Synthesis and Evaluation of Ca-doped Sr2Fe1.5Mo0.5O6–δ as Symmetrical Electrodes for High Performance Solid Oxide Fuel Cells

XIA Tian, MENG Xie, LUO Ting, ZHAN Zhong-Liang

Synthesis and Evaluation of Ca-doped Sr2Fe1.5Mo0.5O6–δas Symmetrical Electrodes for High Performance Solid Oxide Fuel Cells

XIA Tian1,2, MENG Xie1, LUO Ting1, ZHAN Zhong-Liang1

(1. CAS Key Laboratory of Materials for Energy Conversion, Shanghai Institute of Ceramics, Chinese Academy of Sciences, Shanghai 200050, China; 2. University of Chinese Academy of Sciences, Beijing 100049, China)

A series of Ca-substituted Sr2Fe1.5Mo0.5O6–δoxides, Sr2–xCaFe1.5Mo0.5O6–δ(SCFMO,=0, 0.2, 0.4 and 0.6), were synthesized and evaluated as potential electrodes for symmetrical solid oxide fuel cells. X-ray diffraction examination showed that all samples maintained cubic perovskite structure in both air and wet hydrogen atmospheres. Temperature programmed reduction measurements indicated that the Ca2+substitution promoted the catalytic activity of SCFMO toward oxygen evolution reactions. Symmetrical anode fuel cell measurements showed the lowest polarization resistance in humidified hydrogen emerged at=0.6. Single cells-SC0.6FMO|La0.9Sr0.1Ga0.8Mg0.2O3(LSGM)|SC0.6FMO, fabricatedtape-casting and impregnation methods, produced peak power densities of 1.05 W·cm–2at 800 ℃ and 0.41 W·cm–2at 650 ℃ when operating on hydrogen fuels and air oxidants. These results demonstrate SC0.6FMO is a potential electrode material for symmetrical solid oxide fuel cells.

Symmetrical Solid Oxide Fuel Cells; perovskite; electrode materials

Solid Oxide Fuel Cells (SOFCs) have attracted considerable attention as a promising power generation technology due to their high efficiencies and low emissions[1-3]. However, high manufacturing cost and poor long-term stability prevent their widespread implementation. SOFCs were typically composed of three ceramic components: a porous anode, a porous cathode and the dense electrolyte sandwiched between two electrodes to separate fuels from air[4]. Different materials were usually adopted for anode and cathode due to their different requirements, resulting in at least two separate thermal processing steps for fabrication of single cells. Recently, some materials appeared suitable as both electrodes in the symmetrical SOFCs (SSOFCs)[5]. Compared with the traditional SOFCs, SSOFCs showed advantages of simplified production process, reduced manufacturing cost as well as improved thermo-mechanical compatibility with only one type of interface present[6]. Nonetheless, the very different operating conditions of anodes and cathodes posed harsh requirements on the symmetrical electrodes. For example, the symmetrical electrode materials should show adequate chemical stability and acceptable electronic conductivities in both the oxidizing and re-ducing atmospheres with high catalytic activities towards both oxygen reduction and fuel oxidation reactions[7-8].

Until now, only a few number of oxides could fulfil almost all requirements for symmetrical electrodes. In particular, LaCrO3based perovskite exhibited good stability and conductivities over a wide range of oxygen partial pressures. Partial substitution of Ca or Sr in the A-site, and Mn or Fe in the B-site yielded promising symmetrical electrodes such as La0.7Ca0.3Cr0.97O3[9], La0.75Sr0.25Cr0.5Mn0.5O3[10], and La0.75Sr0.25Cr0.7Fe0.3O3[11]with good catalytic activities for both electrode reactions. Maximum power densities of 300 mW·cm–2were achieved in humidified hydrogen for the symmetrical La0.75Sr0.25Cr0.5Mn0.5O3electrode fuel cells at 900 ℃[10]. La(Sr)TiO3-based oxide were usually used as anodes due to their high conductivities in hydrogen and excellent catalytic activities for hydrogen oxidation reactions. Doping Fe or Co in the B-site substantially improved their conductivities under oxidizing atmospheres. La4Sr8Ti6Fe6O38–δ[12]and La0.5Sr0.5Ti0.5Co0.5O3–δ(LSTC)[13]were explored as symmetrical electrodes with maximum power densities of 110 mW·cm–2obtained at 800 ℃ for symmetrical cells-LSTC|LSGM|LSTC[13]. Alternatively, introducing the chemically stable metal element Mo in the B-site of commonly used SOFC cathodes could also enhance their structural stability under highly reducing anode atmospheres, e.g., SrFe0.75Mo0.25O3–δ(SFMO)[14]. Power densities as high as 0.83 W·cm–2were achieved at 900 ℃ for symmetrical SFMO electrode fuel cells in hydrogen fuels[15]. Optimizing the cell microstructureliquid infiltration technique[16]or phase inversion method[17]could further improve the cell performance.

