Zhishan
Li
a,
Meilan
Peng
a,
Yingru
Zhao
a,
Jianhui
Li
b and
Yifei
Sun
*acd
aCollege of Energy, Xiamen University, Xiamen, Fujian 361102, China. E-mail: yfsun@xmu.edu.cn
bNational Engineering Laboratory for Green Chemical Productions of Alcohols, Ethers and Esters, College of Chemistry and Chemical Engineering, Xiamen University, Xiamen, Fujian 361005, China
cShenzhen Research Institute of Xiamen University, Shenzhen, Guangdong 518057, China
dState Key Laboratory of Physical Chemistry of Solid Surfaces, College of Chemistry and Chemical Engineering, Xiamen University, Xiamen, Fujian 361005, China
First published on 15th November 2021
The mismatch of thermal expansion coefficients (TECs) between cobalt-containing perovskite air electrodes and electrolytes is a great challenge for the development of thermo-mechanically durable solid oxide cells (SOCs). In this work, we propose a facile design principle to directly grow highly dispersed Co reactive sites onto ion-conducting scaffolds and confine the dimension of active centres within nanoscale. As a representative, the Co-socketed BaCe0.7Zr0.2Y0.1O3−δ perovskite (denoted as R-BCZY-Co) was constructed via a consecutive sol–gel and in situ exsolution approach. Combined XRD, H2-TPR, SEM and TEM results confirm the emergence of Co nanoparticles on a BCZY matrix without the segregation of a secondary Co-rich phase. The symmetric half-cell measurement suggests that R-BCZY-Co air electrode with the optimal Co content of 10 mol% exhibits a 7-fold promoted oxygen activation performance with a polarization resistance of ∼0.17 Ω cm2 at 750 °C. The TEC mismatch between fabricated R-BCZY-Co electrodes and BCZY electrolytes is minimized down to only ∼11.4%, which is significantly lower than that of other representative counterparts. Moreover, the detailed XPS result proves that the architecture of exsolved Co on BCZY possesses a higher concentration of surface oxygen vacancy, which further benefits the kinetics of ion diffusion and oxygen absorption.
Currently, cobalt-containing perovskites are the most widely investigated air electrodes for SOCs.5–8 However, the huge mismatch in thermal expansion coefficients (TECs) between air electrodes and electrolytes is still the biggest issue hindering the commercialization of SOCs.9 For example, the TECs of representative proton-conducting electrolytes, BZCY (BaZr0.1Ce0.7Y0.2O3−δ) and BCZYYb (BaCe0.7Zr0.1Y0.1Yb0.1O3−δ), were measured to be in the range of 9–13 × 10−6 K−1,3,10 while Co-based air electrode materials such as La0.6Sr0.4Co0.2Fe0.8O3−δ (LSCF) and Ba0.5Sr0.5Co0.8Fe0.2O3−δ (BSCF) obtain TECs falling in the range of 20–25 × 10−6 K−1.11,12 The greater TEC of Co-based perovskites is due to the larger radius of Co ions after thermal reduction (Co4+, 0.068 nm; Co3+, 0.075 nm; Co2+, 0.088 nm) and spin state transition.13 Such huge discrepancy of TECs results in the delamination at electrode/electrolyte interfaces and internal stress of cells, significantly reducing the thermo-mechanical stability.9 A previous study disclosed that approximately 10% of interface area would suffer from delamination when the difference in TEC between electrode and electrolyte reached 7 × 10−6 K−1.14
So far, various strategies have been developed to deal with this challenge. The cobalt-containing perovskites were directly mixed with electrolyte powders as the electrode composites to reduce the TECs.15–17 On the other hand, the defect engineering in the perovskite structure18 and the construction of cobalt-free multiphase nanocomposite19 were also reported to reduce the TECs of the air electrode. However, these results are still not perfectly satisfactory. Zhang et al. proposed a novel thermal-expansion offset strategy that a negative-thermal-expansion component (Y2W3O12) was introduced to eliminate the TEC mismatch of Co-based perovskite (SrNb0.1Co0.9O3−δ) with the electrolyte (Sm0.2Ce0.8O1.9, SDC).9 Even so, other alternative methods without introducing the secondary phase are still highly worthy of pursuing in the perspective of reduced system complexity and uncertainty.
