An efficient and stable protonic ceramic fuel cell cathode achieved by Yb-doping

Yixuan Huang Jiacheng Zeng Wenjie Gong Wanbin Lin Hao Liu Chuqian Jian Xiaofeng Chen Tang Sheng Li Zhang Fan He Yu Chen

Citation:  Yixuan Huang, Jiacheng Zeng, Wenjie Gong, Wanbin Lin, Hao Liu, Chuqian Jian, Xiaofeng Chen, Tang Sheng, Li Zhang, Fan He, Yu Chen. An efficient and stable protonic ceramic fuel cell cathode achieved by Yb-doping[J]. Chinese Chemical Letters, 2026, 37(9): 111664. doi: 10.1016/j.cclet.2025.111664 shu

An efficient and stable protonic ceramic fuel cell cathode achieved by Yb-doping

English

  • The extensive adoption of renewable energy is essential for the attainment of sustainable development [1]. Protonic ceramic fuel cells (PCFCs), as a new generation of clean energy devices, have become a focal point in recent green energy research owing to their high fuel utilization, low cost, and excellent sustainability [25]. However, the widespread development of PCFCs is still constrained by the limited kinetics of the oxygen reduction reaction (ORR) and insufficient durability of cathodes [69]. Consequently, for the practical implementation of PCFCs, it is imperative to develop cathodes with both high electrocatalytic activity for ORR and exceptional durability under operating conditions [10,11]. The structural versatility of perovskite-type oxides, resulting from their tunable cationic substitution of A and B sites, creates dynamic redox active sites and controllable oxygen vacancy concentrations [12]. These properties make them highly attractive as cathode materials for PCFCs. So far, La0.6Sr0.4Co0.2Fe0.8O3−δ (LSCF), Ba0.5Sr0.5Co0.8Fe0.2O3−δ (BSCF), BaCo0.4Fe0.4Zr0.1Y0.1O3−δ (BCFZY), etc., representing the perovskite-type oxides, have been extensively applied in PCFCs and achieved outstanding electrochemical performance [1315]. PrBaCo2O5+δ (PBC), a conventional air electrode material with mixed ionic and electronic conductivity, enables remarkable electrocatalytic activity for ORR and superior oxygen diffusion kinetics [16,17]. The segregation of Ba at the A-site in the PBC cathode induces the stability of PCFCs during operation [18,19]. Therefore, it is necessary to employ targeted modification strategies to improve the structural integrity and electrochemical performance of PBC for effective integration.

    Various practicable methodologies were applied to further improve the electro-catalytic activity and structural integrity of the PBC-based cathodes. For example, Gao et al. infiltrated a multi-cationic oxide catalyst coating with a composition of Pr0.2Ce0.2Ni0.2Co0.2Fe0.2Ox (PCNCF) to boost the ORR activity and longevity of the PBC cathode [20]. The PCNCF-coated PBC air electrode achieved more satisfactory fuel cell performance than the bare PBC air electrode at 700–600 ℃. Meanwhile, as the cerium oxide in the catalyst coating reacted with separate Ba to form active ingredients, both the catalytic reaction activity and the operational stability of PBC have been improved [20]. Entropy engineering can endow perovskite oxides with multifunctionality, including electrocatalytic activity, phase stability, and rapid ion transport [21]. Zhu et al. modulated the conformational entropy of the PBC perovskite by doping alkaline earth metals at the A-site to develop a medium-entropy Pr0.5Ba1/6Sr1/6Ca1/6CoO5+δ (PBSCC) electrode with enhanced functionality [22]. The PCFCs incorporating the PBSCC cathode demonstrated exceptional performance (0.80 W/cm2 at 550 ℃) and stability (for over 250 h) [23]. In addition, precisely engineered doping with cations has been considered as a widely adopted modification strategy to improve ORR activity and reinforce structural robustness for PBC [24]. Du et al. adopted an In-doping method to develop a PrBa0.95Co1.85In0.09O5+δ (PBCIn) air electrode with a BaCo0.85In0.15O3−δ (BCIO) cubic second phase [25]. Indium doping has been demonstrated to enhance ORR and OER kinetics, enabling the PBCIn air electrodes to achieve remarkable electrochemical performance (1.33 W/cm2 at 600 ℃) in PCFCs [25].