Modification of the electrode materials by metal substitution or doping while maintaining the original crystal structure may also improve the cell performance[6,18]. It was reported that partial substitution of Ca2+for Sr2+changed the cationic valence and oxygen-vacancy concentration, yielding increase of electrical conductivity and reduction of cathode polarization resistance in air[19]. Here, partial substitution of Sr2+in SFMO by Ca2+was explored with the aim of improving their performance as the symmetrical electrodes. A series of samples Sr2–xCaFe1.5Mo0.5O6–δ(SCFMO,=0, 0.2, 0.4 and 0.6) were synthesized and their structural stabilities in hydrogen were examined. The chemical stability and the catalytic activities toward oxygen evolution reactions (OER) of SCFM in hydrogen were evaluated by temperature programmed reduction. Thin LSGM electrolyte fuel cells with symmetrical SCFMO electrodes were fabricated by tape casting and liquid impregnation methods. The structures and electrochemical characteristics of single cells were examined to explore their potential applications in SSOFCs.

1 Experimental

The Sr2–xCaFe1.5Mo0.5O6–δ(=0, 0.2, 0.4 and 0.6) powders were synthesizedSol-Gel method[20]. Stoichiometric amounts of Sr(NO3)2, Ca(NO3)2, Fe(NO3)3·9H2O and (NH4)6Mo7O24·4H2O were dissolved in deionized water with addition of citric acid to form the SCFMO precursor solution. The precursor solutions were evaporated at 80 ℃ to form gel. The gel was then dried at 250 ℃for 10 h to obtain dry precursor followed by calcination at 1100 ℃ in air for 5 h to obtain the final SCFMO pow-ders. Crystal structure of the as-synthesized and hydrogen- reduced powders were examined by X-ray diffractometer (XRD, Rigaku Smartlab9, Japan) at room temperature. Temperature-programmed reduction (TPR, Micromeritics ChemiSorb 2720) measurements were carried out to ana-lyze the catalytic activity of SCFMO anodes. 60~80 mg SCFMO powders were loaded into the quartz U-tube. After being pre-treated with high-purity He flow at 450 ℃ for 30 min, the samples were measured under 5vol% H2/He (20 mL·min–1) flow with a linear heating rate of 10 ℃?min–1from room temperature up to 850 ℃.

Symmetrical fuel cells were fabricated with thin LSGM electrolytes and SCFMO catalysts, based upon the “porous|dense|porous” LSGM tri-layer backbones. Powders of LSGM (Praxair) and rice starch used as the fugitive material for the porous layers were ball-milled in a weight ratio of 60:40 for 12 h with appropriate amounts of dispersant, binder, plasticizer and solvent. The tri-layer structures were produced by laminating three tape-cast ceramic green tapes with subsequent co-firing at 1400 ℃ to produce the final ceramic structures. The electrode catalysts SCFMO were added by liquid infiltration method. The precursor solutions were simultaneously impregnated into both porous LSGM backbones, and then calcined at 700 ℃ for 30 min. The impregnation- calcination procedure was repeated until catalyst loading achieved 25wt% relative to the porous LSGM backbones, with a final calcination at 850 ℃ for 2 h to obtain the symmetrical cells. The cross-sectional morphologies of single cells were examined using the scanning electron microscopy (SEM, FEI Inspect F50, USA).