In decade, the in situ exsolution of cation to metal in reducing condition at elevating temperature has emerged as a hot research topic for functional perovskite oxide design.20–25 Such approach endows the strong metal–oxide interface, improved agglomeration resistance and high element utilization efficiency, which is practical for the application of electrochemical/heterogeneous catalysis including solid oxide cells.25
Enlightened by this conception, herein, we demonstrate a design paradigm to manufacture the in situ exsolved Co active site–socketed BCZY heterostructure, which realizes the promotion of catalytic activity, manipulation of overall TEC of electrode and minimization of the mismatch with electrolyte, simultaneously. The Co element was preliminarily doped into the lattice of BCZY perovskite and then exsolved out as nanoparticles (NPs) evenly anchored on the surface of porous scaffold. As a result, the as-obtained composite electrode shows 7-fold enhancement in the electrochemical performance with the negligible TEC mismatch of only ∼11.4%. This study offers a new thinking for robust SOC electrode design, which has promising generality to be employed in other cell systems.
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1.5
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1. The pH value of this mixture was adjusted to ∼8 with ammonium hydroxide (NH3·H2O, Sinopharm Chemical Reagent, 25–28%). The mixture was subsequently heated to 80 °C under stirring until the solvent was vaporized and a viscous gel was formed. Afterward, the gel was heated to 170 °C for 10 h to form a sponge-like material. The resulting material was grounded and compacted into pellets, and then calcined at 1100 °C for 5 h to avoid barium volatilization.28 Similarly, BCZY-Cox was synthesized with additional Co(NO3)2·6H2O (Energy Chemical, 98%) added. The resulting mixture was also compacted into pellets and calcined at 1100 °C for 5 h to obtain BCZY-Cox powders. After reduction at 800 °C for 10 h in an atmosphere containing 5% H2/N2, the in situ exsolved Co-decorated BCZY-Cox powders (denoted as R-BCZY-Cox) were synthesized.
000) were mixed thoroughly and then pressed in a stainless-steel module with a diameter of ∼18.0 mm. The mixture was sintered at 1450 °C for 10 h in air atmosphere to densify the electrolyte. The diameter and thickness of the obtained BCZY electrolyte were ∼14.7 and ∼0.4 mm, respectively. The sintering shrinkage of the electrolyte was calculated to be ∼18.3%, indicating that the electrolyte is dense enough.
The symmetric half-cells of BZCY-Cox||BCZY||BZCY-Cox were fabricated by the screen printing method.29,30 First, a slurry of BCZY-Cox was prepared by thoroughly mixing an electrode powder and a screening glue at a weight ratio of 1
:
1.5. The glue was composed of ∼7 wt% ethyl cellulose (Acmec, Viscosity of ∼180–220) in terpineol (Xilong Chemical, AR), and an appropriate amount of butyldigol (Xilong Chemical, AR) was added to adjust the viscosity. Second, the electrode slurry was screen-printed on the two sides of BCZY electrolyte with an active area of ∼0.5 cm2 and subsequently sintered at 1100 °C for 5 h in air atmosphere. After reduction at 800 °C for 10 h in an atmosphere containing 5% H2/N2, the obtained half-cells were denoted as R-BZCY-Cox||BCZY||R-BZCY-Cox. The BCZY||BCZY||BCZY symmetric half-cell was also fabricated as a reference by screen-printing a pure BCZY slurry on the two sides of BCZY electrolyte. Finally, the Ag paste was painted onto the surface of electrode as a current collector and Ag wires were used as current collectors to connect the symmetric half-cell with the electrochemical workstation (Wuhan Corrtest Instruments, CS2350H). Ag wires were fixed to the Ag paste using a silver conducting resin (Shanghai Institute of Synthetic Resin, DAD87).
