Open Access Article
Yunyang Wu
*
College of Polymer Science and Engineering, Sichuan University, Chengdu 610040, China. E-mail: wuyunyang@stu.scu.edu.cn
First published on 19th March 2026
Oxygen reduction reaction (ORR) and oxygen evolution reaction (OER) are critical half-reactions in energy conversion devices such as metal–air batteries and reversible fuel cells, and their sluggish kinetics severely limit the overall device performance. Therefore, the development of efficient, stable, and low-cost non-precious metal bifunctional electrocatalysts is of great significance. In this study, a MOF-derived bifunctional electrocatalytic material (NiFe@CNT), featuring NiFe bimetallic alloys uniformly anchored within a carbon nanotube network, was successfully fabricated using a two-dimensional metalloporphyrin-based Fe-MOF precursor via metal site modulation by introducing Ni, combined with a high-temperature pyrolysis strategy. Structural characterization results indicate that NiFe@CNT possesses an intact three-dimensional CNT conductive network, a high degree of graphitization (ID/IG = 0.39), and uniformly dispersed NiFe alloy active phases. Electrochemical evaluations reveal that NiFe@CNT functions as a highly active bifunctional catalyst for both ORR and OER in alkaline environments. Regarding its ORR activity, the material exhibits a half-wave potential comparable to that of benchmark Pt/C, with reaction kinetics proceeding through an approximately four-electron transfer mechanism. In terms of OER performance, a current density of 10 mA cm−2 is attained at a modest overpotential of merely 1.514 V. In alkaline electrolyte, the ORR proceeds predominantly through a four-electron pathway converting O2 to H2O (O2 + 4H+ + 4e− → 2H2O), while the OER involves the reverse four-electron oxidation of hydroxide to produce molecular oxygen (2H2O → O2 + 4H+ + 4e−). Furthermore, durability assessments confirm that NiFe@CNT surpasses commercial noble metal benchmarks in long-term operational stability. This work presents a viable approach for fabricating advanced noble-metal-free oxygen electrocatalysts through two-dimensional MOF-derived engineering.
In recent years, catalysts derived from metal–organic frameworks (MOFs) have attracted considerable attention in ORR/OER electrocatalysis owing to their tunable structures, large specific surface areas, and unique capability to construct high-density, atomically dispersed metal active sites.11–13 For instance, Li et al. reported a Fe–N–C/rGO catalyst containing FeN5 atomic sites, synthesized via the pyrolysis of graphene oxide and ZIF-8. The asymmetric electron-deficient region located above the metal center of the FeN5 site was shown to effectively modulate the adsorption energies of reaction intermediates, thereby markedly lowering the reaction energy barriers for both ORR and OER and enhancing the overall catalytic activity. This work convincingly demonstrated the substantial potential of MOF-derived materials for the rational design of high-performance bifunctional catalysts.14,15 Among various metal-based MOFs, iron-based metal–organic frameworks (Fe-MOFs) have received particular attention due to their favorable physicochemical properties and the natural abundance of iron resources.16–19 Chang et al. developed a Fe3C/Fe–N–C catalyst via a Fe single-atom seed-mediated strategy, which exhibited outstanding bifunctional ORR/OER activity. Notably, this catalyst delivered a lower ΔE value during ORR/OER operation than Pt/C + RuO2 and other reference catalysts, further confirming the remarkable promise of Fe-based MOFs in bifunctional electrocatalysis.20
Although single-atom catalysts have demonstrated outstanding activity toward either ORR or OER, their bifunctional catalytic performance is often intrinsically constrained due to the limited ability of isolated active sites to simultaneously optimize the adsorption energies of different reaction intermediates.21 In particular, isolated active sites are often unable to cooperatively promote ORR and OER simultaneously, and the adsorption strengths of key intermediates such as OOH* and OH* cannot be optimized in a balanced manner on a single site. These limitations collectively restrict the overall bifunctional catalytic efficiency of single-atom systems.22–24 The limited bifunctional activity of single-atom catalysts mainly arises from the intrinsic difficulty of simultaneously optimizing the adsorption energies of key reaction intermediates involved in ORR and OER. During ORR, efficient catalysis requires moderate adsorption of oxygenated intermediates such as OOH* to facilitate electron transfer and O–O bond cleavage. In contrast, OER involves the sequential oxidation of hydroxyl intermediates such as OH*, O*, and OOH*. The optimal binding energies of these intermediates often differ significantly. As a result, a single isolated metal site typically cannot provide an ideal adsorption environment for all intermediates involved in both reactions. This limitation restricts the bifunctional