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Depth profiling with Auger electron spectroscopy (AES) was used to investigate Cl diffusion and oxide formation during the first stage of oxidation.
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Since the concentration of oxygen decreases in a CL from the diffusion medium-CL interface towards the polymer membrane, the CL adjacent to the diffusion medium should be of higher porosity than the other CLs.
In addition, geometrical factors such as the catalyst layer (CL) and gas diffusion layer (GDL) porosity are also varied as well.
The published PBPK model structure for organic anion transporting polypeptides (OATP) substrates incorporating hepatic uptake clearance (CL act), passive diffusion (CL pass), metabolic (CL met), and biliary (CL bile) clearances 19 is applied for bosentan, olmesartan, repaglinide, and valsartan.
In the 8 atom % Cl–, the CdSe diffusion is rapid and the grains grow more easily, while in films with 3 atom % Cl–, the CdSe diffusion is relatively slow and <5 nm grains are maintained at 250 °C and below.
The monotonic profile of Cl reveals an upward diffusion.
The porous outer layer can permit the penetration of water and the diffusion of Cl.
The CO2 bubble emergence processes from the catalyst layer (CL) to the gas diffusion layer (GDL) and then to the flow channels are studied with two different strategies.
In this paper a numerical analysis was applied to evaluate performance of square tubular Proton Exchange Membrane (PEM) with three different architectures of catalyst (CL), membrane and gas diffusion layer (GDL).
Alternatively, local diffusion of Cl out of the object may occur in these areas or other explanations may be possible.
It was also clarified that the SiO2 addition in the CL promoted the back-diffusion of water generated at the cathode to the anode, resulting in an increased O2 gas diffusion rate to the cathode-CL/PEM interface, accompanied by an increased water content in the membrane.
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