In situ growth of redox-active covalent organic frameworks on aminated MXene for functional separator coatings in lithium-sulfur batteries

Kehan Tang Peiwen Xu Xinyuan Wu Youlong Zhu

Citation:  Kehan Tang, Peiwen Xu, Xinyuan Wu, Youlong Zhu. In situ growth of redox-active covalent organic frameworks on aminated MXene for functional separator coatings in lithium-sulfur batteries[J]. Chinese Chemical Letters, 2026, 37(8): 111883. doi: 10.1016/j.cclet.2025.111883 shu

In situ growth of redox-active covalent organic frameworks on aminated MXene for functional separator coatings in lithium-sulfur batteries

English

  • As one of the most promising next-generation high-energy-density battery technologies, lithium-sulfur (Li-S) batteries possess high theoretical capacity (1675 mAh/g) and energy density (2600 Wh/kg) as well as abundant natural sulfur element [15]. However, several critical challenges hinder their practical application, particularly in terms of capacity retention and cycle life. These issues include the notorious lithium polysulfides (LiPSs) shuttle effect, the inherently low electrical conductivity of sulfur, and sluggish redox kinetics of sulfur species [6,7]. On the cathode side, the complicated multiphase reactions and high energy barrier associated with the liquid-solid phase conversion significantly slow down the sulfur redox kinetics [810]. Meanwhile, the current commercial polyolefin separators with random and broad pore size distributions are unable to suppress the shuttle effect of soluble LiPSs during the charge-discharge process [1114], resulting in rapid capacity decay of the battery. On the anode side, lithium metal is prone to dendritic growth caused by uneven lithium deposition, which can lead to internal short circuits and, in severe cases, combustion or explosion [1,15]. To address these issues, considerable efforts have been devoted to modify the commercial polyolefin separators to improve their electrochemical performance and suppress the shuttle effect.

    Introducing functional coatings on the cathode-facing side of the separator in Li-S batteries has emerged as an effective strategy to suppress the shuttle effect of LiPSs [1620]. Conductive carbon-based materials, such as carbon nanotubes, graphene, and porous carbon aerogels, have been widely explored owing to their high conductivity and large specific surface area [21,22]. However, they generally exhibit limited catalytic activity toward sulfur redox reactions because of limited functional moieties, which hampers their ability to accelerate the sulfur oxidation–reduction kinetics [23]. Transition metal-based compounds with inherent electrocatalytic activity have been incorporated into the functional coatings [24,25], including transition metal oxides (TMOs) [26,27], transition metal phosphides (TMPs) [28], transition metal nitrides (TMNs) [29], transition metal carbides (TMCs) [3032], transition metal sulfides (TMSs) [33,34], transition metal compounds-based hybrids [3537], metal-organic frameworks (MOFs) [3840], and single atom catalysts [4143]. These catalysts were typically combined with high specific surface area materials to provide abundant active sites for anchoring and catalyzing the conversion of LiPSs, thereby accelerating the kinetics of sulfur redox process [44,45]. However, due to the lack of lithiophilic sites, many of these materials struggle to facilitate uniform lithium ion transport, which is crucial for suppressing lithium dendrite growth [46]. Covalent organic framework (COFs), composed of lightweight elements and featuring tunable structures, high specific surface area, and excellent chemical/thermo stability [47,48]. Their unique pore structure and multiple functional groups allow for the electrostatic adsorption or repulsion of polysulfides, effectively mitigating the shuttle effect [4955]. Furthermore, COF-based functional coatings can serve as lithium-ion transport channels enriched with lithiophilic groups, enabling more uniform ion distribution [5660]. Nevertheless, the inherent poor conductivity of COFs limits their utilization efficiency for active polysulfides [61]. Therefore, the development of multifunctional COF-based composite coatings that combine good electrical conductivity, high catalytic activity, large surface area, and abundant lithiophilic sites is key to achieving high specific capacity, enhanced safety, and long cycle life in advanced Li-S batteries.