    Recently, lanthanide elements have been extensively utilized as dopants in PCFCs. Ytterbium, an element in the lanthanide series, has attracted considerable attention [26,27]. Yb doping has been widely proven as an effective strategy for developing advanced proton-conducting electrolytes [28]. Yang et al. reported that BaZr0.1Ce0.7Y0.2-xYbxO3-δ (BZCYYb), a Y and Yb co-doped mixed ion conductor, enabled rapid transport of protons and oxide ion vacancies, achieving high ionic conductivity at 700–500 ℃ [29]. Further, Guo et al. discovered that higher Yb doping levels led to a simultaneous rise in proton concentration and ionic conductivity, suggesting a critical role of Yb in BZCYYb [30]. Luo et al. synthesized a Yb-doped BaHf0.1Ce0.7Yb0.2O3-δ (BHCYb172) proton-conducting electrolyte, which has high ionic conductivity and excellent chemical stability [31]. When applied in PCFCs, the cell showed outstanding performance of 1.73 W/cm2 at 600 ℃, caused by the fact that Yb doping can increase oxygen migration rates and reduce both activation energy and thermal expansion coefficient in diverse crystalline materials [3234]. To date, studies on the substitution of Yb are primarily focused on electrolytes, with limited investigation of their application in the cathodes of PCFCs. Due to the lower valence state, Yb3+ doping at the B-site may increase the oxygen vacancy concentration [31]. These intrinsic vacancies could promote water incorporation to provide proton sources that contribute to the charge transfer process on the electrode surfaces [35]. Furthermore, in perovskites, the Gibbs free energy of hydration exhibits a linear dependence on the average cationic electronegativity, with lower electronegativity favoring stronger water adsorption [36,37]. The substitution of Co with lower-electronegativity Yb3+ at the B-site could enhance hydration capability, consequently improving electrocatalytic activity. Studies are showing that doping with low-electronegativity elements effectively improved the performance of PBC air electrodes, such as PrBa0.9Cs0.1Co2O5+δ (PBCsC) and PrBaCo1.8Nb0.1Y0.1O5+δ (PBCNY) [38,39].

    Inspired by the above findings, we designed a ytterbium-doped PBC-based perovskite material with the designed composition of PrBaCo1.95Yb0.05O5+δ (PBCYb0.05). The perovskite consists of a major perovskite phase of deficient-PrBa1-xCo1.950.99x Yb0.050.01xO5+δ (D-PBCYb0.05) and a minor secondary perovskite phase BaCo0.99Yb0.01O3-δ (BCYO). The nanoscale synergy between these two phases significantly enhances both the electrocatalysis and durability of the cathode. From the results of the experiments, compared to the PBC, PBCYb0.05 displays more oxygen vacancies and faster oxygen surface exchange and bulk conduction kinetics. Therefore, the PBCYb0.05 cathode achieved a relatively low area-specific resistance of 0.249 Ω cm2 (vs. 0.410 Ω cm2 from the PBC). The PCFCs employing the developed PBCYb0.05 cathode achieved an outstanding power density of 2.25 W/cm2 at 700 ℃ and a desirable short-term stability for 103 h at 600 ℃.

    The details of chemicals and materials, material preparation, cell fabrication, electrochemical measurements, and characterization of materials are provided in Supporting information.

