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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-II-14where TOC 0 is <strong>the</strong> initial TOC (mgC·L –1 ), t is time (min) and k is <strong>the</strong> first order kineticconstant (min –1 ). Results <strong>of</strong> <strong>the</strong> experimental fitting with PolyMath ® v5.0 for k lead to acorrelation coefficient r 2 >0.985 in all individual runs as it is shown in table 1.From table 1, overlapping <strong>of</strong> experimental results is observed in <strong>the</strong> experimental runswhere only sulphate concentration was modified. These experimental results can be describedas it is shown in table 1 (k I ) and one value <strong>of</strong> <strong>the</strong> kinetic parameter independent <strong>of</strong> <strong>the</strong>electrolyte concentration has been obtained. Kinetic parameters for high current density(60 mA·cm –2 ) were later lumped toge<strong>the</strong>r, as summarized in table 1 (k II ) showing <strong>the</strong>negligible influence <strong>of</strong> <strong>the</strong> initial lignosulphonate concentration at high current densities.ConclusionsKinetic results summarized in table 1 show that <strong>the</strong> concentration <strong>of</strong> sodium sulphatesupporting electrolyte between 2.5 and 5 g·L –1 at each level <strong>of</strong> initial TOC and applied currentdensity does not show any influence on <strong>the</strong> kinetic parameter and <strong>the</strong>refore this influence canbe neglected in <strong>the</strong> studied range <strong>of</strong> variables. At high current density (60 mA·cm –2 ) <strong>the</strong>re isnot an influence <strong>of</strong> <strong>the</strong> initial TOC in <strong>the</strong> kinetic parameter (k·10 3 = 4.42±0.12 min –1 ); at lowcurrent density (30 mA·cm –2 ) kinetics is faster at low initial TOC (at 150 mgC·L –1 , k·10 3 =3.78±0.17 min –1 ) when compared to high initial TOC (at 450 mgC·L –1 , k·10 3 = 2.98±0.13min –1 ). Previous studies with phenol oxidation in sulphate media gave higher values <strong>of</strong> <strong>the</strong>first order kinetic constant (k·10 3 = 11.94±0.62 min –1 ) operating at low current density (2).AcknowledgmentsThis research is financially supported by <strong>the</strong> Spanish Ministry <strong>of</strong> Science and Technology(Project CONSOLIDER CTM2006-00317).References1. Rodrigo, M.A.; Michaud, P.A.; Duo, I.; Panizza, M.; Cerisola, G.; Comninellis, C. Oxidation <strong>of</strong>4-Chlorophenol at Boron-Doped Diamond Electrode for Wastewater Treatment. Journal <strong>of</strong> <strong>the</strong>Electrochemical Society 2001, 148 (5), D60-64.2. Sierra, L.; Rodríguez, N.; Urtiaga, A.M.; Ortiz, I. Electrochemical degradation <strong>of</strong> industrial wastewaters byanodic oxidation using a boron-doped diamond electrode. Viability study, 10 th Mediterranean Congress,Barcelona, SPAIN, 2005.298

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