2021
DOI: 10.1016/j.jpowsour.2021.229521
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Development of mathematical transfer functions correlating Solid Oxide Fuel Cell degradation to operating conditions for Accelerated Stress Test protocols design

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Cited by 11 publications
(4 citation statements)
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“…Knowing Ni radius time evolution, the consequences on cell behaviour can be evaluated by applying the microscale kinetics formulation presented in Table 1, which expresses the exchange current density J 0 , the material conductivity s and gas diffusion coefficients D eff as functions of the particle size. As observed in reference studies, 23,35,40,56,57 the radius increase causes the reduction of the particle surface area, which means a lower contact section between both metal-ceramic particles (i.e., lower catalytic activity and TPB density) and metal-metal, ceramic-ceramic particles (i.e., lower electron and ion conductivity, respectively). Moreover, larger particles inuence material porosity also by increasing the pore dimension.…”
Section: Methodsmentioning
confidence: 58%
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“…Knowing Ni radius time evolution, the consequences on cell behaviour can be evaluated by applying the microscale kinetics formulation presented in Table 1, which expresses the exchange current density J 0 , the material conductivity s and gas diffusion coefficients D eff as functions of the particle size. As observed in reference studies, 23,35,40,56,57 the radius increase causes the reduction of the particle surface area, which means a lower contact section between both metal-ceramic particles (i.e., lower catalytic activity and TPB density) and metal-metal, ceramic-ceramic particles (i.e., lower electron and ion conductivity, respectively). Moreover, larger particles inuence material porosity also by increasing the pore dimension.…”
Section: Methodsmentioning
confidence: 58%
“…38 However, multiscale simulation codes that are able to merge all aspects, from the single mechanisms to global cell degradation, and involving simultaneously empirical correlations as well as microstructure-dependent kinetic formulations to be applied depending on the available experimental observations, are still rare in the literature. 39–41…”
Section: Introductionmentioning
confidence: 99%
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“…In addition, the validation of stack components over several years before their integration in a real system is not compatible with the times requested by fuel cell manufacturers for the market deployment of their product. There are only few experiments exceeding 40,000 h [34], with the longest one reaching 100,000 h, i.e., more than 10 years [35]. However, at the end of testing, the stack no longer corresponded to the SoA technology and the conclusions, although correct, could not answer the present day technological challenges.…”
Section: Introductionmentioning
confidence: 97%