    To characterize the phase composition of PBCYb0.05, we performed the X-ray diffraction (XRD) and related Rietveld refinement analysis. As shown in Fig. 1a, the PBCYb0.05 powder is composed of a major perovskite phase of deficient-PrBa1-xCo1.950.99xYb0.050.01xO5+δ (D-PBCYb0.05, a = b = 3.888 Å and c = 7.705 Å, 95.08 wt%) and a minor secondary perovskite phase of BaCo0.99Yb0.01O3-δ (BCYO, a = b = c = 4.143 Å, 4.92 wt%). The corresponding fitting parameters are Rwp = 4.02%, Rp = 3.06%, and χ2 = 2.008, indicating that the Rietveld refinement analysis is reasonable. XRD patterns of PBC and other materials with Yb doping ratios are given in Fig. 1b and Fig. S1 (Supporting information). The BCYO secondary phase emerges when the Yb doping ratio is 1.25%, and its volume fraction increases significantly at 2.50%. The heterogeneous phase increases when the Yb content reaches 3.75%. It is worth noting that the main characteristic peak of PBCYb0.05 exhibits a distinct shift to a lower angle at 32°−34°, compared to PBC, suggesting a lattice expansion (Fig. S2 in Supporting information). This phenomenon indicates that ytterbium has successfully been doped into the B-site of the PBC perovskite since the ionic radius of Yb3+ is between the Pr3+/Pr4+ and Co3+/Co4+ [3840]. It has been confirmed that Yb preferentially occupies the B-sites of perovskites containing large A-site elements such as Pr, Ba, and Sr [41]. The chemical compatibility between the PBCYb0.05 powder and BaZr0.1Ce0.7Y0.1Yb0.1O3-δ (BZCYYb) powder is illustrated in Fig. S3 (Supporting information). The result indicates there are no chemical side reactions between the PBCYb0.05 air electrode and the BZCYYb electrolyte. To determine the phase composition of PBCYb0.05, HR-TEM was employed in combination with energy-dispersive spectroscopy (EDS) mapping analysis. Distinct regions of PBCYb0.05 and BCYO can be identified in the HR-TEM image (Fig. 1c). As shown in Fig. 1d, the lattice spacing of BCYO, determined by fast Fourier transformation (FFT), is approximately 0.207 nm, likely corresponding to the (002) crystallographic plane. Analogously, the measured lattice spacing of 0.276 nm matches mostly with the (110) crystallographic plane of PBCYb0.05 through FFT (Fig. 1e). From the STEM and EDS mapping images, the absence of the Pr element is visible (Fig. 1f). The SEM images of the PBCYb0.05 and PBC powders are shown in Figs. S4 and S5 (Supporting information). In contrast, the BCYO nanoparticles can be found in PBCYb0.05. Combined with the other results (XRD and TEM), it is demonstrated that PBCYb0.05 is a two-phase composite with D-PBCYb0.05 and BCYO.

    Figure 1

    Figure 1.  Phase characterization of the PBCYb0.05 powder. (a) XRD Rietveld refinement of PBCYb0.05 powder sintered at 1000 ℃ for 4 h. (b) XRD patterns of PBCYb0.05 and PBC powders sintered at 1000 ℃ for 4 h. (c) HR-TEM images of PBCYb0.05 powder. The lattice spacings and FFT images of (d) BCYO and (e) PBCYb0.05. (f) STEM image and EDS mapping of PBCYb0.05 powder with Pr, O, Ba, Yb, and Co elements.