    Herein, we report the synthesis of a COF/MXene hybrid material (denoted as DAAQ-TFP/MXene), constructed by in situ growth of an anthraquinone-based COF (DAAQ-TFP) on amine-modified transition metal carbides (MXene). This hybrid was subsequently employed as a functional coating to decorate commercial polypropylene (PP) separators, yielding DAAQ-TFP/MXene@PP, which was then applied in Li-S batteries. In this functional separator, the active metal sites of MXene and the redox-active anthraquinone units in DAAQ-TFP serve as dual anchors, synergistically catalyzing the redox conversion of LiPSs. The covalent linkage between MXene and the DAAQ-TFP enhances the conductivity of the hybrid material. Meanwhile, the microporous structure of DAAQ-TFP promotes effective physical adsorption of LiPSs, thereby mitigating the shuttle effect and enabling synergistic adsorption-catalysis performance. Additionally, the ordered pore channels and abundant lithiophilic sites in the DAAQ-TFP COF, such as carbonyl groups, β-ketoamine linkages, and anthraquinone moieties, can facilitate uniform and efficient lithium-ion transport. As a result, Li-S batteries assembled with DAAQ-TFP/MXene@PP separators exhibited a high specific capacity of 1224 mAh/g at 0.1 C, excellent rate performance (631 mAh/g at 5 C), and outstanding long-term cycling stability. Moreover, Li/Li symmetric cells using the same modified separator demonstrated stable cycling for over 3800 h at a current density of 5 mA/cm2 and an areal capacity of 1 mAh/cm2. This study offers a new approach for developing functional separator coatings toward high-performance Li-S batteries.

    DAAQ-TFP/MXene was synthesized via an in situ growth strategy, as illustrated in Scheme 1. First, amine-modified MXene nanosheets (MXene-NH2) were prepared by reacting diazonium salt with MXene. Subsequently, a Schiff-base reaction between triformylphloroglucinol (TFP) and 2, 6-diaminoanthraquinone (DAAQ) in the presence of MXene-NH₂ led to the in situ growth of the anthraquinone-based COF (DAAQ-TFP) on the MXene-NH2 surface. Prior to the reaction, MXene-NH2 exhibited a typical two-dimensional sheet-like morphology with a smooth and flat surface (Fig. 1a). After polymerization, SEM images revealed the presence of distinct COF nanoparticles uniformly distributed on the surface of MXene nanosheets (Figs. 1b and c). The chemical and crystalline structures of the resulting DAAQ-TFP/MXene hybrid were further characterized by Fourier transform infrared spectroscopy (FT-IR) and powder X-ray diffraction (PXRD). As shown in Fig. 1d, the FT-IR of DAAQ monomer displays N—H stretching vibration peaks at 3332 and 3421 cm-1. After the polymerization, the intensity of N—H peaks significantly decreased, and a characteristic C—N stretching peak appeared at 1255 cm-1, corresponding to the formation of β-ketoamine linkages from the condensation reaction between aldehyde and amine groups followed by the tautomerization. These changes confirm the successful polymerization between TFP and DAAQ. Additionally, PXRD analysis confirmed that the crystalline structure of the DAAQ-TFP COF was preserved in the DAAQ-TFP/MXene hybrid, the diffraction peaks are consistent with the literature reported (Fig. S1 in Supporting information) [62]. These results collectively demonstrate the successful in situ growth of DAAQ-TFP on MXene-NH2. Nitrogen adsorption–desorption measurements (Fig. 1e) was carried out to study their porosities, both materials exhibited typical combination of type Ⅰ and type Ⅳ isotherms. The BET surface area of DAAQ-TFP/MXene is calculated to be 761.4 m2/g, which is lower than that of pristine DAAQ-TFP (1154.3 m2/g) due to the incorporation of nearly nonporous MXene-NH2. Non local density functional theory (NLDFT) pore size analysis indicated that both materials possess similar hierarchical porosity, with dominant pore sizes centered at approximately 1.9 and 4.8 nm (Fig. 1f). This combination of micropores and mesopores is beneficial for PSs adsorption, suppression of the shuttle effect, and improved ion transport.

    Scheme 1

    Scheme 1.  (a) Schematic illustration of the in situ growth of DAAQ-TFP on MXene-NH2 to prepare DAAQ-TFP/MXene hybrid. Comparison of the polysulfide shuttle effect and lithium-ion transport during the discharge/charge process in Li-S batteries using separators with (b) non-catalytic functional coatings and (c) the DAAQ-TFP/MXene hybrid materials.

    Figure 1

    Figure 1.  (a) SEM image of MXene. (b, c) The SEM images of DAAQ-TFP/MXene at different magnifications. (d) FT-IR spectra of DAAQ-TFP/MXene, TFP, and DAAQ. (e) N2 adsorption-desorption isotherms of DAAQ-TFP and DAAQ-TFP/MXene measured at 77 K. (f) Pore size distribution curves of DAAQ-TFP and DAAQ-TFP/MXene.