catalytic efficiency of single-atom systems and motivates the development of multi-metal or cooperative catalytic sites. Compared with monometallic MOFs, bimetallic MOFs generally exhibit larger specific surface areas (typically 20–50% higher than their monometallic counterparts),25,26 a greater density of tunable active sites, and significantly improved electrical conductivity due to the synergistic electronic interactions between the two metal centers. More importantly, the synergistic interactions between two different metal species endow bimetallic MOFs with superior catalytic activity.27–30 Among various transition metals, nickel is abundant in nature and possesses excellent corrosion resistance, high ductility, and favorable electrochemical properties, which have enabled its widespread application in batteries, water splitting, and other redox-related fields.31–33 In addition, a growing body of evidence suggests that the coexistence of Fe and Ni leads to strong electronic and structural interactions, thereby imparting the system with enhanced ORR/OER performance.34–38 Cheng et al. successfully fabricated a highly active and durable bimetallic NiFe-MOF bifunctional oxygen electrocatalyst using a photo-induced lattice strain strategy. The resulting catalyst exhibited ORR/OER activities far exceeding those of conventional MOFs and even commercial noble-metal catalysts. In situ characterization further revealed that the Fe/Ni dual-metal sites jointly drive an efficient four-electron reaction pathway, highlighting the significant application potential of Fe/Ni bimetallic MOFs.39 In alkaline media, the ORR can proceed through two principal pathways: a two-electron pathway producing hydrogen peroxide (O2 + 2H+ + 2e− → H2O2), and a more desirable four-electron pathway in which oxygen is directly reduced to water (O2 + 4H+ + 4e− → 2H2O).40,41 The four-electron pathway is generally preferred because it provides higher energy efficiency and suppresses peroxide formation.42 The OER corresponds to the reverse process, involving a four-electron oxidation of hydroxide ions to produce molecular oxygen (2H2O → O2 + 4H+ + 4e−).43 The catalytic pathway and kinetics of these reactions are strongly influenced by the electronic structure and coordination environment of active sites in MOF-derived catalysts. In particular, Fe–N coordination sites can effectively activate molecular oxygen, while the introduction of Ni species can regulate the electronic structure of Fe centers and optimize the adsorption energies of reaction intermediates such as OOH* and OH*, thereby promoting the four-electron ORR pathway.
Conventional MOF materials are predominantly three-dimensional, and their practical applications are often hampered by poor electrical conductivity and incomplete exposure of active sites.44–47 In contrast, two-dimensional MOFs not only retain the high porosity and structural tunability of their three-dimensional counterparts, but also benefit from extended conjugated frameworks that facilitate electron transport, thereby exhibiting considerable promise in ORR/OER electrocatalysis.48 Nevertheless, the application of 2D MOFs in this field remains challenging. On the one hand, bimetallic MOFs often suffer from limited structural stability.49,50 On the other hand, their synthesis is inherently demanding, as nonuniform metal distribution can induce phase separation or crystallographic defects.49 Moreover, the randomness and poor predictability associated with constructing dual-metal sites in 2D MOFs make precise regulation of active sites particularly difficult.48
In this work, a Ni-modified two-dimensional metal-porphyrin-based Fe-MOF precursor was rationally designed and synthesized, followed by the preparation of a series of bimetallic catalysts through optimization of the pyrolysis process. The morphology, crystalline structure, pore characteristics, and elemental valence states of the resulting materials were systematically characterized using SEM, TEM, XRD, BET, and XPS. Their ORR and OER electrochemical performances were then evaluated in a three-electrode configuration and benchmarked against a commercial Pt/C catalyst to assess bifunctional activity. By establishing an integrated research framework spanning molecular design, material fabrication, and performance validation, this study is expected to advance the application of MOF-derived materials in energy conversion and to contribute to the development of efficient and stable electrochemical devices. Therefore, the aim of this study is to develop an efficient bifunctional electrocatalyst derived from a two-dimensional metalloporphyrin Fe-MOF precursor through bimetallic modulation with Ni. The specific tasks include: (i) synthesizing NiFe-MOF and ZnFe-MOF precursors; (ii) constructing MOF-derived carbon nanotube composite catalysts via controlled pyrolysis; (iii) systematically characterizing their structural and electronic properties; and (iv) evaluating their bifunctional catalytic performance for ORR and OER in alkaline media.
