Yuhu
Huang
ab,
Jin
Li
ab,
Dayu
Yu
ab,
Jiaping
Hu
ab,
Han-Shu
Xu
c and
Kaibin
Tang
*ab
aHefei National Research Center for Physical Sciences at the Microscale, University of Science and Technology of China, Hefei, 230026, China. E-mail: kbtang@ustc.edu.cn
bDepartment of Chemistry, University of Science and Technology of China, Hefei, 230026, China
cDepartment of Applied Physics, School of Biomedical Engineering, Anhui Medical University, Hefei, 230032, China
First published on 7th November 2025
In this work, we systematically investigated the optimization of water-splitting performance in A2BO4-type (214-type) Ruddlesden–Popper (R–P) perovskite catalysts via B-site substitution. PrSrCoO4, previously identified as a highly active bifunctional electrocatalyst, was selected as the parent material. A series of B-site-substituted perovskites, including PrSrCo0.6Fe0.4O4 (Fe0.4), PrSrCo0.6Fe0.2Ni0.2O4 (Ni0.2), PrSrCo0.6Fe0.3Ir0.1O4 (Ir0.1), and PrSrCo0.6Fe0.3Ru0.1O4 (Ru0.1), were successfully synthesized. Structural and magnetic characterization confirmed that all catalysts belong to the tetragonal I4/mmm space group and exhibit paramagnetic behavior at room temperature. Among the series, Ir0.1 exhibited the most remarkable bifunctional electrocatalytic performance, achieving low overpotentials of 277 mV for the oxygen evolution reaction (OER) and 279 mV for the hydrogen evolution reaction (HER) at 10 mA cm−2. This enhanced catalytic activity is attributed to Ir-induced synergistic effects, including optimized surface oxygen species, a favorable shift in the d-band center, and an increased proportion of high-spin (HS) Co3+. Overall, our experimental results broaden the electrochemical application potential of 214-type R–P perovskites and provided an ideal platform for deeper mechanistic understanding and rational catalyst design.
214-type R–P perovskite oxides also exhibit intriguing physical and chemical properties due to their distinctive structures, making them attractive candidates in functional materials research. Representative examples include La2−xSrxCuO4,14 a well-known high-temperature superconductor, and NaRTiO4 (R = rare earth elements),15 which shows notable piezoelectric behavior. While several 214-type R–P catalysts such as Sr2RuO4, Sr2IrO4, and La2NiO4 have been extensively studied for water splitting,16–18 other 214-type perovskite oxides remain largely underexplored in this field. In our previous research, we investigated the effect of A-site substitution on the electrocatalytic performance of LnSrCoO4 (Ln = La, Pr, Sm, Eu, and Ga).19 However, the role of B-site substitution in enhancing the electrocatalytic activity of 214-type R–P perovskite has received far less attention. Further research is needed to elucidate the underlying mechanisms and establish effective design strategies for improving their electrocatalytic performance.
In this work, we study the optimization of water-splitting performance in 214-type R–P perovskite catalysts through B-site substitution. Using PrSrCoO4 as the parent material, the effects of substituting the B-site with transition metals (Fe, Ni) and noble metals (Ir, Ru) on the crystal structure, magnetic behavior, and electrocatalytic activity were comprehensively explored. All catalysts belonged to the tetragonal I4/mmm space group and exhibited paramagnetic behavior at room temperature, with Ir0.1 demonstrating the most outstanding bifunctional catalytic activity. Specifically, Ir0.1 showed a significantly higher mass activity (MA) and turnover frequency (TOF) compared to the other catalysts. XPS and magnetic measurements reveal that the substitution of Ir4+ enhances the surface oxygen species ratio, induces an upward shift in the d-band center, and increases the proportion of HS Co3+.