    Electrochemical impedance spectroscopy (EIS) curves of BZCYYb electrolyte-supported symmetrical cells with PrBaCo2-xYbxO5+δ (x = 0, 0.05, 0.10, and 0.15) (denoted as PBC, PBCYb0.05, PBCYb0.10, PBCYb0.15) electrodes are performed to evaluate the Yb doping effect on the electrochemical performance of PBC-based electrodes (Fig. 2a and Fig. S6-S8 in Supporting information). All the EIS curves were measured at an open-circuit voltage (OCV) condition in humid air (3 vol% H2O). The area-specific resistance (ASR) values of the PBCYb0.05 symmetrical electrode are 0.077, 0.150, 0.249, 0.441, and 1.013 Ω cm2 at 700, 650, 600, 550, and 500 ℃, respectively. As exhibited in Fig. 2b, the PBCYb0.05 electrode achieves the minimum ASR among all Yb doping ratios, suggesting that the formation of unitary and pure BCYO secondary phase is crucial for electrochemical performance. The enhanced electrochemical performance after ytterbium doping compared to the PBC electrode may be attributed to the relatively lower electronegativity of Yb3+, which can reduce the average electronegativity of cations in the system. As evidenced by the ASR comparison in Fig. 2c, the PBCYb0.05 air electrode exhibits remarkable electrocatalytic performance relative to reported advanced cathodes, demonstrating its superior catalytic activity [13,21,23,39,4245]. Further details of these cells are in Table S2 (Supporting information). Meanwhile, the electrochemical stability of symmetrical cells is also an important index for evaluating the cathode. As shown in Fig. 2d, the electrochemical stabilities of symmetrical cells with PBCYb0.05 and PBC cathode are measured in humid air (3 vol% H2O) at 600 ℃. The corresponding EIS spectra are presented in Figs. S9 and S10 (Supporting information), respectively. The polarization resistance (Rp) values of the PBCYb0.05 air electrode increased from 0.249 Ω cm2 to 0.308 Ω cm2 for 104 h, indicating that it maintained better stability than the PBC air electrode (from 0.410 Ω cm2 to 0.506 Ω cm2 for 104 h). The electrochemical performance stability of the PBCYb0.10 air electrode with the corresponding EIS curves is also tested (Figs. S11 and S12 in Supporting information). After 104 h of operation, the Rp values of the PBCYb0.10 air electrode finally ended at 0.355 Ω cm2, exceeding the final Rp values of PBCYb0.05. The result highlights the better electrochemical stability of the PBCYb0.05 air electrode. To elucidate the degradation mechanisms of symmetrical cells, the distribution of relaxation times (DRT), a deconvolution method to resolve EIS curves into discrete electrochemical processes, was applied. Three distinct electrochemical processes can be resolved in a DRT spectrum through different frequency distributions: Low frequency (LF, 103−10 Hz), intermediate frequency (IF, 10−104 Hz), and high frequency (HF, 104−105 Hz). Three typical EIS curves from the stability measurements of the PBCYb0.05 and PBC cathodes are selected for the DRT analysis, covering the beginning, the middle, and the end. As shown in Fig. 2e, the change in DRT curves is concentrated in the IF range, suggesting that the processes of oxygen surface exchange primarily govern the Rp evolution in the PBCYb0.05 air electrode [46]. Similarly, the increased Rp values of the PBC air electrode originate from modifications in both LF and HF ranges (Fig. 2f). The LF and HF ranges are associated with gas diffusion and charge transfer processes, respectively [4648]. The results confirm the efficacy of Yb3+ doping in improving gas diffusion and charge transfer efficiency.

    Figure 2

    Figure 2.  Cathode performance in symmetrical cells. (a) EIS curves of BZCYYb electrolyte-supported symmetrical cells with PBCYb0.05 air electrode tested in humid air (3 vol% H2O) at 700–500 ℃. (b) Electrocatalytic performance comparison of symmetrical cells with PBCYb0.10, PBCYb0.05, PBC, and PBCYb0.15 electrodes. (c) Area-specific resistance of PBCYb0.05 and PBC in this work relative to other materials recently reported. (d) Short-term stability of a symmetrical cell with PBCYb0.05 air electrode in humid air (3 vol% H2O) at 600 ℃. The DRT curves of symmetrical cells with (e) PBCYb0.05 and (f) PBC air electrodes during stability testing.

