Accelerated Stress Testing of Solid Oxide Electrolysis Cells in a Symmetric Steam-Rich Atmosphere

Christian Rose, Luca Mastropasqua, Jack Brouwer
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It is desirable to understand the process by which these phenomena occur not only to minimize it, but to intentionally induce it to develop accelerated stress test protocols for cell lifetime prognostics. The degradation of solid oxide electrolyzers has been reported to be accelerated by certain stressful operating conditions. Brisse and Mocotuguy conducted a review of the degradation mechanisms of solid oxide button cells; they reported that high steam partial pressures can lead to the formation of nickel hydroxide at the cathode, which then diffuse to the surface of YSZ 1 . Sun et al. hypothesize that this is the main mechanism for nickel migration, due to the positive oxidation state of nickel and the direction of the electric potential 2 . Changes in the surface morphology of the fuel electrode due to redox cycle-induced degradation has been reported, showing the dynamics of nickel migration and agglomeration under these conditions 3 . Redox cycling was found to be a destructive test protocol; efforts are currently being made by the group of Daria Vladikova to prevent fracturing of the electrodes and electrolyte during such stressful testing 4 . Königshofer et al. have reported through multiple investigations that protocols inducing operation at high steam conversion rates (>90%) and large current densities (0.8 A/cm 2 ) have been effective at reproducing long-term SOEC voltage degradation 5,6 . The objective of this research is to establish a protocol that will help determine the causes that trigger Ni migration or evaporation, and that will mimic the electrode degradation mechanism to standardize the procedure for comparing the long-term performance of solid oxide electrolysis cells. Symmetric button cells of various fuel electrode chemistries with a diameter of 20 mm (active area 1.23 cm 2 ) are tested under symmetric atmospheres with steam/H 2 blends. The following two accelerated stress tests (AST) protocols are employed: cycling of steam partial pressure and cycling of current density. In the former, the steam molar fraction is varied from 75% to 95% in a 20-minute cycle for at least 400 cycles (i.e., 1,176 h). In the latter protocol, current density is controlled using a galvanodynamic 10-minute long cyclic ramp profile between 0.8 A/cm 2 and 1.5 A/cm 2 at a constant steam molar fraction between 75-95% for at least 800 cycles (i.e., 1,176 h). For all tests, the cells are operated at a constant furnace temperature between 700°C and 850°C. The performance characteristics of the various cells are expressed in terms of electrochemical impedance spectroscopy (EIS) and polarization curves every 12 h during the AST. X-ray diffraction (XRD) and fluorescence (XRF) are used to analyze the cells at beginning of life and post-mortem to identify phase changes which occur during operation. Scanning Electron Microscopy - Energy Dispersion Spectroscopy (SEM-EDS) and Glow-discharge spectroscopy (GD) are used to identify and map the nickel concentration on the cathode surface and cross-section. Preliminary results suggest that the high frequency resistance may increase by nearly 500% under a constant high-steam condition (> 90%) in a Ni-YSZ|YSZ|Ni-YSZ cell during a 200 h operation. P. Moçoteguy and A. Brisse, Int J Hydrogen Energy , 38 , 15887–15902 (2013). X. Sun, T. L. Skafte, and S. H. Jensen, Fuel Cells (2021). S. Yang et al., J Alloys Compd , 921 , 166085 (2022). D. Vladikova et al., Energies (Basel) , 15 (2022). B. Königshofer et al., J Power Sources , 523 (2022). B. Königshofer et al., J Power Sources , 497 (2021).","PeriodicalId":11461,"journal":{"name":"ECS Meeting Abstracts","volume":null,"pages":null},"PeriodicalIF":0.0000,"publicationDate":"2023-08-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"ECS Meeting Abstracts","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1149/ma2023-0154187mtgabs","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
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Abstract