000) were purchased from Aladdin Reagent Co., Ltd (Shanghai, China). 5,10,15,20-Tetrakis(4-carboxyphenyl)porphyrin iron(III) (FeTCPP, ≥97%) and H2TCPP were obtained from Sigma-Aldrich. Carbon nanotubes (CNTs, purity > 95%) were supplied by Timesnano Co., Ltd (Chengdu, China). Nafion solution (5 wt%) and commercial Pt/C catalyst (20 wt%) were purchased from Alfa Aesar. Ethanol and N,N-dimethylformamide (DMF) were analytical grade reagents obtained from Sinopharm Chemical Reagent Co., Ltd.
:
1, 6 mL). Meanwhile, 5,10,15,20-tetrakis(4-carboxyphenyl)porphyrin iron(III) (FeTCPP) (4.2 mg, 0.005 mmol) was dissolved in a DMF/ethanol solution (v/v = 3
:
1, 2 mL) to obtain a FeTCPP solution. The FeTCPP solution was added dropwise into a 10 mL glass vial containing the initial mixture, followed by sonication for 15 min. The mixture was then heated to 80 °C and allowed to react for 20 h, yielding a brown precipitate. The precipitate was collected by centrifugation, washed sequentially with ethanol and dichloromethane, and then dried overnight in a vacuum oven at 60 °C to obtain the target product, denoted as NiFeMOF.
To investigate the respective roles of Ni2+ and the Fe–N4 centers in the resulting NiFeMOF, control samples were prepared using identical procedures. Specifically, ZnFeMOF was synthesized by replacing Ni(NO3)2 in the above solution with Zn(NO3)2, and NiMOF was prepared by substituting FeTCPP with H2TCPP (metal-free 5,10,15,20-tetrakis(4-carboxyphenyl)porphyrin).
In addition to structural characterization, the catalytic reaction products during the oxygen reduction reaction were quantitatively analyzed using rotating ring-disk electrode (RRDE) measurements. The disk current corresponds to the oxygen reduction process, while the ring electrode detects peroxide species generated during the reaction. Based on the disk and ring currents, the electron transfer number and H2O2 yield were calculated to determine the dominant ORR reaction pathway.
Before initiating ORR measurements, the electrolyte (0.1 M KOH) was purged with either high-purity O2 or N2 for a minimum of 30 min to achieve saturation. Cyclic voltammetry (CV) profiles were acquired at a sweep rate of 50 mV s−1, whereas linear sweep voltammetry (LSV) was performed at a slower rate of 5 mV s−1 to assess the ORR activity. The diffusion-limited current density was determined at a potential of 0.2 V versus the reversible hydrogen electrode (RHE). For kinetic analysis, rotating disk electrode (RDE) and RRDE experiments were carried out in O2-saturated 0.1 M KOH at a scan rate of 10 mV s−1. All potentials, originally measured against an Ag/AgCl reference electrode, were converted to the RHE scale using the following relationship (eqn (1)).
| ERHE = EAg/AgCl + 0.197 + 0.0591pH | (1) |
The formation of peroxide intermediates during ORR was quantified using the RRDE system. The disk electrode was used to drive the oxygen reduction reaction, while the platinum ring electrode was maintained at 1.20 V vs. RHE to oxidize the generated peroxide species. The peroxide yield (H2O2%) and the electron transfer number (n) were calculated from the disk and ring currents according to standard RRDE equations (eqn (2)). The measurements were conducted in O2-saturated 0.1 M KOH electrolyte at a rotation speed of 1600 rpm and a scan rate of 10 mV s−1. The H2O2 yield represents the fraction of oxygen molecules reduced through the two-electron pathway relative to the total oxygen reduction process. A lower H2O2 yield indicates a higher selectivity toward the desired four-electron pathway that converts O2 directly into OH−.
| n = 4Id(Id + Ir/N) | (2) |
The oxygen evolution reaction (OER) activity was investigated via LSV in an O2-saturated 1.0 M KOH solution at a scan rate of 5 mV s−1, utilizing an identical catalyst loading to that employed in the ORR studies. To mitigate the influence of uncompensated resistance, all reported polarization curves were subjected to 95% iR correction. The operational durability of the as-synthesized materials was assessed by recording LSV profiles before and after subjecting the electrodes to 2000 successive potential cycles.