For the van der Pauw DC conductivity test, the electrode slurry was screen-printed on only one side of BCZY electrolyte with an active area of ∼0.5 cm2, followed by calcination at 1100 °C for 5 h in air atmosphere. Four Ag wires were mounted on the surface of electrode layer by introducing four contact points with an inscribed square formed. The calculation of electrode conductivity was reported in the literature.31
Furthermore, the H2-TPR measurement was employed to investigate the reducibility of BCZY-Cox with pure BCZY as a reference. It can be seen from Fig. 1(d) that the weak H2 consumption peaks at ∼600 and ∼730 °C are ascribed to the reduction of Ce4+ to Ce3+ in BCZY, which is in agreement with the result reported by He et al.35 For BCZY-Cox (x = 0.025, 0.05, 0.075, 0.10, 0.15 and 0.20) samples, there are two extra H2 consumption peaks at 360–400 and 420–470 °C, which are related to the reduction of Co3+ to Co2+ and Co2+ to Co0, respectively.36,37 As the Co-doping amount increases, the reduction peak areas become greater, indicating that a larger amount of Co with high valence state are reduced. Based on the H2-TPR results, it is concluded that the condition of 800 °C for 10 h in an atmosphere containing 5% H2/N2 is sufficient to trigger the reduction of Co ions and the exsolution of Co NPs.
Fig. S2† provides the morphological information of all the R-BZCY-Cox samples. As illustrated by the example of R-BCZY-Co0.10 (Fig. 2(a) and Fig. S2(a–f)†), the widely dispersed pinned Co NPs are clearly observed on all the surface of reduced samples and the particle sizes are in the range of 30–100 nm. The amount of Co NPs on R-BZCY-Co0.025 is small as compared to the other counterparts, which can be explained by its trace Co-doping amount. The Co 2p XPS spectra of samples before/after reduction are shown in Fig. 2(b) and Fig. S3.† The Co 2p3/2 peaks located at ∼779.5 and ∼781.9 eV are assigned to Co3+ and Co2+, respectively. While an additional small Co 2p3/2 peak appears at ∼777.0 eV for the reduced sample, suggesting the appearance of Co0, which is in agreement with the results reported in literatures for Co exsolution.38,39 The TEM and HAADF-STEM images and the corresponding EDS elemental mappings of R-BCZY-Co0.10 shown in Fig. 2(c) further corroborate the emergence of metallic Co NPs. Apparently, the Ba, Ce, Zr, Y, O and Co species are evenly dispersed well on the bulk of R-BCZY-Co0.10, with bright spots on Co mapping only.
Fig. 3(a) presents the thermal expansion curves and TECs of BCZY electrolytes and BCZY-Cox electrodes measured ranging from 200 to 1000 °C in air. The average TEC of BCZY is measured to be ∼9.6 × 10−6 K−1, which is close to ∼10.2 × 10−6 K−1 of BZCY40 and ∼9.5 × 10−6 K−1 of BCZYYb.3 The average TECs of BCZY-Cox are in the range of ∼10.2–11.4 × 10−6 K−1, leading to the calculated discrepancy of TECs between the electrolyte and the electrode to be ∼0.7–1.9 × 10−6 K−1. This result is much smaller than 7.0 × 10−6 K−1, the reported threshold for interface delamination.14Fig. 3(b) summarizes the reported TECs of electrolytes and Co-based electrodes in literatures.1,3,11,12,40–52 Generally, the TECs of typical SOC electrolytes are in the range of 9–13 × 10−6 K−1, significantly smaller than 15–24 × 10−6 K−1 of Co-based electrodes. The huge differences of TECs are in the range of 5–12 × 10−6 K−1, leading to the risk of thermal-mechanical instability. The calculated TEC mismatches between representative electrolytes and electrodes are further presented in Fig. 3(c).1,11,44–46,49,50,53 It can be seen that the TEC mismatches shown in our work are all below 20% and the minimum one is even as low as ∼6.2%. While the TEC mismatches reported in literatures are generally above 50% with the smallest value of ∼26% between the YBaCo2O5+δ electrode and the Gd0.1Ge0.9O1.95 electrolyte.50 Hence, the negligible TEC mismatch reported in our work ensures a good contact between electrode and electrolyte for future long-term operation.