    The underlying mechanism for the superior electrochemical performance of the PBCYb0.05 air electrode requires thorough exploration. The electrical conductivities of PBCYb0.05 and PBC samples are shown in Fig. 3a. Both samples exhibit the same temperature-dependent conductivity trend as reported in the literature, showing a decrease in conductivity with increasing temperature. Compared to the PBC sample, the relatively low conductivity of the PBCYb0.05 sample originates from the substitution of Yb at Co sites, breaking the strongly covalent Co-O bonds [49]. The surface chemistry of PBC and PBCYb0.05 powders was characterized by XPS to determine Co valence states and oxygen vacancy concentration. As displayed in Fig. 3b, according to the binding energies, the Co 2p3/2 and Ba 3d5/2 XPS spectra can be classified into three subsidiary peaks: Co3+ (central peak is at ≈777.15 eV), Ba2+ (central peak is at ≈779.29 eV), and Co4+ (central peak is at ≈780.89 eV) [22]. After Yb3+ doping, the rise in Co4+ content implies greater catalytic activity availability [50]. Likewise, the O 1s XPS spectra can be resolved into four distinct peaks, which are the lattice oxygen (Olat, central peak is at ≈528.75 eV), the highly oxidative oxygen (O/O22−, central peak is at ≈531.01 eV), the adsorbed oxygen (Oads, central peak is at ≈531.94 eV) and the hydroxyl oxygen (OH, central peak is at ≈533.37 eV) (Fig. 3c) [25]. The relative distribution percentages of four distinct peaks for PBCYb0.05 and PBC materials are quantified in Fig. 3d. The oxygen vacancy concentration correlates with the value of O/O22−. A higher value of highly oxidative oxygen of PBCYb0.05 (O/O22- = 37.38%) than that of PBC (O/O22- = 25.36%) may suggest that Yb doping can lead to more oxygen vacancies in the cathode [25]. To provide additional evidence of the improvement in oxygen transport kinetics and ORR activity, we measured the electrical conductivity relaxation (ECR) response curves of both PBCYb0.05 and PBC samples from 700 ℃ to 600 ℃ (Fig. 3e and Fig. S13 in Supporting information). The determination of surface exchange coefficients (k*chem) and bulk diffusion coefficients (D*chem) is based on Fick's second law. As exhibited in Fig. 3f, the k*chem and D*chem values of PBCYb0.05 are larger than those of PBC, revealing that the oxygen surface exchange and diffusion kinetics of the PBCYb0.05 cathode are enhanced [8]. The detailed k*chem and D*chem are listed in Table S3 (Supporting information). These experimental data confirm that the ORR activity of the PBC-based air electrode can be improved by effectively accelerating the oxygen transport kinetics through Yb doping. Thus, incorporating an appropriate amount of Yb into PBC perovskite generates multifunctional improvements, leading to superior electrocatalytic activity. In addition, thermal expansion coefficient (TEC) curves of the PBCYb0.05 and PBC samples are exhibited in Fig. S14 (Supporting information). It is shown that PBCYb0.05 exhibits a similar thermal expansion to other cobalt-based electrode materials [21,51,52].

    Figure 3

    Figure 3.  Discussion on the mechanism of the PBCYb0.05 electrode. (a) Electrical conductivity of PBCYb0.05 and PBC samples from 400 ℃ to 775 ℃. (b) The Co 2p3/2, Ba 3d5/2 and (c) O 1s XPS spectra for PBC and PBCYb0.05 powders. (d) Column distribution of four oxygen species in PBCYb0.05 vs. PBC powders. (e) ECR response curves of PBCYb0.05 sample from 700 ℃ to 600 ℃. (f) Temperature dependence of the k*chem/D*chem for PBCYb0.05 and PBC samples.

    The Ni-BZCYYb anode-supported PCFCs with PBCYb0.05 or PBC cathode were assembled and systematically tested for electrochemical performance and durability to verify the improvement in ORR activity and oxygen transport. As depicted in Fig. 4a, the current density-voltage-power density (I-V-P) curves of the PCFC loaded with the PBCYb0.05 air electrode are measured during fuel cell operation from 700 ℃ to 600 ℃. Remarkable peak power densities (PPDs) of 2.25, 1.52, and 1.09 W/cm2 are achieved at 700, 650, and 600 ℃, respectively. Simultaneously, as shown in Fig. 4b, under OCV conditions, the Rp values of this PCFC remain relatively low, which are 0.022, 0.054, and 0.135 Ω cm2 at 700, 650, and 600 ℃, respectively. After electrochemical testing under hydrogen reduction conditions, the cross-sectional scanning electron microscopy (SEM) image of this PCFC is presented in Fig. 4c. The specific morphologies of the PBCYb0.05 air electrode and Ni-BZCYYb fuel electrode are exhibited in Figs. S15 and S16 (Supporting information). The PCFC possesses a classic triple-layer structure, consisting of a porous PBCYb0.05 air electrode layer (≈6 μm), a dense BZCYYb electrolyte layer (≈7 μm), and a porous Ni-BZCYYb fuel electrode layer. To enable direct comparison, the I-V-P curve and area-specific polarization resistances of the PCFC loaded with PBC air electrode are recorded in Figs. S17 and S18 (Supporting information). The PCFC loaded with PBC air electrode exhibits peak power densities of 1.68, 1.22, and 0.96 W/cm2 at 700, 650, and 600 ℃, respectively. The enhanced electrochemical performance can be attributed to the Yb doping in PBC. Meanwhile, at 700, 650, and 600 ℃, the Rp values of the PCFC loaded with PBC air electrode are 0.040, 0.085, and 0.183 Ω cm2, respectively. The electrochemical resistances, including both ohmic resistances (Ro) and Rp of PCFCs loaded with PBCYb0.05 and PBC cathode, are quantitatively compared in Fig. 4d. Although the Ro of the PCFC with PBCYb0.05 air electrode is marginally larger, the significantly lower Rp values compared to those with the PBC air electrode are responsible for the enhanced power output, suggesting the polarization resistance of PCFCs contributes mostly to the performance improvement. To explore the influence of different Yb-doped cathodes on the performance of PCFCs, the I-V-P curves and the corresponding impedance spectra of PCFCs loaded with PBCYb0.10 and PBCYb0.15 cathodes were measured (Figs. S19-S22 in Supporting information). Among all the Yb-doped cathodes, the PCFC loaded with PBCYb0.05 exhibited the best electrochemical performance, as demonstrated by the test results of symmetrical cells. In recent literature, the performance of the PBCYb0.05 cell has surpassed most of its counterparts with comparable electrolyte architectures (Table 1 and Fig. S23 in Supporting information) [10,25,38,43,44,5357]. As shown in Fig. 4e, at a current density of 0.5 A/cm2 and 600 ℃, the PCFC loaded with PBCYb0.05 air electrode maintained stable operation for 103 h with a slight degradation rate of 1.08 mV/h, demonstrating the Yb-doped PBC enables reliable application as cathode in PCFCs.