To elucidate the elemental composition of the three samples, the chemical valence states of the constituent metal elements, and their interactions with the carbon support, XPS measurements were carried out, as shown in Fig. 2, S1 and S2 (SI). The survey spectra reveal that NiFe@CNT contains C, N, Ni, Fe, and O; Ni@CNT consists of C, N, Ni, and O; while FeZn@CNT is composed of C, N, Zn, Fe, and O. For all three samples, the high-resolution C 1s spectra can be deconvoluted into five components, corresponding to COOH, C
O, C–O, C–C, and C–H species. Among them, the relative contribution of the C–C component follows the order NiFe@CNT > Ni@CNT > FeZn@CNT, indicating that the carbon phase in NiFe@CNT exhibits a higher degree of graphitization than those in Ni@CNT and FeZn@CNT.51 For NiFe@CNT (Fig. 2), the high-resolution Ni 2p spectrum exhibits characteristic peaks at 856 and 867 eV, accompanied by satellite peaks at approximately 862 and 872 eV associated with Ni2+, as well as a distinct peak at 852 eV attributable to Ni0. These features are characteristic of a NiFe alloy with a small amount of surface-oxidized Ni. In the high-resolution Fe 2p spectrum, the deconvoluted peaks at 712 and 727 eV correspond to Fe2+, those at 716 and 722 eV are assigned to Fe3+, and the peak at 706 eV is attributed to Fe0. These results indicate that, in NiFe@CNT, Ni exists in both metallic and divalent states, while Fe is present in metallic, divalent, and trivalent forms. For Ni@CNT (Fig. S1), the Ni 2p spectrum displays a typical metallic Ni0 peak at around 852 eV, together with Ni2+ features and their corresponding satellite peaks at higher binding energies, suggesting the coexistence of metallic and divalent nickel species in the material. In the case of ZnFe@CNT (Fig. S2), the Fe 2p spectrum suggests that Fe is mainly present in a mixed valence state of Fe2+ and Fe3+. In addition, a weak Fe0 signal is detected, implying that a small fraction of iron exists in the metallic state. The Zn 2p spectrum shows characteristic peaks at approximately 1022 and 1045 eV, which can be assigned to Zn2+, indicating that zinc is present in the divalent state. This observation is consistent with and complementary to the results obtained from XRD analysis.
To evaluate the specific surface area, pore size distribution, and their potential influence on the electrocatalytic performance, BET measurements were conducted on the three samples, with the results presented in Fig. 3, S3 and S4. It was found that the pore size distributions and adsorption–desorption isotherms of the three samples were remarkably similar, indicating that modification with different metal elements does not affect the fundamental framework structure of the material. According to the IUPAC classification, the N2 adsorption–desorption isotherms of all three tested samples at 77 K exhibited type IV isotherms with H4-type hysteresis loops, suggesting the presence of abundant mesopores (2–50 nm).
The influence of metal modification on textural properties was investigated through BET surface area analysis, with the results compiled in Fig. 3, S3 and S4. Inspection of the data revealed that all three samples share virtually identical pore size distributions and adsorption–desorption characteristics, indicating that the core framework remains intact regardless of the metal species introduced. Further analysis of the N2 sorption isotherms measured at 77 K showed that each sample conforms to the type IV isotherm with an H4-type hysteresis loop according to IUPAC standards. This behavior is characteristic of materials containing extensive mesoporosity, specifically pores ranging from 2 to 50 nm in diameter. These mesopores are attributed to the interstitial pores within the CNT network and the superimposed microporous/mesoporous structures generated during the pyrolysis process, which aligns with the pore structure characteristics desirable for electrocatalytic materials. Application of the Brunauer–Emmett–Teller (BET) theory to the nitrogen sorption data yielded specific surface areas of 51 m2 g−1 for NiFe@CNT, 50 m2 g−1 for Ni@CNT, and 56 m2 g−1 for ZnFe@CNT, considering the experimental uncertainty of BET measurements. Further analysis employing the Barrett–Joyner–Halenda (BJH) method coupled with the t-plot approach indicated that the pore size distributions for all three materials are predominantly situated within the mesoporous domain, specifically ranging from 2 to 50 nm, with a high degree of uniformity. Such well-defined porous characteristics are expected to enhance electrolyte permeation and promote the accessibility of active species to catalytic sites.
