Experimental and modeling of the electrodialytic and dialytic treatment of a fly ash containing Cd,Cu and Pb |
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Authors: | A T Lima A B Ribeiro J M Rodríguez-Maroto E P Mateus A M Castro L M Ottosen |
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Affiliation: | 1.CENSE – Center for Environmental and Sustainability Research, Departamento de Ciências e Engenharia do Ambiente, Faculdade de Ciências e Tecnologia,Universidade Nova de Lisboa,Caparica,Portugal;2.Department of Chemical Engineering,University of Málaga,Málaga,Spain;3.INRB,Oeiras,Portugal;4.Department of Civil Engineering,Technical University of Denmark,Lyngby,Denmark |
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Abstract: | A one-dimensional model is developed for simulating the electrodialytic and dialytic treatment of a fly ash containing cadmium,
copper and lead. Two experimental systems have been used, a column of ash and a stirred ash suspension. The movement of Cd,
Cu and Pb has been modeled taking into account the diffusion transport resulting from the concentration gradients of their
compounds through the membranes and boundary layers and the electromigration of their ionic, simple and complex species during
the operation. The model also includes the electromigration of the non-contaminant most important principal ionic species
in the system, H+ and OH−, proceeding of the electrolysis at the electrodes, Ca2+, CO3
=, SO4
=, etc. proceeding from the ash and Na+ and NO3
−, or citrate and ammonium ions incorporated as electrolyte solutions and/or as agent solution during the ash treatment. The
simulation also takes into account that OH− generated on the cathode, during the electrodialytic remediation, is periodically neutralized by the addition of nitric acid
in the cathode compartment. The anion and cation-exchange membranes are simply represented as ionic filters that preclude
the transport of the cations and anions, respectively, with the exception of H+ which is retarded but pass through the anion-exchange membrane. |
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Keywords: | |
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