    The DAAQ-TFP/MXene hybrid, DAAQ-TFP, and MXene materials were individually mixed with carbon black and binder in N-methyl-2-pyrrolidone (NMP). After thorough grinding, the resulting slurries were uniformly coated onto PP membranes via a simple blade-coating process to prepare functional separators, denoted as DAAQ-TFP/MXene@PP, DAAQ-TFP@PP, and MXene@PP, respectively. A digital photograph of the DAAQ-TFP/MXene@PP separator was presented in Fig. 2a. The thickness of the DAAQ-TFP/MXene in the composite separator is about 3 µm (Fig. 2b). SEM images revealed that the top surface of DAAQ-TFP/MXene@PP exhibited a dense and continuous layer formed by DAAQ-TFP/MXene (Fig. 2c), while the uncoated bottom side maintained the original porous morphology of the pristine PP membrane (Fig. 2d). The electrolyte affinity of the modified and unmodified separators was evaluated via optical contact angle measurements. Benefiting from the abundant polar functional groups in the DAAQ-TFP and the metal sites introduced by the MXene nanosheets, the DAAQ-TFP/MXene@PP separator demonstrated excellent wettability with the Li-S electrolyte. As shown in Fig. 2e, the contact angle of DAAQ-TFP/MXene@PP was only 13°, significantly lower than that of the pristine PP membrane (24°, Fig. 2f). Enhanced electrolyte affinity is critical for lowering internal resistance and promoting efficient ion transport within the battery.

    Figure 2

    Figure 2.  (a) Digital photograph and (b) cross-sectional SEM image of the DAAQ-TFP/MXene@PP separator. (c) Top-view and (d) bottom-view SEM images of the DAAQ-TFP/MXene@PP separator. Contact angle measurement of (e) the DAAQ-TFP/MXene@PP and (f) pristine PP separator.

    The lithium-ion transference number ( t Li + ) is a critical parameter for evaluating the lithium-ion transport efficiency of modified separators. Li/Li symmetric cells were assembled using both DAAQ-TFP/MXene@PP and pristine PP membranes. The t Li + value of the DAAQ-TFP/MXene@PP separator was determined to be 0.53, which is significantly higher than that of the unmodified PP membrane with only 0.37 (Figs. 3a and b). This enhancement can be attributed to the high porosity of DAAQ-TFP/MXene hybrid and the presence of abundant lithium-affinitive functional groups in DAAQ-TFP, which collectively provide rapid ion-conduction pathways and improve lithium-ion transport efficiency. Furthermore, constant current charge-discharge experiments were conducted on Li/Li symmetric cells assembled with DAAQ-TFP/MXene@PP and PP membrane under a current density of 5 mA/cm2 and an areal capacity of 1 mAh/cm2 to investigate the stability of lithium metal deposition/stripping. The Li/Li symmetric cells based on DAAQ-TFP/MXene@PP exhibited stable lithium deposition/stripping behavior and lower overpotential, achieving continuous cycling for 3800 h under these conditions (Figs. 3c and d). In contrast, cells based on the pristine PP membrane displayed a much higher overpotential and a significantly shorter cycling lifespan, underscoring the superior lithium-ion transport capability of the functionalized separator.

    Figure 3

    Figure 3.  Chronoamperometry profiles of Li/Li symmetric cells using (a) DAAQ-TFP/MXene@PP and (b) pristine PP separators under a polarization voltage of 10 mV (insets: corresponding impedance spectra before and after polarization). (c) Voltage-time profile of Li/Li symmetric cells with DAAQ-TFP/MXene@PP and pristine PP separators at a current density of 5 mA/cm2 and an areal capacity of 1 mAh/cm2. (d) Enlarged voltage-time profile of Li/Li symmetric cell with DAAQ-TFP/MXene@PP separator during the cycling interval from 3070 h to 3074 h.