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| Fig. 3 (a) Thermal expansion (dL/L0) curves and TEC values of the BCZY electrolyte and BCZY-Cox electrodes in the temperature range of 200–1000 °C in air. (b) Summary of TECs of representative electrodes and electrolytes reported in the literature. (c) Calculated TEC mismatches between reported electrolytes and electrodes. The numbers in (b) and (c) correspond to the number of literatures in references. Tables S2 and S3† list the electrolytes and Co-based electrodes in (b) and (c), respectively. | ||
The electrochemical performance of R-BCZY-Cox||BCZY||R-BCZY-Cox symmetric half-cells was tested at an elevated temperature in air, and all the EIS data were analysed by an equivalent circuit model. The representative fitting EIS results of R-BCZY-Co0.10||BCZY||R-BCZY-Co0.10 at 650 °C in air are shown in Fig. 4(a). This model contains four R–Q elements, and the Nyquist and Bode plots are divided into four parts corresponding to high frequency (HF), middle frequency (MF1 and MF2) and low frequency (LF). The fitting results exhibit a good match with the experimental data.
Fig. S5† shows the electrochemical performance of BCZY||BCZY||BCZY symmetric half-cell at 750–550 °C in air. It is found that the total polarization resistance (Rp) of BCZY symmetric cell is as high as ∼1.2, ∼3.5 and ∼7.2 Ω cm2 at 750, 700 and 650 °C, respectively, indicating the catalytically inert property of BCZY. Fig. 4(b) illustrates the EIS results of R-BCZY-Co0.10||BCZY||R-BCZY-Co0.10 and BCZY-Co0.10||BCZY||BCZY-Co0.10 cells at different temperatures. The Rp value of the R-BCZY-Co0.10 symmetric cell measured at 750 °C was determined to be ∼0.17 Ω cm2, which is ∼30% smaller than ∼0.23 Ω cm2 of the BCZY-Co0.10 symmetric cell, and even only 1/7 of that of the BCZY symmetric cell. Excitingly, this value is comparable to other representative Co-based perovskite electrodes reported in literatures,14,45,55–61 as listed in Table 1. The Rp values of R-BCZY-Co0.10 symmetric cell measured at 700, 650, 600 and 550 °C are all smaller than those of BCZY-Co0.10 symmetric cell (∼0.6 vs. ∼0.7 Ω cm2 at 700 °C, ∼1.5 vs. ∼2.1 Ω cm2 at 650 °C, ∼4.2 vs. ∼5.5 Ω cm2 at 600 °C, and ∼11.7 vs. ∼15.5 Ω cm2 at 550 °C). Thereby, it can be inferred that the Co incorporation significantly reduces the polarization resistance of cells, and surface segregation Co sites could serve as the effective reaction centres for oxygen activation. Fig. S6† presents the evolution of polarization resistance including Rp,HF, Rp,MF1, Rp,MF2 and Rp,LF in Fig. 4(b). All the resistances increase with the decrease in temperature, and Rp,HF is the dominant polarization resistance at a temperature of 600–750 °C, but it occupies the smallest portion at 550 °C.