The surface morphology, growth state of CNTs, and overall morphological uniformity of the samples were examined using SEM, with the results presented in Fig. 4. It can be observed that all the samples exhibit a three-dimensional network structure composed of numerous intertwined one-dimensional CNTs. The CNTs are entangled and interwoven with each other, forming a continuous conductive framework. No obvious bulk aggregates or dense agglomerations are observed, indicating a relatively uniform overall morphology. Furthermore, the complete tubular structure of the CNTs and their relatively uniform diameter distribution can be clearly discerned. The individual CNTs exhibit considerable length and a high growth density, suggesting that the high-temperature pyrolysis process did not compromise the fundamental structure of the CNTs. Although the overall morphology of Ni@CNT and ZnFe@CNT (Fig. 4B and C) appears similar due to the presence of a carbon nanotube network, closer inspection reveals noticeable differences. In Ni@CNT, metallic Ni nanoparticles are relatively uniformly distributed along the CNT surfaces, while in ZnFe@CNT small aggregated particles are occasionally observed at CNT junctions, which may correspond to Zn-containing phases. These differences arise from the distinct metal species involved in the MOF precursor and their different behaviors during the pyrolysis process. Moreover, the elemental composition of the catalysts was further quantified using energy-dispersive X-ray spectroscopy (EDS). The results indicate that the NiFe@CNT composite contains approximately 3.2 wt% Ni and 2.8 wt% Fe, while ZnFe@CNT contains 3.5 wt% Zn and 2.6 wt% Fe, which is consistent with the results of XPS. These results confirm the successful incorporation of bimetallic species into the carbon matrix and support the formation of catalytically active sites.
To further verify the internal structure of the CNTs at the nanoscale, the fine microstructure of the samples was examined using TEM, with the results presented in Fig. 5. It can be observed that the samples exhibit a network structure formed by entangled and cross-linked carbon nanotubes. The CNTs are tightly interconnected, constructing a continuous three-dimensional conductive framework, with no obvious bulk agglomerations detected. Furthermore, closer inspection of the CNT wall structure reveals a relatively uniform diameter distribution, with CNT diameters measuring approximately 40–50 nm. The tube walls are intact and continuous, showing no significant collapse or fracture, indicating that the high-temperature pyrolysis process did not compromise the fundamental structure of the CNTs.
To probe the structural features of the carbon matrix, particularly regarding defects and graphitic ordering, Raman analysis was conducted on the as-prepared samples (Fig. 6). Inspection of the spectra revealed that each sample exhibits a distinct D-band at ∼1350 cm−1 and a G-band at ∼1580 cm−1 within the 500–2000 cm−1 region. The D-band is attributed to defective sites and amorphous carbon derived from sp3-hybridized configurations, while the G-band corresponds to the characteristic stretching mode of sp2-hybridized carbon in graphitic lattices. The relative intensity ratios (ID/IG) were subsequently determined to be 0.39, 0.43, and 0.51 for NiFe@CNT, Ni@CNT, and FeZn@CNT, respectively, reflecting variations in their defect densities and graphitization levels. The lower ID/IG value observed for NiFe@CNT indicates a higher degree of graphitization and fewer structural defects, which is conducive to enhanced electron transport and improved electrocatalytic performance.52,53
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| Fig. 7 CV curves of NiFe@CNT (A), Ni@CNT (B) and ZnFe@CNT (C) in 0.1 M KOH electrolyte saturated with N2 and O2. | ||
It is generally accepted that for electrocatalytic materials, a more positive onset potential (Eonset) and half-wave potential (E1/2), along with a larger absolute value of the limiting current density (JL) in LSV curves, indicate superior ORR electrocatalytic performance.54,55 Here, using commercial Pt/C as a benchmark, the electrocatalytic performance of the three materials was further analyzed via LSV measurements, with the results presented in Fig. 8A. Eonset for NiFe@CNT, Ni@CNT, and ZnFe@CNT were 0.932 V, 0.914 V, and 0.909 V, respectively; their E1/2 were 0.846 V, 0.791 V, and 0.718 V, respectively; and their JL were −5.14 mA cm−2, −4.76 mA cm−2, and −4.42 mA cm−2, respectively. Therefore, based on the LSV curves, the ORR electrocatalytic performance of the three materials follows the order, namely NiFe@CNT > Ni@CNT > ZnFe@CNT. Furthermore, the ORR performance of NiFe@CNT is even comparable to that of commercial Pt/C (Eonset = 0.974 V, E1/2 = 0.823 V, JL = 5.72 mA cm−2).
