Abstract:Surface exchange coefficient (k) of porous mixed ionic-electronic conductors (MIECs) determine the device-level electrochemical performance of solid oxide cells. However, great difference is reported for k values, which are measured...
“…It is difficult to explain these discrepancies, although it is known that the sample morphology (powder, dense sample, porous electrodes (where the gas diffusion can affect the mass transport) as well as the employed method (Electrical conductivity relaxation (ECR), oxygen isotopic exchange (OIE), electrochemical impedance spectroscopy (EIS)) can give quite different results [31] …”
Section: Resultsmentioning
confidence: 99%
“…[22b] It is difficult to explain these discrepancies, although it is known that the sample morphology (powder, dense sample, porous electrodes (where the gas diffusion can affect the mass transport) as well as the employed method (Electrical conductivity relaxation (ECR), oxygen isotopic exchange (OIE), electrochemical impedance spectroscopy (EIS)) can give quite different results. [31] Electrochemical Characterizations of Symmetrical Cells Symmetrical cells were prepared by screen printing inks of LSM, LSCF and LNO on dense 8-YSZ substrates 248 μm thick (see experimental section). Interfacial layers of ceria doped gadolinium oxide (CGO) were employed for the LSM and LSCF cells to inhibit the reactivity between the catalysts and YSZ electrolyte.…”
Oxygen mobility was studied by oxygen isotopic exchange on three electrodes used in Solid Oxide Electrolyser Cells under polarization (La0.8Sr0.2MnO3 (LSM), La0.6Sr0.4Co0.2Fe0.8O3‐d (LSCF) and La2NiO4+d (LNO)). The rate of the surface and the bulk mechanisms for oxygen mobility is depending on the type of conductivity (electronic conduction or mixed ionic and electronic conductivity). It is shown that a one oxygen atom exchange is dominant for the surface path whereas a two oxygen atoms mechanism dominates for the bulk path. The rate constant for the bulk path is much higher than the one for the surface path by two orders of magnitude. Additionally, polarized oxygen isotopic exchange revealed that electrode overvoltage increases significantly the rate constant for the surface path, whereas its impact on the bulk path is negligible.
“…It is difficult to explain these discrepancies, although it is known that the sample morphology (powder, dense sample, porous electrodes (where the gas diffusion can affect the mass transport) as well as the employed method (Electrical conductivity relaxation (ECR), oxygen isotopic exchange (OIE), electrochemical impedance spectroscopy (EIS)) can give quite different results [31] …”
Section: Resultsmentioning
confidence: 99%
“…[22b] It is difficult to explain these discrepancies, although it is known that the sample morphology (powder, dense sample, porous electrodes (where the gas diffusion can affect the mass transport) as well as the employed method (Electrical conductivity relaxation (ECR), oxygen isotopic exchange (OIE), electrochemical impedance spectroscopy (EIS)) can give quite different results. [31] Electrochemical Characterizations of Symmetrical Cells Symmetrical cells were prepared by screen printing inks of LSM, LSCF and LNO on dense 8-YSZ substrates 248 μm thick (see experimental section). Interfacial layers of ceria doped gadolinium oxide (CGO) were employed for the LSM and LSCF cells to inhibit the reactivity between the catalysts and YSZ electrolyte.…”
Oxygen mobility was studied by oxygen isotopic exchange on three electrodes used in Solid Oxide Electrolyser Cells under polarization (La0.8Sr0.2MnO3 (LSM), La0.6Sr0.4Co0.2Fe0.8O3‐d (LSCF) and La2NiO4+d (LNO)). The rate of the surface and the bulk mechanisms for oxygen mobility is depending on the type of conductivity (electronic conduction or mixed ionic and electronic conductivity). It is shown that a one oxygen atom exchange is dominant for the surface path whereas a two oxygen atoms mechanism dominates for the bulk path. The rate constant for the bulk path is much higher than the one for the surface path by two orders of magnitude. Additionally, polarized oxygen isotopic exchange revealed that electrode overvoltage increases significantly the rate constant for the surface path, whereas its impact on the bulk path is negligible.
Oxygen exchange reaction on mixed conducting oxide is a critical reaction for many applications, yet measuring its rate constant remains poorly reliable by standard techniques. Here, a new technique that adapts the conductivity relaxation measurements on porous ceramics is proposed. Using a simple image analysis tool, it is possible to accurately determine the grain size distribution of the porous oxide, which is used in a new relaxation model that integrates relaxation times over that distribution. With such a model, it is possible to fit relaxation transients with the oxygen exchange reaction rate constant kchem as the only fitting parameter. With such rigidity, the output values of kchem are not sensitive to the fitting procedure, which does not require optimization. The model is proven to be applicable to various mixed conducting oxides and to a wide range of microstructures, yielding a remarkably low residual for all the porous ceramics considered. The procedure uses porous ceramics, therefore the derived kinetics are representative of ceramics used in real applications such as fuel cells, sensors, or catalysis.
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