| Electrodes | Electrolytes | R p (Ω cm2) | Ref. | |
|---|---|---|---|---|
| 750 °C | 700 °C | |||
| R-BCZY-Co0.10 | BCZY | 0.17 | 0.60 | This work |
| La0.6Sr0.4Co0.2Fe0.8O3−δ | BCZYYb | — | 1.1 | 55 |
| Ba0.5Sr0.5Co0.8Fe0.2O3−δ | GDC | — | 0.04 | 56 |
| BaFe0.125Co0.125Zr0.75O3−δ | GDC | 0.22 | 0.33 | 14 |
| (Pr0.6Sr0.4)0.99Co0.2Fe0.8O3−δ | GDC | — | 1.6 | 45 |
| (Sm0.6Sr0.4)0.99Co0.2Fe0.8O3−δ | GDC | — | 0.50 | 45 |
| SrCoO3−δ | LSGM | — | 4.1 | 57 |
| SrCo0.8Fe0.2O3−δ | LSGM | — | 2.5 | 58 |
| Ca3Co2O6 | LSGM | 0.25 | 0.51 | 59 |
| SmBaCo1.45Mn0.5Mg0.05O5+δ | SDC | 0.40 | 0.77 | 60 |
| SmBaCo0.4Mn1.5Mg0.1O5+δ | SDC | 0.65 | 1.5 | 60 |
| PrBa0.5Sr0.5Co1.5Fe0.5O5+δ | YSZ | 0.03 | 0.04 | 61 |
Fig. S7† provides the Co content–dependent EIS results of R-BCZY-Cox||BCZY||R-BCZY-Cox (x = 0.025, 0.05, 0.075, 0.10, 0.15 and 0.20) symmetric half-cells. The Rp values of each R-BCZY-Cox symmetric cell at 750, 700 and 650 °C are summarized in Fig. 4(c) and those at 600 and 550 °C are provided in Fig. S8.† There exists an inverted volcanic relationship between the Co-doping amount and the Rp value of symmetric cells, and 10 mol% is determined to be the optimal Co doping level. As illustrated by the example of cells at 650 °C, the Rp value of R-BCZY-Co0.10 symmetric cell is ∼1.7 Ω cm2. Decreasing the Co-doping amount leads to an increase in the Rp value to ∼4.1 Ω cm2 for R-BCZY-Co0.025 symmetric cell, probably due to the less amount of Co active sites (confirmed by SEM images shown in Fig. S2(a)† and XRD patterns shown in Fig. 1(b)), while further boosting the Co-doping amount also rises the Rp value to ∼3.2 Ω cm2 for R-BCZY-Co0.20 symmetric cell.
To investigate the electrochemical processes on R-BCZY-Cox in detail, the EIS plots were further analysed by the distribution of relaxation time (DRT) method. The DRT data were calculated using the MATLAB program (named DRTtools) developed by Ciucci group.62Fig. 4(d) shows the EIS results and the corresponding DRT plots of R-BCZY-Co0.05, R-BCZY-Co0.10 and R-BCZY-Co0.15 symmetric cells at 650 °C in air. The operating temperature–dependent (750–550 °C) DRT plots of R-BCZY-Co0.10 symmetric cell are shown in Fig. S9.† All the DRT plots are deconvoluted into four typical peaks (denoted as P1–P4) in the frequency range of 10−2–105 Hz. According to the previous literatures,63,64 these four electrode reaction processes can be identified as follows. The P4 peak located in the low frequency range of 1–10 Hz is commonly assigned to the gas diffusion process in porous R-BCZY-Cox electrode. The intermediate-frequency of P3 (10–102 Hz) and P2 (102–103 Hz) are associated with chemical surface exchange of O2 and O2− bulk diffusion, respectively. The P1 at high frequency (103–104 Hz) is ascribed to the charge transfer process. The proportions of different frequency bands (i.e., P1–P4 peaks) were calculated, and are presented in Fig. S10 and S11.† Obviously, the proportion of P1 is greater than those of the other three peaks for different Co-doping amounts as well as at 750–600 °C, evidencing that the surface charge transfer process is the rate-limiting step for R-BCZY-Cox symmetric cells. When the temperature decreases to 550 °C, the gas diffusion process becomes the rate-limiting step.