    To demonstrate the superior electrochemical performance of DAAQ-TFP/MXene@PP separator in Li-S batteries, a series of Li-S cells were assembled using DAAQ-TFP/MXene@PP, DAAQ-TFP@PP, MXene@PP, and pristine PP membranes, with the modified coatings facing the sulfur cathode. Cyclic voltammetry (CV) curves were tested at a scan rate of 0.1 mV/s within the voltage range of 1.7–2.8 V (Fig. 4a). Among the four configurations, the Li-S battery employing the DAAQ-TFP/MXene@PP separator exhibited the highest peak currents, along with a noticeable positive shift in the reduction peak and a negative shift in the oxidation peak. The CV curves of symmetric cells using DAAQ-TFP/MXene@PP separator exhibited the largest redox peak current and smallest polarization voltage among Li-S symmetric cells with DAAQ-TFP@PP or pristine PP separators (Fig. S3 in Supporting information). Furthermore, Tafel analysis was performed to evaluate their catalytic behavior. The exchange current density (Io) derived from the Tafel plot fitting revealed that the Li-S battery with the DAAQ-TFP/MXene@PP separator achieved the highest Io value of 0.381 mA/cm2, surpassing those of the DAAQ-TFP@PP-based (0.371 mA/cm2) and pristine PP-based (0.311 mA/cm2) Li-S battery at a scan rate 50 mV/s (Fig. S4 in Supporting information). These results indicate accelerated redox kinetics, reduced polarization, and enhanced catalytic activity toward polysulfide conversion. Furthermore, electrochemical impedance spectroscopy (EIS) was performed at the open-circuit voltage, and the equivalent circuit diagram was also provided to evaluate charge transfer resistance (Fig. 4b). The corresponding fitted impedance parameters are summarized in Table S1 (Supporting information). The Nyquist plots consist of the electrolyte/electrode interface resistance (RS), charge transfer resistance (RCT), and Warburg impedance (WO) [63,64]. All Li-S batteries with different separators exhibited small RS values, indicating their good electrolyte/electrode compatibility. Compared to the pristine PP separator, all modified separators showed reduced RCT values. Notably, the DAAQ-TFP/MXene@PP-based cell displayed the lowest RCT, underscoring the synergistic effect of DAAQ-TFP and MXene in promoting efficient charge transfer and ion diffusion across the separator, which also suppressing the PSs shuttling.

    Figure 4

    Figure 4.  (a) Cyclic voltammetry curves and (b) Nyquist plots of the Li-S batteries using DAAQ-TFP/MXene@PP, DAAQ-TFP@PP, MXene@PP, and pristine PP separators. (c) Galvanostatic charge-discharge profiles of Li-S batteries with DAAQ-TFP/MXene@PP separator at various current densities. (d) Rate performance and (e) cycling performance at 1 C of Li-S batteries using DAAQ-TFP/MXene@PP, DAAQ-TFP@PP, MXene@PP, and pristine PP separators.

    The rate performance of Li-S batteries assembled with DAAQ-TFP/MXene@PP, DAAQ-TFP@PP, MXene@PP, and pristine PP separators was evaluated at under various current densities. All batteries exhibited typical charge/discharge profiles with one charging plateau and two distinct discharge plateaus, corresponding to the stepwise oxidation of Li2S2/Li2S to S8 and the stepwise reduction of S8 to Li2S2/Li2S (Fig. 4c and Fig. S5 in Supporting information). At 0.2 C, the charge/discharge profiles (Fig. S6 in Supporting information) reveal that the DAAQ-TFP/MXene@PP-based cell exhibited and a lower polarization voltage (254.7 mV) compared to the cells with DAAQ-TFP@PP (258.6 mV), MXene@PP (261.9 mV), or PP (268.7 mV) separators, indicating the fast reaction kinetics of DAAQ-TFP/MXene@PP-based Li-S battery. Additionally, DAAQ-TFP/MXene@PP-based cell exhibited a longer discharge plateau compared to cells with other separator, the discharge curves can be divided into high discharge plateaus (QH) and low discharge plateaus (QL), which are corresponding to the conversions of S8 to long-chain LiPSs and LiPSs to Li2S2/Li2S, respectively [65]. The DAAQ-TFP/MXene@PP-based cell delivers a markedly higher QH capacity than the other separator-based batteries (Fig. S7 in Supporting information), suggesting an accelerated transformation of S8 to PSs. Since S8 is often encapsulated by Li2S2/Li2S during discharge-limiting sulfur utilization-the high QH capacity further confirms that Li2S2 is efficiently converted back to S8, catalyzed by the DAAQ-TFP/MXene@PP layer. Among the four Li-S batteries, the DAAQ-TFP/MXene@PP-based Li-S battery consistently achieves the highest specific capacities across all tested current rates, demonstrating its superior rate performance (Fig. 4d). Specifically, the DAAQ-TFP/MXene@PP-based Li-S battery achieved reversible capacities of 1224, 1058, 925, 834, 744, 691 and 631 mAh/g at 0.1, 0.2, 0.5, 1, 2, 3, and 5 C, respectively. When the current was restored to 1 C, the capacity recovered to 819 mAh/g, indicating excellent structure stability and rate reversibility. To further evaluate the long-term cycling performance, Li-S batteries with the four different separators were tested at 1 C for 300 cycles (Fig. 4e). The Li-S battery employing the DAAQ-TFP/MXene@PP separator delivered an initial discharge capacity of 985 mAh/g and the capacity retention rate was 71.3% after 300 cycles, with an average capacity decay rate of only 0.096% per cycle. In contrast, the Li-S battery assembled with pristine PP membrane exhibited a lower initial discharge specific capacity of 768.3 mAh/g and a capacity retention rate of only 63.2% after 300 cycles, corresponding to a higher average decay rate of 0.12% per cycle. These results confirm that the DAAQ-TFP/MXene@PP separator imparts excellent rate performance and cycling stability to Li-S batteries. This can be attributed to its synergistic adsorption-catalysis properties, stemming from the combination of a porous COF and dual catalytic sites. Additionally, the mesoporous structure and interconnected channels formed by stacked nanosheets of MXene facilitate rapid lithium-ion diffusion, further enhancing electrochemical performance.

