Electrochemical treatment of water containing Microcystis aeruginosa in a fixed bed reactor with three-dimensional conductive diamond anodes

被引:28
作者
Mascia, Michele [1 ]
Monasterio, Sara [1 ]
Vacca, Annalisa [1 ]
Palmas, Simonetta [1 ]
机构
[1] Univ Cagliari, Dipartimento Ingn Meccan Chim & Mat, Via Marengo 3, I-09123 Cagliari, Italy
关键词
M; aeruginosa; Electrochemical treatment; Conductive diamond; Three-dimensional electrodes; Mathematical model; BY-PRODUCT FORMATION; ALGAE REMOVAL; BDD ANODES; ESCHERICHIA-COLI; DISINFECTION; ELECTRODES; ELECTROLYSIS; INACTIVATION; COAGULATION; CONTAMINANTS;
D O I
10.1016/j.jhazmat.2016.03.004
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
An electrochemical treatment was investigated to remove Microcystis aeruginosa from water. A fixed bed reactor in flow was tested, which was equipped with electrodes constituted by stacks of grids electrically connected in parallel, with the electric field parallel to the fluid flow. Conductive diamond were used as anodes, platinised Ti as cathode. Electrolyses were performed in continuous and in batch recirculated mode with flow rates corresponding to Re from 10 to 160, current densities in the range 10-60 A m(-2) and Cl- concentrations up to 600 gm(-3). The absorbance of chlorophyll-a pigment and the concentration of products and by-products of electrolysis were measured. In continuous experiments without algae in the inlet stream, total oxidants concentrations as equivalent Cl-2, of about 0.7 g Cl-2 m(-3) were measured; the maximum values were obtained at Re = 10 and i = 25 A m(-2), with values strongly dependent on the concentration of Cl-. The highest algae inactivation was obtained under the operative conditions of maximum generation of oxidants; in the presence of microalgae the oxidants concentrations were generally below the detection limit. Results indicated that most of the bulk oxidants electrogenerated is constituted by active chlorine. The prevailing mechanism of M. aeruginosa inactivation is the disinfection by bulk oxidants. The experimental data were quantitatively interpreted through a simple plug flow model, in which the axial dispersion accounts for the non-ideal flow behaviour of the system; the model was successfully used to simulate the performances of the reactor in the single-stack configuration used for the experiments and in multi-stack configurations. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:111 / 120
页数:10
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