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| Fig. 8 (A) LSV curves of NiFe@CNT, Ni@CNT, ZnFe@CNT, and Pt/C in O2-saturated 0.1 M KOH; (B) Tafel slopes derived from the LSV curves. | ||
To elucidate the kinetic parameters governing the oxygen reduction reaction, Tafel plots were constructed from the LSV data, as displayed in Fig. 8B. The extracted Tafel slopes for NiFe@CNT, Ni@CNT, and ZnFe@CNT were found to be 65.73, 93.46, and 112.35 mV dec−1, respectively. It is a widely accepted tenet in electrocatalysis that a steeper Tafel slope (i.e., a larger numerical value) is associated with slower reaction kinetics, whereas a shallower slope reflects more rapid electron transfer during the rate-determining step.56,57 Consequently, the minimal Tafel slope exhibited by NiFe@CNT underscores its kinetic superiority, a conclusion that mirrors the performance hierarchy established through LSV analysis.
In addition to kinetic parameters, the efficiency of charge transfer across the electrode/electrolyte interface plays a pivotal role in determining overall catalytic activity. Electrochemical impedance spectroscopy (EIS) was therefore employed to investigate this aspect, with the resulting Nyquist plots presented in Fig. S5. The charge transfer resistance (Rct), which correlates inversely with the diameter of the semicircular arc in the high-frequency region, is a key metric for assessing interfacial electron transport.58–60 Examination of the impedance spectra revealed a distinct progression in arc diameters, increasing in the order NiFe@CNT < Ni@CNT < ZnFe@CNT. This sequence unequivocally demonstrates that NiFe@CNT possesses the lowest charge transfer resistance and thus the most efficient electron transfer kinetics, providing compelling corroboration of its enhanced electrocatalytic performance relative to Ni@CNT and ZnFe@CNT.
Based on the comprehensive results of the CV, LSV, Tafel slopes, and EIS tests described above, NiFe@CNT exhibited the optimal ORR electrocatalytic performance. Therefore, NiFe@CNT was selected for further LSV polarization curve measurements at different rotation speeds to evaluate its stability, with the results shown in Fig. S6. At various rotation speeds, Eonset of this material remained stable at approximately 0.932 V, indicating good electrochemical stability. Corresponding to rotation speeds ranging from 400 rpm to 1600 rpm, its E1/2 were 0.869 V, 0.861 V, 0.854 V, 0.849 V, and 0.844 V, respectively. Although the rotation speed increased by 1200 rpm within the range of 400 rpm to 1600 rpm, the E1/2 exhibited a change of only 0.025 V. This result falls within a reasonable margin of error, further demonstrating the material's good stability. Regarding the limiting current density, a clear increase was observed with increasing rotation speed, indicating a progressive enhancement in the electrocatalytic ORR performance.
The electron transfer number and H2O2 yield were additionally determined using the RRDE technique. As shown in Fig. 9A, the H2O2 yield of NiFe@CNT was 9.5%, which is lower than those of Co@CNT (31.3%) and ZnFe@CNT (57.6%). The low H2O2 yield of CoFe@CNT confirms that its ORR process proceeds via a four-electron pathway. According to Fig. 9B, the electron transfer numbers for the NiFe@CNT, Ni@CNT, and ZnFe@CNT catalysts were 3.9, 3.5, and 2.9, respectively, confirming a four-electron pathway for the NiFe@CNT catalyst. This result indicates that NiFe@CNT exhibits a desirable four-electron transfer mechanism under alkaline conditions, similar to that observed for the commercial Pt/C catalyst. This favorable four-electron process effectively suppresses H2O2 production, thereby facilitating the conversion of O2 to H2O during the ORR.