    To further validate the adsorption-catalysis performance and highlight the advantages of the DAAQ-TFP/MXene hybrid material, LiPSs adsorption experiments (Li2S6 was used as model PSs) were conducted to compare the adsorption kinetics of different samples. Specifically, 10 mg of each sample was added to 3 mL of 5 mmol/L Li2S6 solution and allowed to stand for 24 h (Figs. S8a-d in Supporting information). Upon addition of MXene or DAAQ-TFP, the solution color changed from the original yellow-brown to a darker brown, indicating partial Li2S6 adsorption. Notably, the solution containing the DAAQ-TFP/MXene hybrid underwent significant decolorization, suggesting its superior adsorption capability. Subsequently, the supernatants were analyzed using UV–visible spectroscopy (Fig. S8e in Supporting information). Compared to the characteristic Li2S6 absorbance peak at ~412 nm observed in the blank solution, all samples showed reduced peak intensities, with varying degrees of attenuation. The DAAQ-TFP sample exhibited a notably lower absorbance than MXene, attributable to its high porosity and strong interactions between anthraquinone moieties and Li2S6. Remarkably, the Li2S6 solution treated with the DAAQ-TFP/MXene hybrid showed an almost complete disappearance of the absorption peak, underscoring the synergistic effect of dual catalytic sites and the porous structure in enhancing adsorption-catalysis performance.

    In summary, a redox-active covalent organic framework/MXene hybrid (DAAQ-TFP/MXene) was successfully synthesized via an in situ growth strategy. The resulting DAAQ-TFP/MXene was subsequently coated onto a commercial PP membrane to fabricate a functional separator, denoted as DAAQ-TFP/MXene@PP. The porous structure of DAAQ-TFP enables effective adsorption of LiPSs, while the metal-active sites of MXene and the anthraquinone moieties within DAAQ-TFP synergistically catalyze LiPSs conversion, thereby enhancing sulfur redox kinetics. In addition, the abundant polar functional groups in DAAQ-TFP, along with the pore channels formed by the stacking of MXene nanosheets, facilitate efficient lithium-ion transport. As a result, the DAAQ-TFP/MXene@PP modified separator can simultaneously suppress shuttle effects of LiPSs and promote uniform lithium deposition and stripping. Li||Li symmetric cells assembled with this modified separator can stably cycle for 3800 h under conditions of 5 mA/cm2 and 1 mAh/cm2. Moreover, Li-S full batteries employing DAAQ-TFP/MXene@PP separator demonstrate a high specific capacity of 1224 mAh/g at 0.1 C, excellent rate capability (631 mAh/g at 5 C), and outstanding cycling performance with a capacity retention of 71.3% after 300 cycles at 1 C. This work presents a facile and effective strategy for constructing COF/MXene hybrids as functional separator coatings, offering a promising route toward high-performance Li-S batteries.

    The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

    Kehan Tang: Writing – original draft, Methodology, Investigation, Formal analysis, Data curation. Peiwen Xu: Methodology, Investigation, Formal analysis, Data curation. Xinyuan Wu: Formal analysis, Data curation. Youlong Zhu: Writing – review & editing, Investigation, Funding acquisition, Conceptualization.

    This work is financial supported by the projects of National Natural Science Foundation of China (No. 52103328), Guangzhou Science and Technology Programme (No. 2024A04J9960), and Guangdong Basic Research Center of Excellence for Functional Molecular Engineering.

    Supplementary material associated with this article can be found, in the online version, at doi:10.1016/j.cclet.2025.111883.