For electrochemical measurement at 650–800 ℃, the symmetrical cells were sealed to alumina tubes using ceramic adhesive (Aremco, Ultra-Temp 552). Current- voltage curves (-) and electrochemical impedance spectra (EIS) were obtained by using Electrochemical Workstation (ZAHNER IM6e, Germany) with the cathode exposed to dry air (100 mL?min–1) and the anode to humidified (3vol% H2O) hydrogen (100 mL?min–1). To determine the individual electrode polarization resis-tances, impedance measurements were also performed on symmetrical cells in homogeneous environments,., in dry air for symmetrical cathode cells and in humidified (3vol% H2O) hydrogen for symmetrical anode cells. The impedance data were recorded at open circuits over the frequency range from 0.1 Hz to 100 kHz with a 20 mV AC perturbation.

2 Results and discussion

Fig. 1(a) summarized the room temperature XRD patterns of as-synthesized SCFMO powders, showing cubic perovskite crystal structure for all powders as previously reported[19]. In order to examine their structural stability as the SOFC anode, these powders were thermally treated in 97vol% H2–3vol% H2O at 800 ℃ for 4 h, with XRD patterns of the reduced powders summarized in Fig. 1(b). Notably, the cubic perovskite structures for all samples were well maintained with little impurities detected, indicating that SCFMO oxides could be adopted as the symmetrical electrodes in SOFCs. The magnified XRD patterns at 67.5° in Fig. 1(c) showed that the peak shifted toward higher angle with Ca2+substitution increasing, due to smaller ionic radius of Ca2+compared with Sr2+. Fig. 1(c) also showed increased lattice parameter after reduction in hydrogen due to the reduction of Fe and Mo elements as previously reported for the SFMO-based oxides[21].

Fig. 1 XRD patterns of Sr2–xCaxFe1.5Mo0.5O6–δ powders synthetized in air (a) and reduced in humidified hydrogen (b) at 800 ℃ for 4 h; (c) Magnified view of the diffraction peak at 67.5°

Temperature programmed reduction measurements were used to evaluate the stability and catalytic activities of the SCFMO anode materials. Fig. 2 showed the TPR profiles of all SCFMO samples, showing only one peak for the pure SFMO and two peaks for the Ca2+-substituted samples. Similar profiles were observed by Xiao,[22]and Wang,[23]in the TPR curves of SFMO materials, related to reduction of Fe3+and Mo6+. Kubo,[24]assigned the ~550 ℃ peak to the red-uction of AMoVIO4 to AMoIVO3. Thus it was reason-able to attribute the peaks at ~490 and ~550 ℃ in TPR curves to reductions of Fe3+and Mo6+, respectively. TPR curves shifted towards lower temperature with increasing substitution of Ca2+, indicative of enhanced OER catalytic activity[23]. Furthermore, no reduction peak reflecting the formation of metal Fe was observed in the TPR profiles, confirming the structural stability of all the SCFMO oxides in hydrogen as consistent with the XRD results.

Fig. 2 Measured H2-TPR profiles for Sr2–xCaxFe1.5Mo0.5O6–δ powders with a ramp rate of 10 ℃·min?1

Fig. 3(a) showed SEM micrograph of the thin LSGM electrolyte fuel cell with symmetrical SCFMO electrodes. The LSGM electrolyte layer was fully dense with ~35 μm thickness. Higher-magnification micrograph (Fig. 3(b)) of the impregnated composite electrode showed a homogeneous distribution of 70 nm SCFMO catalysts on the internal surfaces of the porous LSGM backbones. Fig. 3(b)also showed well-connected catalysts and sufficient porosities that were conducive to current collection and gas transport.