:
0.4 exhibited the best bifunctional OER/HER performance (Fig. S1). Based on this optimal ratio, we further explored transition-metal (Ni) and noble-metal (Ir, Ru) substitution strategies, designing PrSrCo0.6Fe0.4−zNizO4 (Fig. 1c) and PrSrCo0.6Fe0.4−xMxO4 (M = Ir, Ru), respectively. XRD results revealed that co-substitution with Fe and Ni (z ≤ 0.4) did not cause lattice distortion or phase separation, and the R–P structure remains stable. In contrast, increasing Ir or Ru content beyond x = 0.1 resulted in the appearance of secondary phase peaks in the XRD patterns (Fig. S2), indicating structural instability and phase impurity at higher noble metal contents. Furthermore, the effects of both temperature and calcination time were systematically investigated. It was found that any deviation from 1150 °C within the 1050–1250 °C range increased the impurity peaks, indicating a higher secondary phase content (Fig. S3a–c). Similarly, changing the calcination time revealed that a shorter duration of 5 hours resulted in significant impurities (Fig. S3d), while a longer 20 hour calcination caused a marked decline in OER and HER performance (Fig. S3e and f). Therefore, the optimal synthesis conditions were determined to be 1150 °C for 10 hours. Based on these optimized conditions, the best-performing catalysts from each substitution series were selected for comprehensive comparison: Fe0.4, Ni0.2 (Fig. S4), and the noble-metal-substitution samples Ir0.1 and Ru0.1.
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| Fig. 1 (a) Schematic illustration of the layered perovskite crystal structure of PrSrCo1−yFeyO4. XRD patterns of (b) PrSrCo1−yFeyO4 and (c) PrSrCo0.6Fe0.4−zNizO4. | ||
Fig. 2a shows the XRD patterns of Fe0.4, Ni0.2, Ir0.1 and Ru0.1. The diffraction peaks of all samples match well with the standard powder diffraction data (JCPDS Card No. 01-074-4676), indicating identical crystal structures for these four catalysts. Fig. 2b–e shows the Rietveld refinement results of the four catalysts based on the I4/mmm space group. The refined patterns exhibit excellent consistency between the experimental and calculated profiles, confirming the high reliability of the fitting. The corresponding lattice parameters and reliability factors are summarized in Table S1. The refinement results clearly indicate that all catalysts exhibit a pure 214-type R–P phase without detectable impurity peaks.
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| Fig. 2 (a) XRD patterns of Fe0.4, Ni0.2, Ir0.1 and Ru0.1 catalysts. The XRD data for Fe0.4 and Ni0.2 used here are reproduced from Fig. 1b and c, respectively. Rietveld refinement XRD results of (b) Fe0.4, (c) Ni0.2, (d) Ir0.1 and (e) Ru0.1. | ||
As shown in Fig. S5, the SEM images revealed that the Fe0.4, Ni0.2, Ir0.1 and Ru0.1 catalysts exhibit irregular, micron-sized block-like morphologies. The N2 adsorption–desorption isotherms of the four catalysts display typical type II behavior (Fig. S6a), indicating a predominantly nonporous structure. The values of BET surface area are 2.309, 1.463, 2.353 and 0.952 m2 g−1 for Fe0.4, Ni0.2, Ir0.1 and Ru0.1, respectively. Among these four catalysts, Ir0.1 exhibited the largest specific surface area. BJH pore size distribution analysis further indicated the absence of distinct pore structures in all four 214-type R–P perovskite oxides (Fig. S6b), consistent with their morphologies observed by SEM.
To further investigate the atomic-scale structural characteristics and elemental distribution, Ir0.1, which possesses the highest surface area, was analyzed by HRTEM and EDX elemental mapping. The TEM image shows that Ir0.1 retains the irregular micron-sized block morphology with slight aggregation (Fig. 3a). The HRTEM image in Fig. 3b clearly reveals well-defined lattice fringes with an interplanar spacing of 6.24 Å, which closely matches the theoretical (002) plane spacing of 6.23 Å obtained from the XRD refinement. The corresponding FFT pattern acquired along the [2−10] zone axis exhibits distinct diffraction spots corresponding to the (004), (121), and (125) planes (inset of Fig. 3b), confirming its high crystallinity. The EDX mapping confirms that the Pr, Sr, Co, Fe, Ir, and O elements were uniformly distributed throughout the whole measured region (Fig. 3c), and the elemental ratios of Pr, Sr, Co, Fe, and Ir in Ir0.1 closely match the designed stoichiometry (Fig. S7).