As discussed in Fig. 4(d), the surface charge transfer process is the rate-determining step for R-BCZY-Cox symmetric cells, manifesting that the electrical conduction could be a crucial parameter for future material optimization. Fig. 5(c) presents the total conductivities of BCZY-Co0.10 and R-BCZY-Cox (x = 0.05, 0.10 and 0.15), which were measured in air ranging from 400 to 850 °C. It can be seen that all the Co-containing samples display a typical p-type semi-conductor behaviour.1 The measured conductivities gradually increase with the increase of temperature, indicative of the small polaron hopping mechanism.10 The conductivity of BCZY-Co0.10 is observed to be slightly greater than that of R-BCZY-Co0.10 (e.g., ∼0.042 vs. ∼0.040 S cm−1 at 600 °C, ∼0.082 vs. ∼0.076 S cm−1 at 700 °C, and ∼0.15 vs. ∼0.14 S cm−1 at 800 °C). The decrease in the conductivity of R-BCZY-Co0.10 might be due to the introduction of oxygen vacancy after the reduction treatment.67 Furthermore, the conductivities of R-BCZY-Cox at a certain temperature increase with the increase of Co-doping amount. For example, the conductivity of R-BCZY-Co0.05 at 650 °C is ∼0.04 S cm−1, and those of R-BCZY-Co0.10 and R-BCZY-Co0.15 increase to ∼0.06 and ∼0.08 S cm−1, respectively. This can be explained by the contribution of surface Co species for enhancing the electronic conductivity. The lower conductivity of R-BCZY-Co0.05 than those of R-BCZY-Co0.10 and R-BCZY-Co0.15 is consistent with the greater P1 peak area of R-BCZY-Co0.05 symmetric cell, as presented in Fig. 4(d).
The conductivity of BCZY was also evaluated by the van der Pauw DC conductivity test and the BCZY slurry was screen-printed on one side of BCZY electrolyte. However, there is no pronounced difference in conductivity between BCZY and Co-doped samples, as shown in Fig. 5(c), which fails to explain the observation that the Rp value of BCZY is 7-fold greater than that of R-BCZY-Cox. Thereby, it is concluded that the improvement of electrochemical performance for R-BCZY-Cox is mainly related to the introduction of Co as active sites rather than the conductivity.
Fig. 5(d) shows the corresponding Arrhenius plots of ln(σT) vs. 1000/T for these samples in air. According to the Arrhenius equation, the activation energies for electrical conduction were calculated by the slopes of the fitted lines. The activation energy for conductivity of BCZY was measured to be ∼0.552 eV. In comparison, the activation energies for the conductivity of BCZY-Co0.10 and R-BCZY-Cox (x = 0.05, 0.10 and 0.15) are in the range of ∼0.50–0.52 eV. which are the typical values for proton transport (0.3–0.6 eV).3 The activation energies for conductivity in this work are close to ∼0.44 eV of BaCe0.7Zr0.1Y0.1Co0.1O3−δ and ∼0.59 eV of BaCe0.7Zr0.1Y0.18Co0.02O3−δ reported by Yang et al.68
Assisted by the design principle of in situ exsolution, the direct growth of nano Co active sites onto the BCZY matrix (Fig. 1 and 2) could effectively break through the bottleneck of TEC mismatch (Fig. 3) without the trade-off of electrocatalytic performance (Fig. 4) and system simplicity. However, the ionic-conducting active/electronic-conducting inactive properties of BCZY scaffold still restrict the establishment of fast electrical conduction pathway for electron transfer, which, unfortunately, is unable to be concurrently alleviated by the exsolved nanoparticles with isolated-standing modality (Fig. 5). In future work, other strategies that could boost the electronic conduction of the materials without sacrificing other merits should be pursued.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/d1nr06845h |
| This journal is © The Royal Society of Chemistry 2021 |