کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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190115 | 459692 | 2011 | 7 صفحه PDF | دانلود رایگان |
The oxygen-depolarized cathode has become attractive by reducing energy consumption and also CO2 emissions. The initial gas-diffusion electrode was for a three-compartment cell in which the alkaline electrolyte was separated from the oxygen feeder. During the electrolysis, the electrolyte penetrated into the hydrophobic gas-diffusion layer. Thus the pores in the diffusion layer were flooded with the electrolyte and the performance decreased.We proposed a new gas-diffusion electrode (GDE) having a large pore radius for a two-compartment cell in which the GDE was pressed on the membrane, and the electrolyte was transported through the GDE. The previous electrode was used for a three-compartment cell, which contained the anolyte, catholyte and oxygen-feeder compartments. First, a model analysis was made to simulate the cathodic overpotential curves of the GDE's for the two-compartment and three-compartment cells. Experiments were made using a half cell for the cathodic polarization curve and a zero-gap cell for testing the increased durability. The two-compartment cell with Ag–CC (carbon cloth) had the highest performance among the GDE's. However, the decrease in performance during a longer period, such as 600 days, was considered to be due to catalyst aggregation and not flooding the pores based on the cathodic potential curve and the SEM images.
Journal: Electrochimica Acta - Volume 56, Issue 28, 1 December 2011, Pages 10575–10581