Fig. 4 presents the OER performance of Fe0.4, Ni0.2, Ir0.1, and Ru0.1. As shown in Fig. 4a, Ir0.1 achieves a current density of 10 mA cm−2 at an overpotential of 277 mV, significantly outperforming Fe0.4 (355 mV), Ni0.2 (332 mV), Ru0.1 (359 mV) and commercial RuO2 (330 mV), thereby demonstrating superior OER activity. Kinetic analysis reveals that Ir0.1 exhibits the lowest Tafel slope (51.9 mV dec−1) (Fig. 4b), indicating more favorable four-electron transfer kinetics. The EIS spectra shown in Fig. 4c further confirm that Ir0.1 possesses the lowest charge transfer resistance (Rct), signifying the highest charge transport efficiency among the four catalysts. The charge transport capability follows the order: Ir0.1 > Ni0.2 > Fe0.4 > Ru0.1, which correlates well with their respective overpotential values, highlighting the critical role of interfacial charge transfer in OER performance.21
The Cdl curves, as presented in Fig. 4d and S8, indicate that Ir0.1 has the highest Cdl value of 5.60 mF cm−2, representing 3.4-fold, 1.2-fold, and 1.8-fold enhancements compared to Fe0.4, Ni0.2, and Ru0.1, respectively. This suggests that Ir0.1 possesses a larger electrochemical active surface area, providing more active sites for catalytic reactions and thereby enhancing OER performance.22,23 Furthermore, Ir0.1 exhibits the highest MA and TOF within the potential range of 1.5–1.65 V (Fig. S9a and b), indicating that the substitution of Ir improves both active site density and single-site efficiency. Long-term stability tests under a constant current density of 10 mA cm−2 show that Ir0.1 maintains optimal durability with a minimal voltage increase of 10 mV over 85 hours (Fig. S9c), markedly surpassing Fe0.4/Ni0.2 (which show a 19 mV increase over 66 hours) and Ru0.1 (which deteriorate rapidly within 5 hours). In addition, a comparative analysis with state-of-the-art perovskite materials reveals that Ir0.1 exhibits superior OER performance, exceeding even that of the pure Ir-based perovskite, SrIrO3 (Fig. 4e).
The HER performance of Fe0.4, Ni0.2, Ir0.1, Ru0.1 and 20 wt% Pt/C is presented in Fig. 5. At 10 mA cm−2, the corresponding overpotentials in Fig. 5a are 346, 355, 279, 384 and 51 mV, respectively. Among the four 214-type R–P perovskite catalysts, Ir0.1 exhibits the most favorable HER activity with an overpotential of 279 mV, significantly outperforming the other catalysts. In contrast, Ru0.1 showed the lowest catalytic performance with the highest overpotential of 384 mV. In terms of reaction kinetics, all catalysts exhibit Tafel slopes exceeding 120 mV dec−1 (Fig. 5b), specifically 205.5, 187.2, 195.8, and 246.4 mV dec−1 for Fe0.4, Ni0.2, Ir0.1, and Ru0.1, respectively. This indicates that the Volmer step is the rate-determining step in the HER process for all catalysts.24,25 Notably, although Ir0.1 does not exhibit the lowest Tafel slope, it shows the smallest overpotential, highlighting that electrocatalytic performance arises from the synergistic effects of multiple factors.26–28
As shown in Fig. 5c and d and S10, EIS and Cdl measurements further confirm the superior electrocatalytic performance of Ir0.1. It displays the lowest Rct, indicating enhanced charge transport capability, and the highest Cdl value of 10.30 mF cm−2, suggesting a larger electrochemical active surface area and more active sites for the HER. Furthermore, Ir0.1 showed remarkable advantages in both MA and TOF within the potential range of −0.3 to −0.45 V (Fig. S11a and b), indicating that the substitution of Ir enhances both the density of active sites and the intrinsic activity of each site. Long-term stability tests in Fig. S11c further revealed that Ir0.1 maintained superior stability compared to other samples, with only a minimal voltage increase of 9 mV during continuous operation over 86 hours. After comparison with other reported perovskite catalysts, it is found that the synthesized Ir0.1 demonstrates competitive catalytic performance (Fig. 5e).