    1. [1]

      Q. Cheng, Z.X. Chen, X.Y. Li, et al., Adv. Energy Mater. 13 (2023) 2301770. doi: 10.1002/aenm.202301770

    2. [2]

      Y. Mo, L. Liao, D. Li, et al., Chin. Chem. Lett. 34 (2023) 107130. doi: 10.1016/j.cclet.2022.01.023

    3. [3]

      H. Pan, Z. Cheng, Z. Zhou, et al., Nano-Micro Lett. 15 (2023) 165. doi: 10.1007/s40820-023-01137-y

    4. [4]

      Y. Fei, G. Li, Adv. Funct. Mater. 34 (2024) 2312550. doi: 10.1002/adfm.202312550

    5. [5]

      S.C. Kim, X. Gao, S.L. Liao, et al., Nat. Commun. 15 (2024) 1268. doi: 10.1038/s41558-024-02171-3

    6. [6]

      X.Y. Li, S. Feng, M. Zhao, et al., Angew. Chem. Int. Ed. 134 (2022) e202114671. doi: 10.1002/ange.202114671

    7. [7]

      J. Li, L. Gao, F. Pan, et al., Nano-Micro Lett. 16 (2024) 12. doi: 10.1007/s40820-023-01223-1

    8. [8]

      R. Liu, Z. Wei, L. Peng, et al., Nature 626 (2024) 98–104. doi: 10.1038/s41586-023-06918-4

    9. [9]

      Z. Wang, Y. Li, H. Ji, et al., Adv. Mater. 34 (2022) 2203699. doi: 10.1002/adma.202203699

    10. [10]

      W. Yao, K. Liao, T. Lai, H. Sul, A. Manthiram, Chem. Rev. 124 (2024) 4935–5118. doi: 10.1021/acs.chemrev.3c00919

    11. [11]

      L. Wang, W. Hua, X. Wan, et al., Adv. Mater. 34 (2022) 2110279. doi: 10.1002/adma.202110279

    12. [12]

      L. Wang, Z. Hu, X. Wan, et al., Adv. Energy Mater. 12 (2022) 2200340. doi: 10.1002/aenm.202200340

    13. [13]

      X. Gao, Z. Yu, J. Wang, et al., Proc. Natl. Acad. Sci. U. S. A. 120 (2023) e2301260120. doi: 10.1073/pnas.2301260120

    14. [14]

      T. Wang, J. He, Z. Zhu, et al., Adv. Mater. 35 (2023) 2303520. doi: 10.1002/adma.202303520

    15. [15]

      R. Gao, M. Zhang, Z. Han, et al., Adv. Mater. 36 (2024) 2303610. doi: 10.1002/adma.202303610

    16. [16]

      Z. Zhao, Y. Pan, H. Chen, et al., Adv. Funct. Mater. 34 (2024) 2402182. doi: 10.1002/adfm.202402182

    17. [17]

      W. Jin, Y. Guo, T. Gan, et al., Angew. Chem. Int. Ed. 64 (2025) e202420544. doi: 10.1002/anie.202420544

    18. [18]

      Y. Wang, X. Yang, P. Li, et al., Macromol. Rapid Commun. 44 (2023) 2200760. doi: 10.1002/marc.202200760

    19. [19]

      M.K. Aslam, S. Jamil, S. Hussain, M. Xu, Energy Environ. Mater. 6 (2023) e12420. doi: 10.1002/eem2.12420

    20. [20]

      A. Kim, S.H. Oh, A. Adhikari, et al., J. Mater. Chem. A 11 (2023) 7833–7866. doi: 10.1039/d2ta09266b

    21. [21]

      J. Huang, K. Leng, Z. Cen, et al., Sci. China Mater. 66 (2023) 1747–1756. doi: 10.1007/s40843-022-2303-0

    22. [22]

      T. Wang, K. Kretschmer, S. Choi, et al., Small Methods 1 (2017) 1700089. doi: 10.1002/smtd.201700089

    23. [23]

      J. Qin, R. Wang, P. Xiao, D. Wang, Adv. Energy Mater. 13 (2023) 2300611. doi: 10.1002/aenm.202300611

    24. [24]

      Q. Liang, S. Wang, Y. Yao, P. Dong, H. Song, Adv. Funct. Mater. 33 (2023) 2300825. doi: 10.1002/adfm.202300825

    25. [25]

      C. Shi, J. Huang, Y. Tang, et al., Carbon. 202 (2023) 59–65. doi: 10.1016/j.carbon.2022.09.086

    26. [26]

      X. Liang, C.Y. Kwok, F. Lodi-Marzano, et al., Adv. Energy Mater. 6 (2016) 1501636. doi: 10.1002/aenm.2015016361

    27. [27]

      Z. Ma, Z. Qi, G. Song, et al., Adv. Funct. Mater. 34 (2024) 2403101. doi: 10.1002/adfm.202403101

    28. [28]

      S. Huang, E. Huixiang, Y. Yang, et al., J. Mater. Chem. A 9 (2021) 7458–7480. doi: 10.1039/d0ta11919a

    29. [29]

