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                <forename type="first">Sié Alain</forename>
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            <idno type="halRefHtml">&lt;i&gt;Journal of Hazardous Materials&lt;/i&gt;, 2022, 437, pp.129326. &lt;a target="_blank" href="https://dx.doi.org/10.1016/j.jhazmat.2022.129326"&gt;&amp;#x27E8;10.1016/j.jhazmat.2022.129326&amp;#x27E9;&lt;/a&gt;</idno>
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                <title xml:lang="en">Comparison of homogeneous and heterogeneous electrochemical advanced oxidation processes for treatment of textile industry wastewater</title>
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                    <forename type="first">Bi Gouessé Henri</forename>
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                <title level="j">Journal of Hazardous Materials</title>
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                <term xml:lang="en">Perchlorate</term>
                <term xml:lang="en">Dye</term>
                <term xml:lang="en">Mineralization</term>
                <term xml:lang="en">Electro-Fenton</term>
                <term xml:lang="en">Anodic Oxidation</term>
                <term xml:lang="en">Anodic Oxidation Electro-Fenton Mineralization Dye Perchlorate</term>
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              <p>This study aimed at understanding the influence of the generation of oxidants in a heterogeneous way at boron-doped diamond (BDD) anode (anodic oxidation (AO)) or homogeneously in the bulk (electro-Fenton (EF)) during treatment of a textile industry wastewater. Both processes achieved high TOC removal. A yield of 95% was obtained by combining EF with BDD anode during 6 h of treatment. The EF process was found to be faster and more efficient for discoloration of the effluent, whereas AO was more effective to limit the formation of degradation by-products in the bulk. An advantage of AO was to treat this alkaline effluent without any pH adjustment. Operating these processes under current limitation allowed optimizing energy consumption in both cases. However, using BDD anode led to the formation of very high concentration of ClO3-/ClO4-from Cl-oxidation (even at low current density), which appears as a key challenge for treatment of such effluent by AO. By comparison, EF with Pt anode strongly reduced the formation of ClO3-/ClO4-. Operating EF at low current density even maintained these concentrations below 0.5% of the initial Cl-concentration. A trade-off should be considered between TOC removal and formation of toxic chlorinated by-products.</p>
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