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Electrochemical Degradation of Reactive Black 5 Using Three-Dimensional Electrochemical System Based on Multiwalled Carbon Nanotubes Publisher



Mengelizadeh N1 ; Pourzamani H2, 3 ; Saloot MK4, 5 ; Hajizadeh Y1 ; Parseh I1 ; Parastar S6 ; Niknam N7
Authors
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Authors Affiliations
  1. 1. Research Center of Health, Safety and Environment, Dept. of Environmental Health Engineering, Evaz School of Health, Larestan Univ. of Medical Sciences, P.O. Box 74318-95659, Larestan, Iran
  2. 2. Environment Research Center, Research Institute for Primordial Prevention of Noncommunicable Disease, Isfahan Univ. of Medical Sciences, Isfahan, 81746-73461, Iran
  3. 3. Dept. of Environmental Health Engineering, Student Research Committee, School of Health, Isfahan Univ. of Medical Sciences, Isfahan, Iran
  4. 4. Dept. of Environmental Engineering, Faculty of Natural Resources and Environment, Science and Research Branch, Islamic Azad Univ., Tehran, 14778-93885, Iran
  5. 5. Dept. of Environmental Health Engineering, Behbahan Faculty of Medical Science, Behbahan, 63617-96819, Iran
  6. 6. Dept. of Environmental Health Engineering, School of Health, Ardabil Univ. of Medical Sciences, Ardabil, 56189-53141, Iran
  7. 7. Health Care Management, School of Health Management and Medical Informatics, Iran Univ. of Medical Sciences, Tehran, 19967-13883, Iran

Source: Journal of Environmental Engineering (United States) Published:2019


Abstract

The removal of Reactive Black 5 (RB5) dye and chemical oxygen demand (COD) was investigated using a three-dimensional (3D) electrochemical (3DE) reactor with multiwalled carbon nanotubes (MWCNTs). The experiments were performed according to a Taguchi design model, with the variables being the solution pH (2-9), current density (10-25 mA/cm2), reaction time (15-60 min), MWCNT concentration (25-200 mg/L), and RB5 concentration (25-100 mg/L). The best conditions for optimum removal of RB5 and COD were pH 3, MWCNT concentration 200 mg/L, current density 15 mA/cm2, RB5 concentration 100 mg/L, and reaction time 60 min. Among the main factors, the solution pH for removal of COD and RB5 and the current density for energy consumption had the highest impact. The 3D system generated more H2O2 and OH radicals compared with a two-dimensional (2D) system because the MWCNTs act as microelectrodes in the optimal conditions. In the 3D process, the production of high levels of reactive species led to an increase in the degradation of RB5 into aromatic compounds and various acids. © 2019 American Society of Civil Engineers.
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