The catalytic activities of SCFMO nano particles toward hydrogen oxidation at the anode and oxygen reduction at the cathode were evaluated by electrochemical impedance spectroscopy (EIS). Fig. 4(a) showed Nyquist plots of impedance data measured on the symmetrical anode cells at 800 ℃ in the homogeneous environment of 97vol% H2–3vol% H2O, where the ohmic resistances were omitted for easy comparison among different samples. The anode polarization resistances (,) were 0.23, 0.21, 0.20 and 0.18 Ω?cm2for SCFMO at= 0, 0.2, 0.4 and 0.6, respectively. Fig. 4(b) showed the temperature dependence of the,value on the substitution amounts of Ca2+.,decreased with the Ca2+substitution increasing over the whole temperature range from 650 to 800 ℃ with the minimized,values observed at=0.6. Moreover, the slope of Arrhenius plots in Fig. 4(b) also decreased with increasing Ca2+substitution. The activation energy decreased from 0.93 to 0.77 eV, which were slightly smaller than 1.07 eV in previous report[25]. These results indicated that Ca2+substitution could effectively enhance the anode catalytic activities with reduced anode polarization resistances, especially at lower temperatures.

Fig. 3 Cross-sectional SEM micrographs showing impregnated fuel cells

(a) Low magnification; (b) High magnification

Fig. 4 (a) EIS plots of the Sr2–xCaxFe1.5Mo0.5O6–δ symmetrical cells measured in humidified hydrogen at 800 ℃, and (b) Arrhenius plots of the anode polarization resistances over the temperature range of 650–800 ℃

Fig. 5(a) showed Nyquist plots of impedance data measured on the symmetrical cathode cells at 800 ℃ in homogeneous air environment. The cathode polarization resistances (,) were 0.104, 0.056, 0.058 and 0.077 Ω·cm2at=0, 0.2, 0.4 and 0.6, respectively. Fig. 5(b) showed the temperature dependence of the,value on the substitution amounts of Ca2+at 650–800 ℃. Minimized,values emerged at=0.2 with all tem-peratures, similar to the observation in previous report[19]. However, the slope of the curve in Arrhenius plots was close to each other for all SCFMO cathodes, indicating that Ca2+substitution might not alter the cathode reaction mechanism. And the increase in conductivity may be the reason for improvement of cathode performance[19]. How-ever, compared with the resistance of cathode, higher anode impedance of the SCFMO electrode showed more significant impact on the cell performance, especially at lower temperatures. Although the cathode impedances of the electrode were low at=0.2, the minimum value of the total polarization impedance of the cells was achieved at=0.6.

Fig. 5 (a) EIS plots of the Sr2–xCaxFe1.5Mo0.5O6–δsymmetrical cells measured in air at 800 ℃, and (b) Arrhenius plots of the cathode polarization resistances over the temperature range of 650–800 ℃

Fuel cell performances were measured in humidified hydrogen fuels and dry air oxidants both at a flow rate of 100 mL?min–1. Fig. 6(a) showed the polarization curves of the cell voltages () and power densities () as a fun-ction of current densities () measured over 650–800 ℃ for the symmetrical SCFMO electrodes with=0.6. The open circuit voltage (OCV) values increased from 1.103 V at 800 ℃ to 1.127 V at 650 ℃, which were close to the theoretical values (1.12–1.15 V) calculated from Nernst equation over the very temperature range. The maximum power densities were 1.05, 0.88, 0.66 and 0.41 W·cm–2at 800, 750, 700 and 650 ℃, respectively. Fig. 6(b) showed Nyquist plots of impedance data obtained at open circuit, and the combined anode and cathode interfacial polarization resistances were 0.155, 0.179, 0.230 and 0.359 ?·cm2at 800, 750, 700 and 650 ℃, respectively. The polarization impedance and the ohmic impedance increased gradually with the operating temperature decreasing in Nyquist plots, indicating decrease in the catalytic activity of the electrodes and the electrical conductivity of the electrolyte. Compared with our prior symmetrical SFMO electrode cells[16], the present fuel cell showed lower polarization resistance and higher power density, even though the electrolyte of the present fuel cell in Fig. 3(a) was almost twice thick. Decreasing the electrolyte thickness will further enhance the fuel cell performance. Fig. 6(c) summarized the maximum power densities for all symmetrical fuel cells with different Ca2+substitutions at 650–800 ℃. The samples with=0.6 exhibited the highest power densities at all temperatures, in agreement with the observed total polarization impedance and the H-TPR measurements. These results demonstrate that Sr1.4Ca0.6Fe1.5Mo0.5O6–δis a kind of promising symmetrical fuel cell electrode material.

