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19 results on '"Mercier G"'

4. Operational definition of Active and Healthy Ageing (AHA): A conceptual framework

Author

Bousquet, Jean, primary, Kuh, D., additional, Bewick, M., additional, Standberg, T., additional, Farrell, J., additional, Pengelly, R., additional, Joel, M. E., additional, Rodriguez Mañas, L., additional, Mercier, J., additional, Bringer, J., additional, Camuzat, T., additional, Bourret, R., additional, Bedbrook, A., additional, Kowalski, M. L., additional, Samolinski, B., additional, Bonini, S., additional, Brayne, C., additional, Michel, J. P., additional, Venne, J., additional, Viriot-Durandal, P., additional, Alonso, J., additional, Avignon, A., additional, Ben-Shlomo, Y., additional, Bousquet, P. J., additional, Combe, B., additional, Cooper, R., additional, Hardy, R., additional, Iaccarino, G., additional, Keil, T., additional, Kesse-Guyot, E., additional, Momas, I., additional, Ritchie, K., additional, Robine, J. M., additional, Thijs, C., additional, Tischer, C., additional, Vellas, B., additional, Zaidi, A., additional, Alonso, F., additional, Andersen Ranberg, K., additional, Andreeva, V., additional, Ankri, J., additional, Arnavielhe, S., additional, Arshad, H., additional, Augé, P., additional, Berr, C., additional, Bertone, P., additional, Blain, H., additional, Blasimme, A., additional, Buijs, G. J., additional, Caimmi, D., additional, Carriazo, A., additional, Cesario, A., additional, Coletta, J., additional, Cosco, T., additional, Criton, M., additional, Cuisinier, F., additional, Demoly, P., additional, Fernandez-Nocelo, S., additional, Fougère, B., additional, Garcia-Aymerich, J., additional, Goldberg, M., additional, Guldemond, N., additional, Gutter, Z., additional, Harman, D., additional, Hendry, A., additional, Heve, D., additional, Illario, M., additional, Jeande, C., additional, Krauss-Etschmann, S., additional, Krys, O., additional, Kula, D., additional, Laune, D., additional, Lehmann, S., additional, Maier, D., additional, Malva, J., additional, Matignon, P., additional, Melen, E., additional, Mercier, G., additional, Moda, G., additional, Nizinkska, A., additional, Nogues, M., additional, O’Neill, M., additional, Pelissier, J. Y., additional, Poethig, D., additional, Porta, D., additional, Postma, D., additional, Puisieux, F., additional, Richards, M., additional, Robalo-Cordeiro, C., additional, Romano, V., additional, Roubille, F., additional, Schulz, H., additional, Scott, A., additional, Senesse, P., additional, Slagter, S., additional, Smit, H. A., additional, Somekh, D., additional, Stafford, M., additional, Suanzes, J., additional, Todo-Bom, A., additional, Touchon, J., additional, Traver-Salcedo, V., additional, Van Beurden, M., additional, Varraso, R., additional, Vergara, I., additional, Villalba-Mora, E., additional, Wilson, N., additional, Wouters, E., additional, and Zins, M., additional

Published
2015
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19. In situ active chlorine generation for the treatment of dye-containing effluents

Author

Jean-François Blais, Patrick Drogui, François Zaviska, Guy Mercier, Zaviska, Francois Alan, Drogui, P, Blais, K, and Mercier, G

Subjects
Eosin, indirect electrochemical oxidation, Electrolytic cell, General Chemical Engineering, Acridine orange, Inorganic chemistry, chemistry.chemical_element, dye, colour removal, Electrochemistry, Chloride, Reaction rate, chemistry.chemical_compound, Reaction rate constant, chemistry, Materials Chemistry, Chlorine, medicine, active chlorine, Ti/IrO2 anode, medicine.drug
Abstract

This study examined the possibility to remove colour causing-compounds from synthetic effluent by indirect electrochemical oxidation using iridium oxide anode electrodes. Using a high concentration of chloride ions (17.1 mM) and various current densities, it was possible to produce high concentration of active chlorine with a specific production rate of 2.8 mg min−1 A−1. The best performance for acid methyl violet 2B dye (MV2B) decomposition was obtained using Ti/IrO2 anodes operated at a current density of 15 mA cm−2 during 40 min of treatment in the presence of 3.42 mM of chloride ions. Under these conditions, more than 99% of MV2B was removed (with a reaction rate apparent constant of 0.20 min−1), whereas COD and TOC removal were 51% and 75%, respectively. The electrolytic cell was then used for the degradation of three other synthetic dye solutions: Eosin yellowish (EOY), Trypan Blue (TRB), Acridine Orange (ACO). TRB was the most difficult dye to remove from solution with a value reaction rate constant of 0.12 min−1, compared to 0.19 min−1 and 0.24 min−1 recorded for ACO and EOY dyes, respectively. More than 99% of these dyes were removed by electrochemical oxidation.

Published
2009

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