In addition, the intrinsic electrocatalytic activities were further assessed using ECSA-normalized LSV curves for both the OER and HER (Fig. S12). For the OER (Fig. S12b), Ir0.1 exhibits the highest intrinsic activity at low potentials (E < 1.6 V), while Fe0.4 shows the highest normalized current density at higher potentials due to its smallest ECSA. For the HER (Fig. S12d), Ir0.1 delivers the largest current density between 0 and −0.4 V, indicating superior intrinsic activity, but its ECSA-normalized performance decreases at lower potentials, becoming inferior to Fe0.4 and Ru0.1, due to the largest ECSA of Ir0.1. These results indicate that the factors governing catalytic performance change with increasing potential. In the low-potential region (OER < 1.6 V; HER > −0.4 V), where reaction rates are sluggish, the catalytic performance is mainly determined by the intrinsic activity of active sites. In this regime, Ir0.1 exhibits the best performance owing to its optimized electronic configuration (discussed in detail below). At higher potentials, mass-transport effects dominate. The largest ECSA of Ir0.1 enhances reactant adsorption and product desorption, improving its geometric-area-normalized activity (Fig. S12a and c). However, when normalized by ECSA to exclude the contribution of surface area, this mass-transfer limitation leads to relatively lower intrinsic activity for Ir0.1 compared to Fe0.4 (OER) and Fe0.4/Ru0.1 (HER).
The elemental composition and chemical states of the Fe0.4, Ni0.2, Ir0.1, and Ru0.1 catalysts were analyzed using XPS. As shown in Fig. S13a, the full spectra of all catalysts exhibit characteristic peaks corresponding to Pr, Sr, Co, Fe, and O. In addition, the distinct signals for Ni, Ir, and Ru are only observed in Ni0.2, Ir0.1, and Ru0.1, respectively, confirming the successful substitution of the corresponding elements. In Fig. S13b, the Fe 2p spectra of the four catalysts exhibit nearly identical peak positions and line shapes, with Fe3+ 2p3/2 and 2p1/2 peaks located at 711.5 eV and 723.8 eV, respectively.29,30 This similarity indicates that the crystal field environment of Fe sites remains largely unchanged by Ni, Ir, or Ru substitution, suggesting a stable electronic structure for Fe sites. Furthermore, the valence states of substituting elements were investigated. For Ni0.2 (Fig. S13c), the Ni 2p3/2 and 2p1/2 peaks appear at 855.6 eV and 873.5 eV, respectively,31,32 suggesting that Ni predominantly exists in the Ni3+. In Ir0.1, the Ir 4f spectrum shows 4f7/2 and 4f5/2 peaks at 63.1 eV and 66.1 eV, respectively (Fig. S13d),33 which are consistent with the binding energies of Ir4+. Similarly, for Ru0.1, the Ru 3p3/2 and 3p1/2 peaks are located at 464.4 eV and 486.6 eV, respectively (Fig. S13e),34 confirming the presence of Ru4+.
In the Co 2p spectra (Fig. 6a and S14), Fe0.4, Ni0.2, Ir0.1, and Ru0.1 exhibit highly similar peak features at 780.4 eV (Co 2p3/2) and 795.6 eV (Co 2p1/2), suggesting the comparable valence state of cobalt ions. To further investigate the oxidation states of Co ions, detailed peak deconvolution of the Co 2p spectra was performed in Fig. 6a. The results show that the Co3+ to Co2+ ratios are nearly identical across the four catalysts (Table S4), with an average Co oxidation state of 2.73. These results confirm that Co valence states remain unchanged upon substituting with Ni, Ir, or Ru. Therefore, the difference in catalytic performance cannot be attributed to changes in the Co oxidation state.