Fig. 6 (a) Voltage and power density versus current density for a symmetrical fuel cell with Sr2–xCaxFe1.5Mo0.5O6–δ(x=0.6) electrode measured in humidified hydrogen fuel and dry air over the temperature range of 650–800 ℃; (b) Nyquist plots of impedance data measured at open circuits; (c) Maximum power densities of the symmetrical SCFMO electrode cells at different Ca2+ substitutions over the temperature range of 650–800 ℃

3 Conclusion

In summary, we synthesized and evaluated a series of Sr2–xCaFe1.5Mo0.5O6–δ(=0, 0.2, 0.4 and 0.6) oxides as potential electrode catalysts for symmetrical fuel cells. These oxides maintained cubic perovskite crystal structure under both oxidizing and reducing conditions. H2-TPR measurements indicated that substituting Ca2+for Sr2+reduced the onset temperature of hydrogen oxidation reactions. Impedance analysis showed that Sr1.4Ca0.6Fe1.5Mo0.5O6–δexhibited the lowest anode polarization resistances among all samples with slighltly higher cathode polarization resistances than those of Sr1.6Ca0.4Fe1.5Mo0.5O6–δ. Fuel cell measurements also showed the highest power densities for symmetrical Sr1.4Ca0.6Fe1.5Mo0.5O6–δelectodes, e.g., 1.05, 0.88, 0.66 and 0.41 W·cm–2at 800, 750, 700 and 650 ℃, respectively. These results indicate that Ca2+substitution is effective in enhancing the catalytic activity of SFMO oxides toward hydrogen oxidation and oxygen reduction reactions, and Sr1.4Ca0.6Fe1.5Mo0.5O6–δis a promising symmetrical electrode material.

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Ca摻雜Sr2Fe1.5Mo0.5O6–δ材料的合成與作為對稱固體氧化物燃料電池電極催化劑的性能研究

夏天1,2, 孟燮1, 駱婷1, 占忠亮1

(1. 中國科學院 上海硅酸鹽研究所, 能量轉換材料重點實驗室, 上海 200050；2. 中國科學院大學, 北京 100049)

對稱固體氧化物燃料電池由于生產過程簡單、成本低, 受到了研究者的廣泛關注。然而較低的電極催化性能制約了其進一步的發展。本研究利用溶膠–凝膠法合成了一系列鈣取代Sr2Fe1.5Mo0.5O6的鈣鈦礦材料(Sr2–xCaFe1.5Mo0.5O6–δ,=0, 0.2, 0.4, 0.6), 并研究了其作為對稱固體氧化物燃料電池電極催化劑的性能。X射線衍射(XRD)測試表明所有樣品在空氣與氫氣氣氛中均能保持立方鈣鈦礦結構。而在程序升溫還原(TPR)過程中, Ca2+的摻入能有效降低還原溫度, 提升其對析氧反應的催化活性。對稱陽極電池在氫氣氣氛中的測試表明, 當Ca2+的摻入量為0.6時電池極化阻抗最小。利用流延骨架與濕化學浸漬法制備了單電池SC0.6FMO|La0.9Sr0.1Ga0.8Mg0.2O3(LSGM)| SC0.6FMO。以氫氣作為燃料時, 單電池在800與650 ℃的最大功率密度分別為1.05與0.41 W?cm–2。以上結果表明Sr2–xCaFe1.5Mo0.5O6–δ可以作為高效對稱燃料電池的電極催化劑。

對稱固體氧化物燃料電池; 鈣鈦礦結構; 電極材料

TQ174

A

2019-02-13;

2019-04-22

National Natural Science Foundation of China (51672298, 51702344, 51737011); The State of Grid (SGSDJN00FZQT1700446)

XIA Tian (1993–), male, candidate of Master degree. E-mail: xiatian@student.mail.sic.ac.cn

ZHAN Zhong-Liang, professor. E-mail: zzhan@mail.sic.ac.cn

1000-324X(2019)10-1109-06

10.15541/jim20190067