    Figure 4

    Figure 4.  Electrochemical performance and microcosmic structure of PCFCs loaded with PBCYb0.05 and PBC cathodes. (a) The I-V-P curves and (b) impedance spectra of PCFCs loaded with PBCYb0.05 cathode from 700 ℃ to 600 ℃. (c) The cross-sectional SEM image of a single cell loaded with the PBCYb0.05 cathode after electrochemical testing. (d) Comparison of Ro and Rp of PCFCs loaded with PBCYb0.05 and PBC cathodes. (e) Operational durability of PBCYb0.05 cell at a current density of 0.5 A/cm2 and 600 ℃.

    Table 1

    Table 1.  Comparison of the PPDs of PBCYb0.05 and PBC cells with other recently reported cells which possess a similar construction.
    DownLoad: CSV
    Air electrode Electrolyte Fuel electrode Electrolyte thickness (μm) Temp. (℃) PPD (W/cm2) Source
    700 2.25
    PrBaCo1.95Yb0.05O5+δ (PBCYb0.05) BZCYYb Ni-BZCYYb ~7 650 1.52 This work
    600 1.09
    700 1.68
    PrBaCo2O5+δ (PBC) BZCYYb Ni-BZCYYb ~7 650 1.22 This work
    600 0.96
    700 1.77
    Pr0.1Ce0.9O2+δ-PrBaCo2O5+δ (PCO-PBC) BZCYYb Ni-BZCYYb 8 650 1.21 [10]
    600 0.87
    700 1.64
    Pr0.5Ba0.5Co0.7Fe0.25Sn0.05O3-δ (PBCFS05) BZCYYb Ni-BZCYYb 6–7 650 1.33 [53]
    600 1.12
    700 1.45
    PrBaCo1.92Zr0.08O5+δ (PBCZ) BZCYYb Ni-BZCYYb 15 650 0.99 [54]
    600 0.55
    700 1.78
    SrCo0.5Nb0.5O3-δ-Pr0.5Sr0.5Co0.9Nb0.1O3-δ (SCN-PSCN) BZCYYb Ni-BZCYYb ~10 650 1.36 [44]
    600 0.89
    700 2.04
    BaCe0.25Fe0.75O3-δ−0.75V2O3 (BCF-V75) BZCYYb Ni-BZCYYb ~20 650 1.73 [55]
    600 1.21
    700 1.69
    PrBa0.8Ca0.2Co2O6 (PBCC) BZCYYb Ni-BZCYYb 8 650 1.22 [56]
    600 0.88
    700 2.08
    PrBa0.8Ca0.2Co1.95Pd0.05O5+δ (PBCCPd) BZCYYb Ni-BZCYYb 8 650 1.41 [43]
    600 0.97
    700 1.78
    PrBa0.8Ca0.2Fe1.8Ce0.2O6-δ (PBCFC) BZCYYb Ni-BZCYYb 10 650 1.27 [57]
    600 0.87
    700 2.25
    PrBaCo1.9In0.1O5+δ (PBCIn0.10) BZCYYb Ni-BZCYYb 8 650 1.78 [25]
    600 1.33
    700 1.99
    PrBaCo1.8Nb0.1Y0.1O5+δ (PBCNY) BZCYYb Ni-BZCYYb ~8 650 1.44 [38]
    600 0.97

