, while inhibiting LiFSI-induced aluminum current collector corrosion. Under thermal abuse conditions, however, single PFPN exhibits limited protection and requires synergistic additives such as DFEC and HTCN for improved safety. For high-voltage layered oxide cathodes, PFPN realizes multifunctional interfacial regulation. It suppresses electrolyte oxidative decomposition and promotes the formation of LiF and phosphate-enriched CEI, which mitigates cathode-electrolyte parasitic reactions and enhances high-voltage stability. In LMBs, PFPN-derived F- and P-containing species build mechanically robust, ion-conductive SEI. Stable interphases still rely on synergistic additives including NaDFOB and FEC. Electrolyte anions also cooperatively regulate interfacial chemistry to construct LiF-rich protective layers. For SiOx@C anodes, PFPN synergizes with FEC to form dense LiF-rich SEI, alleviating volume-expansion-driven SEI rupture, gas evolution, and side reactions. Nevertheless, PFPN alone cannot stably adsorb on SiOx@C surfaces or efficiently participate in SEI construction, where the molecular cling effect of FEC is essential. These comparisons highlight that PFPN is not merely a universal flame retardant, but a structure-dependent multifunctional electrolyte component, whose interfacial behavior and high-voltage compatibility are strongly coupled with electrode chemistry and electrolyte design.
| Formula | Cathode‖anode | Voltage | Discharging rate | Cycling stability (capacity retention/cycles) | Performance in Ah-level pouch cells | SET/thermal runaway trigger temperatures | Ref. |
|---|---|---|---|---|---|---|---|
1.0 M LiPF6 in EC : DMC (1 : 1 by vol) + 3 wt% PFPN |
LFP‖Gr | 2.5–4.0 V | 1C | 97.25% 100 cycles | — | Lower than 10 s g−1 | 29 |
1.0 M LiFSI in DOL : PFPN (9 : 1 by vol) |
LFP‖Gr | 2.5–3.8 V | 1C | 88.7% 300 cycles | — | 0 s g−1 | 34 |
1.0 M LiPF6 in EC : DMC (3 : 7 by vol) + 4 wt% D3F + 3 wt% FK + 1.7 wt% PFPN |
LFP‖Gr | 2.5–3.8 V | 0.2C | 80.5% 200 cycles | 93% 200 cycles (1Ah) | 3 s g−1/168 °C | 36 |
1.0 M LiPF6 in EC : DEC : DMC (1 : 1 : 1 by vol) + 5 wt% PFPN |
LiNi0.5Mn1.5O4‖Gr | 2.5–5.0 V | 1C | 87.3% 100 cycles | — | 0 s g−1 | 26 |
1.0 M LiPF6 in EC : DEC (1 : 1 by vol) + 10 wt% PFPN |
LiNi0.5Mn1.5O4‖Gr | 3.0–4.9 V | 0.5C | 90.7% 100 cycles | — | 0 s g−1 | 25 |
LiFSI : DME : FEC : PFPN (1 : 1.5 : 0.5 : 3 by mol) |
NCM811‖Gr | 2.8–4.5 V | 1/3C | 82.0% 1000 cycles | — | 0 s g−1 | 16 |
1.5 M LiFSI in DME : PFPN (1 : 2 by vol) |
NCM811‖Li | 3.0–4.3 V | 0.5C | 86.5% 200 cycles | — | 0 s g−1 | 14 |
1.0 M LiPF6 in EC : DMC : EMC (1 : 1 : 1 by vol) + 7 wt% PFPN |
NCM811‖Li | 3.0–4.5 V | 1C | 89.5% 200 cycles | — | 0 s g−1 | 28 |
LiFSI : DMC : PFPN (1 : 3 : 3 by mol) |
LiCoO2‖Li | 3.0–4.5 V | 2C | 86.0% 1000 cycles | — | 0 s g−1 | 18 |
0.8 M LiFSI + 0.2 M LiTFSI + 0.6 M LiPF6 in PC : EMC (1 : 2 by vol) + 6 wt% PFPN |
NCM811‖Gr | 3.0–4.3 V | 1C | 94.43% 600 cycles | — | 0 s g−1/199 °C | 43 |
1.5 M LiFSI in TEP : PFPN (1 : 2 by vol) + 1 wt% trioxane |
NCM811‖Li | 2.8–4.5 V | 1.5C | 92.0% 300 cycles | — | 0 s g−1/250 °C | 23 |
LiFSI : DME : ETE : PFPN (1 : 1.2 : 1.6 : 0.8 by mol) |
NCM523‖Li | 2.8–4.5 V | 0.33C | 84.0% 310 cycles | — | 0 s g−1 | 17 |
1.0 M LiPF6 in EC : DMC : EMC (1 : 1 : 1 by wt) + 10 vol% PFPN |
NCM811‖Gr | 2.7–4.5 V | 1/3C | 81.7% 200 cycles | 83.2% 500 cycles (1Ah) | 0 s g−1/168.2 °C | 19 |
To promote the application of PFPN-containing electrolytes in LIBs for stable and safe energy storage, future research should focus on the following aspects: (i) the decomposition pathways of PFPN under realistic electrochemical conditions should be clarified. The P
N backbone, P–F bonds, and ethoxy substituent may undergo reductive or oxidative cleavage, producing LiF-, Li3N-, and phosphate-rich interphases. However, the exact sequence of bond breaking and its dependence on local Li+ solvation remain unclear advanced in situ/operando spectroscopic techniques, including in situ Raman, nuclear magnetic resonance (NMR), X-ray absorption fine structure (XAFS) spectroscopy, and online gas analysis should be integrated with first-principles calculations and theoretical simulations to identify PFPN-derived intermediates and correlate molecular decomposition with SEI/CEI formation. (ii) The compatibility of PFPN with high-voltage cathodes requires deeper investigation. For NCM811, Ni-rich layered oxides, Li-rich layered oxides, LNMO, and high-voltage LCO, PFPN may simultaneously act as a sacrificial film-forming additive, HF/PF5 scavenger, and flame retardant. However, oxidative decomposition, gas generation, transition-metal dissolution, and impedance growth remain potential failure modes. Advanced imaging techniques (e.g., cryo-TEM, in situ AFM, SEM, and TOF-SIMS depth profiling) should be applied to track the evolution of PFPN-derived CEI layers during long-term high-voltage cycling. (iii) Future molecular design should strike a balance among flame retardancy, viscosity, ionic conductivity, high-voltage stability and gas evolution. Compared with other phosphazene derivatives and conventional flame retardants, PFPN delivers superior flame-retardant efficiency and interfacial protection, yet suffers from high cost, limited solubility, and compromised electrochemical performance at high dosages, with P–F/P–O–C bond cleavage-induced gas evolution as its main failure mode. Increasing PFPN content generally improves flame-retardant performance yet impairs battery electrochemical properties; moreover, the cleavage of P–F or P–O–C bonds under harsh conditions generates gaseous by-products. Machine learning models trained on molecular descriptors, including HOMO/LUMO energy levels, bond dissociation energy, solvation free energy, oxidation/reduction potential, viscosity, conductivity, SET, COI and gas generation data, can accelerate the screening of next-generation phosphazene derivatives with balanced performance. (iv) PFPN-containing electrolytes should be validated in practical full cells. Most current studies remain based on coin cells, where heat dissipation and gas accumulation differ from commercial batteries. Future studies should evaluate Ah-level pouch, cylindrical, and prismatic cells under high-voltage cycling, elevated temperature storage, overcharge, nail penetration, and accelerating rate calorimetry conditions (Fig. 10).
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