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| Fig. 6 XPS spectra of (a) Co 2p, (b) O 1s and (c) valence-band spectra for Fe0.4, Ni0.2, Ir0.1 and Ru0.1 catalysts. | ||
The O 1s spectra of Fe0.4, Ni0.2, Ir0.1, and Ru0.1 as shown in Fig. 6b were analyzed to elucidate the intrinsic relationship between surface oxygen species and electrocatalytic activity. The spectra of all catalysts can be deconvoluted into four oxygen species: lattice oxygen species (O2− at 529.1 eV), highly oxidative oxygen species (O22−/O− at 530.5 eV), surface hydroxyl/adsorbed oxygen (OH−/O2 at 531.5 eV), and adsorbed water (H2O at 533.1 eV). Among the four oxygen species, the proportion of O22−/O− is positively correlated with the concentration of oxygen vacancy. Oxygen vacancies not only enhance the adsorption/desorption kinetics of reaction intermediates but also modulate the coordination environment of Co–O bonds, thereby inducing local electronic structure rearrangements.35,36 Previous studies have demonstrated that an increased ratio of O22−/O− species is generally associated with improved catalytic activity.37–39 As shown in Fig. 6b and summarized in Table S5, Ir0.1 exhibits the highest proportion of O22−/O−, which corresponds well with its superior OER and HER performance. Moreover, Ru0.1 exhibits the highest content of O2− and OH−/O2 species in the four catalysts, yet it shows the lowest catalytic performance, suggesting that these two types of surface oxygen species do not play a beneficial role in 214-type R–P perovskites. In addition, although Fe0.4 contains the highest fraction of H2O species, its electrocatalytic activity is significantly lower than that of Ir0.1, indicating that the adsorbed water content is not the primary determinant of catalytic performance.
The valence-band spectra as shown in Fig. S15 for Fe0.4, Ni0.2, Ir0.1, and Ru0.1 exhibit similar spectral features, indicating broadly consistent valence band structures. Further analysis of the d-band center (εd) through valence-band spectra integration (Fig. 6c) shows that the εd of Ir0.1 (−3.81 eV) is shifted closer to the Fermi level compared to those of Fe0.4 (−3.99 eV), Ni0.2 (−3.95 eV), and Ru0.1 (−3.91 eV). According to the d-band center theory, an εd closer to the Fermi level reflects an increase in the energy of antibonding orbitals, resulting in a lower filling of the antibonding orbitals.40,41 This modified electronic configuration leads to enhanced bonding stability and stronger adsorption between the catalytic active sites and the reaction intermediates, thereby improving electrocatalytic performance.29,42 Correlating the d-band center with electrocatalytic performance (Fig. S16), a negative relationship is observed between εd and the overpotential at 10 mA cm−2 (η10) for both the OER and HER. Specifically, a higher εd (closer to the Fermi level) corresponds to a lower η10 value. Obviously, Ir0.1, with the εd value closest to the Fermi level, achieves the best electrocatalytic performance. These findings highlight the unique advantage of Ir substitution, which induces an upward shift of the d-band center. This electronic modulation optimizes the adsorption strength between the active sites and reaction intermediates, effectively lowering the energy barriers for both the OER and HER. In addition, the Co–O bond length was also correlated with catalytic activities toward both reactions (Fig. S17). For the OER (Fig. S17a), the bond length follows the order Ir0.1 > Ni0.2 > Ru0.1 > Fe0.4, whereas the overpotential exhibits the opposite trend (Ir0.1 < Ni0.2 < Fe0.4 ≤ Ru0.1), revealing a clear negative correlation in which a longer Co–O bond generally promotes superior OER performance. A similar relationship is observed for the HER (Fig. S17b), where the overpotential sequence (Ir0.1 < Fe0.4 ≤ Ni0.2 < Ru0.1) inversely correlates with the bond-length trend. Although Fe0.4 slightly deviates from this relationship, the overall trend remains consistent, suggesting that a longer Co–O bond length tends to favor improved HER activity as well.
The structural stability of Ir0.1 after long-term OER and HER testing was systematically evaluated. The XRD and Raman results confirm that the Ir0.1 catalyst retains its original crystalline structure without detectable phase transition or degradation (Fig. S18). HRTEM reveals the formation of a thin amorphous surface layer (yellow dashed lines), while the bulk remains well-crystallized, indicating excellent structural integrity (Fig. S19). Furthermore, the XPS spectra of Co 2p, Fe 2p, and Ir 4f show negligible changes before and after reaction (Fig. S20a–c), indicating stable oxidation states and chemical environments. In contrast, the O 1s spectra exhibit a significant decrease in the lattice oxygen, particularly after the OER (Fig. S20d), which is consistent with the surface amorphization revealed by HRTEM.