    To summarize, we have successfully developed a Yb-doped PBC-based air electrode with a nominal composition of PBCYb0.05. As evidenced by XRD patterns, HR-TEM images, and EDS mapping, the coexistence of D-PBCY and BCYO phases in the PBCYb0.05 material is confirmed. According to the testing of symmetrical cells and DRT analysis, the PBCYb0.05 air electrode demonstrates excellent electrocatalytic activity and operational stability. From the combined analyses of XPS and ECR, compared to PBC, PBCYb0.05 possesses more oxygen vacancies and faster oxygen transport kinetics, accounting for enhanced oxygen reduction reaction (ORR) activity. In the single-cell tests, the PCFCs loaded with PBCYb0.05 cathode achieved an ideal peak power density of 2.25 W/cm2 at 700 ℃. In addition, it also showed promising durability for 103 h during operation. The testing demonstrates that the Yb-doped PBC serves as a highly reliable air electrode for the practical applications of PCFCs. The Yb-doping strategy efficiently broadens the modification methodologies for the cathodes in PCFCs.

    Yixuan Huang: Writing – original draft, Visualization, Investigation, Data curation. Jiacheng Zeng: Software, Investigation, Data curation. Wenjie Gong: Investigation, Data curation. Wanbin Lin: Investigation, Data curation. Hao Liu: Investigation, Data curation. Chuqian Jian: Investigation, Data curation. Xiaofeng Chen: Investigation, Data curation. Tang Sheng: Investigation, Data curation. Li Zhang: Investigation, Data curation. Fan He: Investigation, Data curation. Yu Chen: Writing – review & editing, Project administration, Funding acquisition, Conceptualization.

    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.

    This work was financially supported by the National Natural Science Foundation of China (No. 22179039), the Guangdong Basic and Applied Basic Research Foundation (No. 2024A1515010448), the Introduced Innovative R&D Team of Guangdong (No. 2021ZT09L392), the Pearl River Talent Recruitment Program (No. 2019QN01C693), the Zijin Mining Group Co., Ltd. (No. 5405–ZC–2023–00008), and Guangzhou Applied Basic Research Plan Project (No. 2024A04J3079).

    Supplementary material associated with this article can be found, in the online version, at doi:10.1016/j.cclet.2025.111664.


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  • Figure 1  Phase characterization of the PBCYb0.05 powder. (a) XRD Rietveld refinement of PBCYb0.05 powder sintered at 1000 ℃ for 4 h. (b) XRD patterns of PBCYb0.05 and PBC powders sintered at 1000 ℃ for 4 h. (c) HR-TEM images of PBCYb0.05 powder. The lattice spacings and FFT images of (d) BCYO and (e) PBCYb0.05. (f) STEM image and EDS mapping of PBCYb0.05 powder with Pr, O, Ba, Yb, and Co elements.

    Figure 2  Cathode performance in symmetrical cells. (a) EIS curves of BZCYYb electrolyte-supported symmetrical cells with PBCYb0.05 air electrode tested in humid air (3 vol% H2O) at 700–500 ℃. (b) Electrocatalytic performance comparison of symmetrical cells with PBCYb0.10, PBCYb0.05, PBC, and PBCYb0.15 electrodes. (c) Area-specific resistance of PBCYb0.05 and PBC in this work relative to other materials recently reported. (d) Short-term stability of a symmetrical cell with PBCYb0.05 air electrode in humid air (3 vol% H2O) at 600 ℃. The DRT curves of symmetrical cells with (e) PBCYb0.05 and (f) PBC air electrodes during stability testing.