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| Fig. 9 H2O2 yield (A) and electron transfer number (B) of NiFe@CNT, Ni@CNT and ZnFe@CNT during ORR process. | ||
The operational robustness of NiFe@CNT was scrutinized through chronoamperometric (i–t) measurements performed at a constant applied potential of 0.8 V vs. RHE, as illustrated in Fig. S7. Impressively, the NiFe@CNT electrode demonstrated minimal current attenuation, sustaining 93.4% of its initial current density after continuous operation for more than 20
000 seconds. By contrast, the state-of-the-art Pt/C catalyst, tested under identical conditions, exhibited a more substantial deterioration, retaining only 74.5% of its original current. This stark disparity unequivocally attests to the superior electrochemical durability of NiFe@CNT.
In addition to ORR activity, the OER performance was systematically evaluated to confirm the bifunctional electrocatalytic potential of the materials. LSV was employed to acquire polarization curves in an O2-saturated 1.0 M KOH electrolyte, with RuO2 serving as a benchmark for comparison (Fig. 10A). The onset potentials, marking the commencement of the OER, were measured as 1.476 V for NiFe@CNT, 1.499 V for Ni@CNT, 1.532 V for ZnFe@CNT, and 1.484 V for RuO2. More importantly, the potentials required to achieve a current density of 10 mA cm−2—a key metric for comparing OER catalysts—were found to be 1.514 V for NiFe@CNT, 1.636 V for Ni@CNT, 1.751 V for ZnFe@CNT, and 1.578 V for RuO2. According to well-established criteria in electrocatalysis, lower onset potentials and reduced overpotentials at 10 mA cm−2 are indicative of enhanced OER kinetics. Thus, the data conclusively demonstrate that NiFe@CNT possesses superior OER catalytic activity relative to both Ni@CNT and ZnFe@CNT.
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| Fig. 10 (A) LSV polarization curves of NiFe@CNT, Ni@CNT, ZnFe@CNT and RuO2 for the OER in 1 M KOH solution; (B) Tafel slopes derived from the OER curves. | ||
To further analyze the reaction kinetics during OER, the Tafel slopes of each electrocatalytic material were fitted, with the results presented in Fig. 10B. It can be observed that the Tafel slopes corresponding to the NiFe@CNT, Ni@CNT, ZnFe@CNT, and RuO2 electrodes are 93.48 mV dec−1, 109.25 mV dec−1, 127.16 mV dec−1, and 99.21 mV dec−1, respectively. It is generally believed that a smaller Tafel slope indicates more favorable OER kinetics. Therefore, the OER performance of NiFe@CNT is superior to that of Ni@CNT and ZnFe@CNT, which is consistent with the findings from the LSV during OER.
XRD characterization (Fig. 1) clarified the differences in the crystalline phase structures of NiFe@CNT, Ni@CNT, and ZnFe@CNT, as the phase characteristics directly determine the intrinsic activity of the catalytic sites. After pyrolysis of NiFeMOF, Ni and Fe ions are reduced to form an active NiFe alloy phase. Compared to the single Ni element in Ni@CNT and the single Fe element along with ZnO impurity phases in ZnFe@CNT, the NiFe alloy exhibits significantly enhanced intrinsic ORR/OER catalytic activity due to the bimetallic electronic coupling effect. Simultaneously, its ultra-fine dispersion state further increases the density of active sites, and the absence of interfering inactive phases allows the active sites to function optimally. In contrast, Ni@CNT possesses only single Ni active sites, and grain agglomeration leads to insufficient exposure of these sites. ZnFe@CNT contains inactive ZnO impurity phases, and Fe species may undergo agglomeration, both of which prevent the formation of an efficient bifunctional catalytically active phase.
