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

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LIGNOSULPHONATE TOTAL ORGANIC CARBONTREATMENT USING ELECTROCHEMICAL OXIDATIONA. Dominguez-Ramos, A. Fuente-Martin, R. Aldaco and A. Irabien *PP-II-14Departmento de Ingeniería Química y Química Inorgánica, Universidad de Cantabria, ETSIIT, Avda. de los Castros s/n, 39005, Santander, SPAIN: (+34)-942201591 : e-mail * : irabienj@unican.esIntroductionLignin derivatives account for a significant fraction <strong>of</strong> <strong>the</strong> biorefractory content in <strong>the</strong>wastewaters coming from <strong>the</strong> pulp and paper industry. Biological activated sludge processesdo not allow <strong>the</strong> treatment <strong>of</strong> biorefreactory organic carbon. Advanced oxidation processes(AOP) such as electrochemical oxidation have been described as an efficient alternative dueto <strong>the</strong> removal <strong>of</strong> dissolved organic matter by electro-generated oxidations (1).Lignosulphonate was selected as specific compound to describe <strong>the</strong> biorefractory fraction <strong>of</strong><strong>the</strong> wastewaters. Total Organic Carbon (TOC) will be studied in <strong>the</strong> effluent.Experimental results and discussionThe Lab-scale electrochemical treatment plant is based on a conventional two-parallelboron-doped diamond (BDD) electrodes flow cell DiaCell 106.101 ® (Adamant Technologies)operated in a batch mode under iso<strong>the</strong>rmal conditions and constant flowrate. TOC removalwas studied until 90% reduction was obtained.In order to study <strong>the</strong> effect <strong>of</strong> selected variables (initial TOC ([TOC] 0 ), current density (j)and supporting electrolyte concentration ([Na 2 SO 4 ])) in <strong>the</strong> electrochemical oxidation <strong>of</strong>lignosulphonate, <strong>the</strong> experimental design and kinetic modelling shown in table 1 wasperformed. According to experimental TOC time pr<strong>of</strong>iles, a first order kinetics was used todescribe experimental results in <strong>the</strong> form <strong>of</strong> dimensionless TOC:Table 1. Experimental design and kinetic constants[TOC]Exp. run0 j [Na 2 SO 4 ] k·10 3(mgC·L –1 ) (mA·cm –2 ) (g·L –1 ) (min –1 ) * r 2 k I·10 3(min –1 ) * 2 kr II·10 3I(min -1 ) * 2r II1 150 30 5 3.92±0.29 0.9883.78±0.17 0.989 3.78±0.17 0.9892 150 30 2.5 3.64±0.20 0.9935 450 30 5 2.93±0.15 0.9932.98±0.13 0.988 2.98±0.13 0.9886 450 30 2.5 3.03±0.26 0.9853 150 60 5 4.39±0.22 0.9944.52±0.16 0.9934 150 60 2.5 4.65±0.25 0.9944.42±0.12 0.9917 450 60 5 4.07±0.25 0.9928 450 60 2.5 4.59±0.24 0.994 4.32±0.20 0.989− 10( )TOC· TOC = exp −k·t ∀t≥ 0,*Confidence range=95%297

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