Oxidation of organics in water by active chlorine performed in microfluidic electrochemical reactors: a new way to improve the performances of the process

Wastewater polluted by organics can be treated by using electro-generated active chlorine, even if this promising route presents some important drawbacks such as the production of chlorinated by-products. Here, for the first time, this process was studied in a microfluidic electrochemical reactor wi...

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Bibliographic Details
Published inChemosphere (Oxford) Vol. 355; p. 141855
Main Authors Randazzo, Serena, Geagea, Ange, Proietto, Federica, Galia, Alessandro, Scialdone, Onofrio
Format Journal Article
LanguageEnglish
Published England Elsevier Ltd 01.05.2024
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Summary:Wastewater polluted by organics can be treated by using electro-generated active chlorine, even if this promising route presents some important drawbacks such as the production of chlorinated by-products. Here, for the first time, this process was studied in a microfluidic electrochemical reactor with a very small inter-electrode distance (145 μm) using a water solution of NaCl and phenol and a BDD anode. The potential production of chloroacetic acids, chlorophenols, carboxylic acids, chlorate and perchlorate was carefully evaluated. It was shown, for the first time, up to our knowledge, that the use of the microfluidic device allows to perform the treatment under a continuous mode and to achieve higher current efficiencies and a lower generation of some important by-products such as chlorate and perchlorate. As an example, the use of the microfluidic apparatus equipped with an Ag cathode allowed to achieve a high removal of total organic carbon (about 76%) coupled with a current efficiency of 17% and the production of a small amount of chlorate (about 30 ppm) and no perchlorate. The effect of many parameters (namely, flow rate, current density and nature of cathode) was also investigated. [Display omitted] •Electrochemical wastewater treatment by active chlorine was done in microfluidic cells.•Higher current efficiencies and lower generation of ClO3− and ClO4− were achieved.•The performance of the process improved using an Ag cathode.
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ISSN:0045-6535
1879-1298
DOI:10.1016/j.chemosphere.2024.141855