The magnetic behavior of Fe0.4, Ni0.2, Ir0.1, and Ru0.1 was systematically investigated through magnetic measurements. As shown in Fig. 7a, the zero-field-cooled (ZFC) χ(T) curve of Fe0.4 displays a clear shoulder at approximately 75 K, while this feature is significantly weakened in the field-cooled (FC) curve. Upon further cooling to around 50 K, a clear bifurcation appears between the ZFC and FC curves, suggesting the formation of a spin-glass or cluster-glass state in this system. Indeed, such magnetic states are commonly reported in Co-based perovskite oxides, including typical single perovskites such as La1−xSrxCoO3 and double perovskites like Sr2FeCoO6 and La1.5Ca0.5CoMnO6.43–45 For Ni0.2 (Fig. 7b), a rapid increase in magnetic susceptibility is observed in both ZFC and FC curves around 180 K, which can be attributed to a ferromagnetic/ferrimagnetic phase transition. In the noble-metal-substitution systems, the magnetic behavior of both Ir0.1 and Ru0.1 is similar to that of LaSrCoO4 (Fig. 7c and d),19 exhibiting spin freezing in these systems. Further, the M(H) curves reveal that the four catalysts exhibit weak ferromagnetic/ferrimagnetic behavior at 10 K, while displaying paramagnetism at 300 K (insets of Fig. 7a–d).
The ZFC 1/χ(T) curves of Fe0.4, Ni0.2, Ir0.1, and Ru0.1 were fitted using the Curie–Weiss (CW) law to obtain the Weiss temperature (θ) and the effective magnetic moment (μeff), as summarized in Table. S6. For the Fe0.4 system, μeff (Co) was calculated using the formula: μeff = [μeff (Pr3+)2 + 0.6μeff (Co)2 + 0.4μeff (Fe3+)2]1/2. Given that μeff (Pr3+) is 3.60 μB and μeff (Fe3+) in the octahedral coordination is 4.04 μB,46–49 the calculated μeff (Co) in Fe0.4 is 3.15 μB. This value represents a significant deviation from the parent PrSrCoO4. PrSrCoO4 exhibits a μeff (Co) of 2.80 μB, which is consistent with the theoretical value for Co3+ in the intermediate-spin (IS) state (S = 1, μeff ≈ 2.83 μB), as discussed in our previous work.19 The increased μeff (Co) in Fe0.4 suggests a partial transition of Co3+ from an IS to a HS (S = 2, μeff = 4.90 μB), indicating that the substitution of Fe3+ induces a partial spin-state transition of Co3+, resulting in a mixed IS/HS configuration. For Ni0.2, a more pronounced spin-state transition is observed. Upon substituting with Ni3+ (μeff = 1.73 μB), the μeff (Co) increases to 3.66 μB, implying a higher proportion of HS Co3+. The enhanced OER performance of Ni0.2 compared to Fe0.4 may be partly attributed to the increased HS Co3+ content, while its slightly reduced HER activity suggests that the spin state of Co3+ plays distinct roles in the OER and HER processes.
In the noble-metal-substitution systems, the μeff (Co) values in Ir0.1 and Ru0.1 are 3.93 μB and 3.78 μB, respectively, where the μeff values for Ir4+ and Ru4+ are 0.10 μB and 2.00 μB.50–52 Although charge compensation due to Ir4+ or Ru4+ substitution might induce a minor reduction of Co3+ to Co2+, the low substitution levels ensure that Co3+ remains the dominant species. Therefore, the analysis primarily focuses on changes in the spin state of Co3+ in Ir0.1 and Ru0.1. Among the four catalysts, Ir0.1 exhibits the highest μeff (Co), indicating the largest proportion of HS Co3+, consistent with previous reports that associate HS Co3+ with enhanced water-splitting activity.53–55 This provides a reasonable explanation for the superior bifunctional catalytic performance of Ir0.1. In contrast, although Ru0.1 shows the second-highest HS Co3+ content, it displays the lowest OER and HER activities in these four catalysts, which may be attributed to its lowest specific surface area and oxygen vacancy concentration. The results suggest that electrocatalytic performance arises from a synergistic interplay among intrinsic activity, surface active site density, and charge transport dynamics. While metal substitution can effectively tune the spin state of Co3+ to enhance intrinsic catalytic activity, the overall performance is constrained by a complex set of multiscale factors.
Supplementary information: includes SEM, EDS mapping, BET, XPS, XRD, HRTEM and electrocatalytic performance. See DOI: https://doi.org/10.1039/d5ce00782h.
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