      S. Gu, H. Jiang, X. Li, et al., Energy Storage Mater. 53 (2022) 32–41. doi: 10.1016/j.ensm.2022.08.048

    30. [30]

      J.L. Cheong, C. Hu, W. Liu, et al., Nano Energy 102 (2022) 107659. doi: 10.1016/j.nanoen.2022.107659

    31. [31]

      M. Zhao, P. Tan, D. Cai, et al., Adv. Funct. Mater. 33 (2023) 2211505. doi: 10.1002/adfm.202211505

    32. [32]

      Z.U. Rehman, K. Khan, S. Yao, et al., Mater. Today Chem. 40 (2024) 102200. doi: 10.1016/j.mtchem.2024.102200

    33. [33]

      B. Yan, X. Li, W. Xiao, et al., J. Mater. Chem. A 8 (2020) 17848–17882. doi: 10.1039/d0ta06220k

    34. [34]

      S. Tian, G. Liu, S. Xu, et al., Adv. Funct. Mater. 34 (2024) 2309437. doi: 10.1002/adfm.202309437

    35. [35]

      R. Wang, C. Ma, C. Li, et al., J. Energy Storage 109 (2025) 115168. doi: 10.1016/j.est.2024.115168

    36. [36]

      Y. Chen, C. Ma, Z. Li, et al., Electrochim. Acta 517 (2025) 145762. doi: 10.1016/j.electacta.2025.145762

    37. [37]

      D. Li, H. Sun, C. Ma, et al., J. Energy Storage. 113 (2025) 115698. doi: 10.1016/j.est.2025.115698

    38. [38]

      F. Qi, Z. Sun, X. Fan, et al., Adv. Energy Mater. 11 (2021) 2100387. doi: 10.1002/aenm.202100387

    39. [39]

      R. Razaq, M.M.U. Din, D.R. Småbråten, et al., Adv. Energy Mater. 14 (2024) 2302897. doi: 10.1002/aenm.202302897

    40. [40]

      P. Feng, W. Hou, Z. Bai, et al., Chin. Chem. Lett. 34 (2023) 107427. doi: 10.1016/j.cclet.2022.04.025

    41. [41]

      X. Zhang, T. Yang, Y. Zhang, et al., Adv. Mater. 35 (2023) 2208470. doi: 10.1002/adma.202208470

    42. [42]

      C. Zhou, M. Li, N. Hu, et al., Adv. Funct. Mater. 32 (2022) 2204635. doi: 10.1002/adfm.202204635

    43. [43]

      Y. Miao, Y. Zheng, F. Tao, et al., Chin. Chem. Lett. 34 (2023) 107121. doi: 10.1016/j.cclet.2022.01.014

    44. [44]

      J. Wu, T. Ye, Y. Wang, et al., ACS Nano 16 (2022) 15734–15759. doi: 10.1021/acsnano.2c08581

    45. [45]

      B. Liu, H. Gu, J.F. Torres, Z. Yin, A. Tricoli, Energy Environ. Sci. 17 (2024) 1073–1082. doi: 10.1039/d3ee03700b

    46. [46]

      W. Yao, J. Xu, L. Ma, et al., Adv. Mater. 35 (2023) 2212116. doi: 10.1002/adma.202212116

    47. [47]

      S. Haldar, A. Schneemann, S. Kaskel, J. Am. Chem. Soc. 145 (2023) 13494–13513. doi: 10.1021/jacs.3c01131

    48. [48]

      Y.L. Zhu, Q.S. Bai, S. Ouyang, Y.H. Jin, W. Zhang, ChemSusChem. 17 (2024) e202301118. doi: 10.1002/cssc.202301118

    49. [49]

      Q. An, L. Wang, G. Zhao, et al., Adv. Mater. 36 (2024) 2305818. doi: 10.1002/adma.202305818

    50. [50]

      P. Li, H. Lv, Z. Li, et al., Adv. Mater. 33 (2021) 2007803. doi: 10.1002/adma.202007803

    51. [51]

      Z. Cheng, H. Pan, H. Zhong, et al., Adv. Funct. Mater. 28 (2018) 1707597. doi: 10.1002/adfm.201707597

    52. [52]

      D. Luo, M. Li, Q. Ma, et al., Chem. Soc. Rev. 51 (2022) 2917–2938. doi: 10.1039/d1cs01014j

    53. [53]

      X. Kang, T. He, R. Zou, et al., Small. 20 (2024) 2306503. doi: 10.1002/smll.202306503

    54. [54]

      X. Liu, X.R. Sun, R. Yan, et al., Adv. Funct. Mater. 35 (2025) 2505986. doi: 10.1002/adfm.202505986

    55. [55]