Temperature, current density, steam utilization variability, and local steam starvation or excess may cause diverse degradation processes to occur in solid oxide electrolysis cells. Typical degradation mechanisms for SOEC with nickel-based fuel electrode materials include nickel migration/evaporation and agglomeration, which may lead to reduced active sites at the triple-phase boundary. However, the phenomenological cause of such degradation mechanisms is still actively debated, making the selection of a durable fuel electrode material challenging. It is desirable to understand the process by which these phenomena occur not only to minimize it, but to intentionally induce it to develop accelerated stress test protocols for cell lifetime prognostics. The degradation of solid oxide electrolyzers has been reported to be accelerated by certain stressful operating conditions. Brisse and Mocotuguy conducted a review of the degradation mechanisms of solid oxide button cells; they reported that high steam partial pressures can lead to the formation of nickel hydroxide at the cathode, which then diffuse to the surface of YSZ 1 . Sun et al. hypothesize that this is the main mechanism for nickel migration, due to the positive oxidation state of nickel and the direction of the electric potential 2 . Changes in the surface morphology of the fuel electrode due to redox cycle-induced degradation has been reported, showing the dynamics of nickel migration and agglomeration under these conditions 3 . Redox cycling was found to be a destructive test protocol; efforts are currently being made by the group of Daria Vladikova to prevent fracturing of the electrodes and electrolyte during such stressful testing 4 . Königshofer et al. have reported through multiple investigations that protocols inducing operation at high steam conversion rates (>90%) and large current densities (0.8 A/cm 2 ) have been effective at reproducing long-term SOEC voltage degradation 5,6 . The objective of this research is to establish a protocol that will help determine the causes that trigger Ni migration or evaporation, and that will mimic the electrode degradation mechanism to standardize the procedure for comparing the long-term performance of solid oxide electrolysis cells. Symmetric button cells of various fuel electrode chemistries with a diameter of 20 mm (active area 1.23 cm 2 ) are tested under symmetric atmospheres with steam/H 2 blends. The following two accelerated stress tests (AST) protocols are employed: cycling of steam partial pressure and cycling of current density. In the former, the steam molar fraction is varied from 75% to 95% in a 20-minute cycle for at least 400 cycles (i.e., 1,176 h). In the latter protocol, current density is controlled using a galvanodynamic 10-minute long cyclic ramp profile between 0.8 A/cm 2 and 1.5 A/cm 2 at a constant steam molar fraction between 75-95% for at least 800 cycles (i.e., 1,176 h). For all tests, the cells are operated at a constant furnace temperature between 700°C and 850°C. The performance characteristics of the various cells are expressed in terms of electrochemical impedance spectroscopy (EIS) and polarization curves every 12 h during the AST. X-ray diffraction (XRD) and fluorescence (XRF) are used to analyze the cells at beginning of life and post-mortem to identify phase changes which occur during operation. Scanning Electron Microscopy - Energy Dispersion Spectroscopy (SEM-EDS) and Glow-discharge spectroscopy (GD) are used to identify and map the nickel concentration on the cathode surface and cross-section. Preliminary results suggest that the high frequency resistance may increase by nearly 500% under a constant high-steam condition (> 90%) in a Ni-YSZ|YSZ|Ni-YSZ cell during a 200 h operation. P. Moçoteguy and A. Brisse, Int J Hydrogen Energy , 38 , 15887–15902 (2013). X. Sun, T. L. Skafte, and S. H. Jensen, Fuel Cells (2021). S. Yang et al., J Alloys Compd , 921 , 166085 (2022). D. Vladikova et al., Energies (Basel) , 15 (2022). B. Königshofer et al., J Power Sources , 523 (2022). B. Königshofer et al., J Power Sources , 497 (2021).
对称富蒸汽大气中固体氧化物电解槽的加速应力测试
温度、电流密度、蒸汽利用率可变性和局部蒸汽缺乏或过剩可能导致固体氧化物电解池中发生不同的降解过程。镍基燃料电极材料对SOEC的典型降解机制包括镍的迁移/蒸发和团聚,这可能导致三相边界活性位点的减少。然而,这种降解机制的现象学原因仍然存在争议,这使得选择耐用的燃料电极材料具有挑战性。我们希望了解这些现象发生的过程,不仅是为了尽量减少它,而且是为了有意地诱导它来开发用于细胞寿命预后的加速压力测试方案。据报道,固体氧化物电解槽的降解在一定的高压操作条件下会加速。Brisse和Mocotuguy对固体氧化物纽扣电池的降解机制进行了综述;他们报告说,高蒸汽分压会导致阴极形成氢氧化镍,然后扩散到ysz1的表面。Sun等人假设这是镍迁移的主要机制,由于镍的正氧化态和电势2的方向。据报道,由于氧化还原循环引起的降解,燃料电极表面形貌发生了变化,显示了在这些条件下镍迁移和团聚的动力学。发现氧化还原循环是一种破坏性的试验方案;达里亚·弗拉迪科娃(Daria Vladikova)小组目前正在努力防止在这种压力测试中电极和电解质破裂。Königshofer等人通过多次调查报道,在高蒸汽转化率(>90%)和大电流密度(0.8 A/ cm2)下诱导操作的方案有效地再现了长期的SOEC电压退化5,6。本研究的目的是建立一个方案,以帮助确定触发Ni迁移或蒸发的原因,并将模拟电极降解机制,以标准化比较固体氧化物电解电池长期性能的程序。在蒸汽/ h2混合物的对称气氛下,对直径为20mm(活性面积1.23 cm 2)的各种燃料电极化学的对称纽扣电池进行了测试。采用了蒸汽分压循环和电流密度循环两种加速应力测试(AST)协议。在前,蒸汽摩尔分数从75%变化到95% 20分钟周期至少400周期(例如,1176 h)。在后一种协议,电流密度控制使用galvanodynamic 10分钟长循环斜坡剖面/厘米2 0.8和1.5之间以恒定的蒸汽/厘米2摩尔分数在75 - 95%之间至少800个周期(即1176 h)。对于所有的测试,细胞在一个常数炉温700°C到850°C。在AST过程中,用电化学阻抗谱(EIS)和每隔12 h的极化曲线来表达各种细胞的性能特征,用x射线衍射(XRD)和荧光(XRF)分析细胞在生命初期和死亡后的状态,以识别运行过程中发生的相变。扫描电子显微镜-能量色散光谱(SEM-EDS)和辉光放电光谱(GD)用于识别和绘制阴极表面和横截面上的镍浓度。初步结果表明,在恒定高蒸汽条件下,高频电阻可提高近500% (>90%)在Ni-YSZ|YSZ|Ni-YSZ电池中工作200小时。张建军,张建军,张建军,等。氢能与氢能的关系[J] .能源工程学报,2003,19(3):557 - 557(2013)。Sun, T. L. Skafte和S. H. Jensen,燃料电池(2021)。杨士林等,合金材料学报,1999,16(6):444 - 444。D. Vladikova等人,能源(巴塞尔),15(2022)。B. Königshofer et al., J Power Sources, 523(2022)。B. Königshofer et al., J Power Sources, 497(2021)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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