La1.5Sr1.5Mn1.5Ni0.5O7 ±δ Vs La1.5Sr1.5Co1.5Ni0.5O7 ±δ: Exsolved Materials as Anodic Layers for Direct Biogas-Fueled SOFC

Sebastian Vecino-Mantilla, Massimiliano Lo Faro, Gaetano Squadrito
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Abstract

Currently, one of the main problems in commercial SOFC systems fueled directly with hydrocarbon compounds, such as biogas, is the high risk of blocking the active phase on the anode side ( e.g. Ni-YSZ ) due to carbon formation/deposition during the conversion of fuel into power energy. This issue causes a lowering in the overall performance and durability of the cell. Therefore, to overcome this deactivation mechanism, it was successfully demonstrated that an additional anodic active layer in commercial SOFC using materials based on exsoluted perovskites could be an interesting and viable alternative. This asseveration is based on the fact that using this kind of material is possible to get heterogeneous surface systems with highly stable and electrocatalytically active embedded nanoparticles uniformly distributed on the surface with a high carbon coking tolerance in a hydrocarbon fuel atmosphere. This study aimed to evaluate and compare the electrocatalytic behaviour of two new catalytic materials with Ni exsolution for direct dry biogas-fueled SOFC. The starting materials were Ruddlesden-Popper-type based on a nickel manganite (La 1.5 Sr 1.5 Mn 1.5 Ni 0.5 O 7±δ or LSMN ) and nickel cobaltite (La 1.5 Sr 1.5 Co 1.5 Ni 0.5 O 7±δ or LSCN ). Both materials have been synthesized by the Pechini method using stoichiometric amounts of precursors as nitrates. Once the respective gels have been formed, they were treated in the air at two dwell temperatures, 300°C for 2 h and 500°C for 3 h, to ensure the total elimination of the organic compounds. Finally, the resulting powders were treated in air at 1300°C for 12h and then, physicochemically characterized. For the electrochemical characterization, the as-treated powders were mixed individually with Gd 0.1 Ce 0.9 O 2 ( CGO ) in a weight ratio of 70:30 using a ball milling for 6h. Finally, to get the slurry for the coating layer, each mixture ( LSMN+CGO and LSCN+CGO ) was ground for an additional 2h in the presence of 8 wt % of triethanolamine, 2 wt % polyvinyl butyral resin (BUTVAR B-98) and 2-propanol. Commercial button SOFC cells by InDEC® (anode-supported cell Ni-YSZ/YSZ/LSM) were painted on the anode side getting an active area of 2 cm 2 . The experiments were carried out at 800°C with pre-conditioning using diluted H 2 and then, with simulated dry biogas. A Biologic tool was used as a device for the electrochemical measurements. The purpose of this communication is to present the results of experiments with two button cells derived from the same large area commercial cell (anode supporting cell) coated with the two electrocatalysts developed in this work. The electrochemical test carried out for more than 200 h demonstrated that this external functional layer on the anode side contributes to getting a stable potential within the whole working time at the selected galvanostatic conditions (500 mA cm −2 ). By comparing the results of these two tests, the exsolved LSCN layer showed better perfomances, because of the the B-site doped with Co instead of Mn which is responsible for an enhanced O 2- transport within the crystal structures. Finally, post-reaction characterization revealed minimum/null carbonous species in both cases which suggests that the classical risks caused by the direct use of hydrocarbon fuels in commercial SOFC can be suppressed with this kind of approach which would lead us to think about the use of this type of materials in a next level or further electrochemical applications. Acknowledgements The authors acknowledge the project entitled "Direct utilisation of bio-fuels in solid oxide fuel cells for sustainable and decentralised electric power production and heat (DIRECTBIOPOWER)" Grant Agreement number: 2017FCFYHK. The authors acknowledge the Ministry of Ecological Transition of Italy (MiTE) for funding this research through the AdP "Piano Operativo di Ricerca (POR) sull'idrogeno verde Figure 1
La1.5Sr1.5Mn1.5Ni0.5O7±δ Vs La1.5Sr1.5Co1.5Ni0.5O7±δ:作为直接沼气燃料SOFC阳极层的外溶材料
目前,直接以碳氢化合物(如沼气)为燃料的商用SOFC系统的主要问题之一是,在将燃料转化为电能的过程中,由于碳的形成/沉积,极有可能阻塞阳极侧的活性相(如Ni-YSZ)。这个问题会降低电池的整体性能和耐用性。因此,为了克服这种失活机制,成功地证明了在商用SOFC中使用基于外溶钙钛矿的材料的额外阳极活性层可能是一种有趣且可行的替代方案。这一结论是基于这样一个事实,即使用这种材料可以得到具有高稳定性和电催化活性的嵌入纳米颗粒的非均相表面体系,这些纳米颗粒在碳氢燃料气氛中均匀分布在表面上,并且具有高的碳焦化耐受性。本研究旨在评价和比较两种新型催化材料与Ni溶出液对直接干燥沼气燃料SOFC的电催化性能。起始材料为ruddlesden - popper型镍锰矿(La 1.5 Sr 1.5 Mn 1.5 Ni 0.5 O 7±δ或LSMN)和钴酸镍(La 1.5 Sr 1.5 Co 1.5 Ni 0.5 O 7±δ或LSCN)。这两种材料都是用化学计量量的前体作为硝酸盐通过Pechini方法合成的。一旦凝胶形成,它们将在空气中以两种停留温度(300°C 2小时和500°C 3小时)进行处理,以确保有机化合物的完全消除。最后,将得到的粉末在1300℃的空气中处理12h,然后进行物理化学表征。为了进行电化学表征,将处理后的粉末分别与Gd 0.1 Ce 0.9 o2 (CGO)以70:30的质量比混合,球磨6h。最后,为了得到用于涂层的浆料,每种混合物(LSMN+CGO和LSCN+CGO)在8wt %的三乙醇胺、2wt %的聚乙烯醇丁醛树脂(BUTVAR B-98)和2-丙醇的存在下再研磨2h。由InDEC®(阳极支撑电池Ni-YSZ/YSZ/LSM)制成的商用纽扣式SOFC电池被涂在阳极一侧,得到2平方厘米的有效面积。实验在800°C下进行,用稀释的h2预处理,然后用模拟的干燥沼气。采用生物工具作为电化学测量装置。本次交流的目的是展示两个纽扣电池的实验结果,这些纽扣电池来自于相同的大面积商业电池(阳极支撑电池),并涂有本工作中开发的两种电催化剂。200多小时的电化学测试表明,在选定的恒流条件下(500 mA cm−2),阳极侧的外部功能层有助于在整个工作时间内获得稳定的电位。通过比较这两种测试的结果,发现外溶的LSCN层表现出更好的性能,这是因为b位掺杂了Co而不是Mn,从而增强了晶体结构内的o2 -输运。最后,反应后表征显示,在两种情况下,碳物质都是最小的/零的,这表明,在商业SOFC中直接使用碳氢燃料造成的传统风险可以通过这种方法得到抑制,这将导致我们考虑在下一个层次或进一步的电化学应用中使用这种类型的材料。作者承认该项目名为“固体氧化物燃料电池中生物燃料的直接利用,用于可持续和分散的电力生产和供热(DIRECTBIOPOWER)”。资助协议编号:2017FCFYHK。作者感谢意大利生态转型部(MiTE)通过AdP“Piano Operativo di Ricerca (POR) sull'idrogeno verde图1”资助本研究
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