Electrochemical study of a hydrogen diffusion anode-membrane assembly for membrane electrolysis

The membrane electrode assembly (MEA) studied was constituted with a gas diffusion electrode (E-TEK) impregnated with Nafion® solution which was assembled with a Nafion® 117 cation exchange membrane under heat and pressure. The MEA was used as anode in a membrane electrolysis (ME) cell with the objective to regenerate HCl and NaOH from NaCl. Current efficiency for hydrogen oxidation was determined and its value is 100%, which indicates that the only reaction occurring at the anode is the oxidation of hydrogen. Current-potential curves, recorded in different conditions, showed a linear variation in the range 0-3000 A m−2 when hydrochloric acid concentration is below 2 mol dm−3. In this case, the overvoltage was shown to be mainly due to the ohmic drop in the membrane and in the layer where Nafion® impregnation was performed. MEA overvoltage necessary to reach 3000 A m−2 current density was about 0.12 V. For high HCl concentration (6-8 mol dm−3), the MEA overvoltage increased sharply with current density due to the adsorption of chloride anions on platinum catalyst.