SEM and TEM images (Fig. 4 and 5) reveal that the CNTs in NiFe@CNT maintain an intact interwoven tubular structure without significant agglomeration. The three-dimensional porous network morphology of NiFe@CNT enables synergistic optimization of active sites, mass transfer, and electron conduction. On the one hand, the high specific surface area and uniform pore structure substantially increase the exposure of active sites while accelerating the diffusion rate of O2 and H2O molecules in the electrolyte. This reduces the mass transfer resistance for ORR/OER, facilitating rapid access of reactants to the active sites and timely removal of products. On the other hand, the intact CNT tubular structure, combined with the uniform dispersion of the NiFe alloy, constructs continuous electron transport channels, minimizing charge loss during electron transfer and enhancing electron conduction efficiency.
The Raman spectra of the three electrocatalysts (Fig. 6) indicate that NiFe@CNT achieves a dual enhancement in both electron conduction and active site activity. The low ID/IG ratio of NiFe@CNT, corresponding to a higher degree of graphitization and moderate defect density within the CNTs, constructs efficient and continuous electron transport channels. This significantly improves electron conduction efficiency, overcoming the electron transport limitations observed in Ni@CNT and ZnFe@CNT, and provides sufficient electron supply for ORR/OER reactions. Furthermore, the moderate defect sites enable efficient adsorption and activation of O2 and H2O molecules. Simultaneously, the excellent structural stability arising from the high graphitization degree, combined with the robust interfacial integration between the NiFe bimetallic species and the CNTs, enhances the long-term durability of the catalyst. Additionally, the synergistic effect of the NiFe bimetallic components underlying the low ID/IG ratio further strengthens the intrinsic catalytic activity of the active sites, leading to a synergistic improvement in ORR/OER bifunctional catalytic performance. In contrast, Ni@CNT and ZnFe@CNT exhibit higher ID/IG ratios, indicating insufficient graphitization and excessive defects within the CNTs. This results in low electron conduction efficiency and poor structural stability. Moreover, the absence of bimetallic synergy fails to enhance the active site activity. Consequently, their bifunctional catalytic performance is significantly inferior to that of NiFe@CNT. This mechanism also clarifies the regulatory role of the ID/IG ratio from Raman spectroscopy in governing the bifunctional catalytic performance of MOF-derived carbon-based bimetallic catalysts, providing a theoretical reference for performance optimization of analogous catalysts.
XPS characterization (Fig. 2, S1 and S2) revealed the chemical states, electronic distribution, and surface-active species content of each element in the three materials, elucidating the core reasons for the bifunctional catalytic advantages of NiFe@CNT from the perspectives of electronic state modulation and active species optimization. First, the electronic coupling effect of the NiFe bimetallic components significantly increases the content of high-valence Ni3+ (ORR active centers) and Fe3+ (OER active centers), while simultaneously modulating the electron cloud density of the metal ions. This lowers the reaction energy barriers for ORR/OER, achieving a synergistic enhancement in bifunctional catalytic activity. Secondly, the presence of abundant hydroxyl oxygen promotes the generation of ˙OH species, thereby reinforcing indirect catalytic effects. Concurrently, oxygen-containing functional groups increase the number of O2 adsorption sites, accelerating ORR reaction kinetics. Thirdly, the chemical bonding between the metals and the CNTs ensures efficient electron transfer, enabling a synergistic interaction between the active sites and the conductive channels, which further enhances catalytic efficiency. In contrast, Ni@CNT possesses only single Ni active sites with a low content of high-valence active centers. ZnFe@CNT also suffers from a low content of high-valence active centers and the presence of inactive impurity phases. Consequently, neither material achieves the optimization of electronic states and active species observed in NiFe@CNT, resulting in limited bifunctional catalytic activity.
Therefore, the fundamental reason why NiFe@CNT exhibits superior ORR/OER bifunctional catalytic performance lies in its synergistic enhancement across four dimensions, namely crystalline phase, structure, electronic state, and active sites, which is significantly superior to Ni@CNT and ZnFe@CNT. Compared to Ni@CNT, NiFe@CNT forms an active NiFe bimetallic alloy phase, overcoming the issues of single active sites and grain agglomeration. The bimetallic electronic coupling effect enhances the intrinsic activity of the active sites. Compared to ZnFe@CNT, NiFe@CNT avoids the formation of inactive ZnO impurity phases, achieving uniform dispersion of the bimetallic alloy while simultaneously improving electron conduction efficiency and increasing the content of active species.
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