2005
DOI: 10.1149/200507.1636pv
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The Oxygen Reduction Kinetics of Mixed Conducting Electrodes: Model Considerations and Experiments on La0.6Sr0.4Co0.8Fe0.2O3 Microelectrodes

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Cited by 3 publications
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“…Here, j ano,TPB 0 (A m −1 ) is the exchange current density per unit length of the TPB and j cath,DPB 0 (A m −2 ) is the exchange current density per unit area of the DPB; ρ L TPB (m 3 m −1 ) is the TPB length density and ρ L DPB (m 3 m −2 ) is the DPB area density. The anodic and cathodic charge-transfer coefficients are taken from the porous Ni/YSZ anode measurements of de Boer [51] and from the LSCF cathode investigation of Fleig et al [52]. The activation overpotentials η act (V) are calculated as follows:…”
Section: Thermo-electric Modelmentioning
confidence: 99%
“…Here, j ano,TPB 0 (A m −1 ) is the exchange current density per unit length of the TPB and j cath,DPB 0 (A m −2 ) is the exchange current density per unit area of the DPB; ρ L TPB (m 3 m −1 ) is the TPB length density and ρ L DPB (m 3 m −2 ) is the DPB area density. The anodic and cathodic charge-transfer coefficients are taken from the porous Ni/YSZ anode measurements of de Boer [51] and from the LSCF cathode investigation of Fleig et al [52]. The activation overpotentials η act (V) are calculated as follows:…”
Section: Thermo-electric Modelmentioning
confidence: 99%
“…In the case of a tubular geometry, a large number of mesh elements are generally necessary because of the large ratio between the length and thickness of the layers, which is of the order of 500‐1,000 (Hwang et al , 2005; Fleig et al , 2005). A second particular feature of such a geometrical configuration concerns the non negligible effects of radiation heat transfer in both the single cells (Haynes and Wepfer, 2001) and in the stacks (Verda and Borchiellini, 2007).…”
Section: Introductionmentioning
confidence: 99%