      X. Chen, H. Jiang, J.H. Liu, et al., Adv. Funct. Mater. 35 (2025) 2421697. doi: 10.1002/adfm.202421697319355

    56. [56]

      X. Wu, S. Zhang, X. Xu, et al., Angew. Chem. Int. Ed. 136 (2024) e202319355. doi: 10.1002/anie.202319355

    57. [57]

      J. Xu, S. An, X. Song, et al., Adv. Mater. 33 (2021) 2105178. doi: 10.1002/adma.202105178

    58. [58]

      G. Yu, Y. Cui, S. Lin, et al., Adv. Funct. Mater. 34 (2024) 2314935. doi: 10.1002/adfm.202314935

    59. [59]

      J. Duan, K. Wang, L. Teng, et al., ACS Nano 18 (2024) 29189–29202. doi: 10.1021/acsnano.4c11262

    60. [60]

      S. Gullace, M. Abruzzese, L. Cusin, et al., J. Mater. Chem. A 12 (2024) 25359–25370. doi: 10.1039/d4ta03930k

    61. [61]

      B. Hu, J. Xu, Z. Fan, et al., Adv. Energy Mater. 13 (2023) 2203540. doi: 10.1002/aenm.202203540

    62. [62]

      C.R. DeBlase, K.E. Silberstein, T.T. Truong, H.D. Abruna, W.R. Dichtel, J. Am. Chem. Soc. 135 (2013) 16821–16824. doi: 10.1021/ja409421d

    63. [63]

      C. Zhang, C. Ma, W. Zhang, et al., Chem. Eng. J. 481 (2024) 148374. doi: 10.1016/j.cej.2023.148374

    64. [64]

      S. Yao, H. Liu, C. Zhang, et al., J. Energy Storage. 78 (2024) 110087. doi: 10.1016/j.est.2023.110087

    65. [65]

      Y. Song, Y. Sun, L. Chen, et al., Adv. Funct. Mater. 34 (2024) 2409748. doi: 10.1002/adfm.202409748

  • Scheme 1  (a) Schematic illustration of the in situ growth of DAAQ-TFP on MXene-NH2 to prepare DAAQ-TFP/MXene hybrid. Comparison of the polysulfide shuttle effect and lithium-ion transport during the discharge/charge process in Li-S batteries using separators with (b) non-catalytic functional coatings and (c) the DAAQ-TFP/MXene hybrid materials.

    Figure 1  (a) SEM image of MXene. (b, c) The SEM images of DAAQ-TFP/MXene at different magnifications. (d) FT-IR spectra of DAAQ-TFP/MXene, TFP, and DAAQ. (e) N2 adsorption-desorption isotherms of DAAQ-TFP and DAAQ-TFP/MXene measured at 77 K. (f) Pore size distribution curves of DAAQ-TFP and DAAQ-TFP/MXene.

    Figure 2  (a) Digital photograph and (b) cross-sectional SEM image of the DAAQ-TFP/MXene@PP separator. (c) Top-view and (d) bottom-view SEM images of the DAAQ-TFP/MXene@PP separator. Contact angle measurement of (e) the DAAQ-TFP/MXene@PP and (f) pristine PP separator.

    Figure 3  Chronoamperometry profiles of Li/Li symmetric cells using (a) DAAQ-TFP/MXene@PP and (b) pristine PP separators under a polarization voltage of 10 mV (insets: corresponding impedance spectra before and after polarization). (c) Voltage-time profile of Li/Li symmetric cells with DAAQ-TFP/MXene@PP and pristine PP separators at a current density of 5 mA/cm2 and an areal capacity of 1 mAh/cm2. (d) Enlarged voltage-time profile of Li/Li symmetric cell with DAAQ-TFP/MXene@PP separator during the cycling interval from 3070 h to 3074 h.

    Figure 4  (a) Cyclic voltammetry curves and (b) Nyquist plots of the Li-S batteries using DAAQ-TFP/MXene@PP, DAAQ-TFP@PP, MXene@PP, and pristine PP separators. (c) Galvanostatic charge-discharge profiles of Li-S batteries with DAAQ-TFP/MXene@PP separator at various current densities. (d) Rate performance and (e) cycling performance at 1 C of Li-S batteries using DAAQ-TFP/MXene@PP, DAAQ-TFP@PP, MXene@PP, and pristine PP separators.

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  • 发布日期:  2026-08-15
  • 收稿日期:  2025-07-25
  • 接受日期:  2025-09-23
  • 修回日期:  2025-09-16
  • 网络出版日期:  2025-09-23
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