    Figure 3  Discussion on the mechanism of the PBCYb0.05 electrode. (a) Electrical conductivity of PBCYb0.05 and PBC samples from 400 ℃ to 775 ℃. (b) The Co 2p3/2, Ba 3d5/2 and (c) O 1s XPS spectra for PBC and PBCYb0.05 powders. (d) Column distribution of four oxygen species in PBCYb0.05 vs. PBC powders. (e) ECR response curves of PBCYb0.05 sample from 700 ℃ to 600 ℃. (f) Temperature dependence of the k*chem/D*chem for PBCYb0.05 and PBC samples.

    Figure 4  Electrochemical performance and microcosmic structure of PCFCs loaded with PBCYb0.05 and PBC cathodes. (a) The I-V-P curves and (b) impedance spectra of PCFCs loaded with PBCYb0.05 cathode from 700 ℃ to 600 ℃. (c) The cross-sectional SEM image of a single cell loaded with the PBCYb0.05 cathode after electrochemical testing. (d) Comparison of Ro and Rp of PCFCs loaded with PBCYb0.05 and PBC cathodes. (e) Operational durability of PBCYb0.05 cell at a current density of 0.5 A/cm2 and 600 ℃.

    Table 1.  Comparison of the PPDs of PBCYb0.05 and PBC cells with other recently reported cells which possess a similar construction.

    Air electrode Electrolyte Fuel electrode Electrolyte thickness (μm) Temp. (℃) PPD (W/cm2) Source
    700 2.25
    PrBaCo1.95Yb0.05O5+δ (PBCYb0.05) BZCYYb Ni-BZCYYb ~7 650 1.52 This work
    600 1.09
    700 1.68
    PrBaCo2O5+δ (PBC) BZCYYb Ni-BZCYYb ~7 650 1.22 This work
    600 0.96
    700 1.77
    Pr0.1Ce0.9O2+δ-PrBaCo2O5+δ (PCO-PBC) BZCYYb Ni-BZCYYb 8 650 1.21 [10]
    600 0.87
    700 1.64
    Pr0.5Ba0.5Co0.7Fe0.25Sn0.05O3-δ (PBCFS05) BZCYYb Ni-BZCYYb 6–7 650 1.33 [53]
    600 1.12
    700 1.45
    PrBaCo1.92Zr0.08O5+δ (PBCZ) BZCYYb Ni-BZCYYb 15 650 0.99 [54]
    600 0.55
    700 1.78
    SrCo0.5Nb0.5O3-δ-Pr0.5Sr0.5Co0.9Nb0.1O3-δ (SCN-PSCN) BZCYYb Ni-BZCYYb ~10 650 1.36 [44]
    600 0.89
    700 2.04
    BaCe0.25Fe0.75O3-δ−0.75V2O3 (BCF-V75) BZCYYb Ni-BZCYYb ~20 650 1.73 [55]
    600 1.21
    700 1.69
    PrBa0.8Ca0.2Co2O6 (PBCC) BZCYYb Ni-BZCYYb 8 650 1.22 [56]
    600 0.88
    700 2.08
    PrBa0.8Ca0.2Co1.95Pd0.05O5+δ (PBCCPd) BZCYYb Ni-BZCYYb 8 650 1.41 [43]
    600 0.97
    700 1.78
    PrBa0.8Ca0.2Fe1.8Ce0.2O6-δ (PBCFC) BZCYYb Ni-BZCYYb 10 650 1.27 [57]
    600 0.87
    700 2.25
    PrBaCo1.9In0.1O5+δ (PBCIn0.10) BZCYYb Ni-BZCYYb 8 650 1.78 [25]
    600 1.33
    700 1.99
    PrBaCo1.8Nb0.1Y0.1O5+δ (PBCNY) BZCYYb Ni-BZCYYb ~8 650 1.44 [38]
    600 0.97
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  • 发布日期:  2026-09-15
  • 收稿日期:  2025-06-19
  • 接受日期:  2025-07-31
  • 修回日期:  2025-07-30
  • 网络出版日期:  2025-08-05
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