2022
DOI: 10.1016/j.jhazmat.2022.129326
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Comparison of homogeneous and heterogeneous electrochemical advanced oxidation processes for treatment of textile industry wastewater

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Cited by 29 publications
(5 citation statements)
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“…The formation of ClO 4 – during the electrochemical oxidation of chlorinated wastewater is a long-standing problem. , However, previous studies implied that the Pt electrode used in this study may have certain advantages in treating wastewater containing chlorine compared to the widely acclaimed BDD electrode in the degradation of PFOA, as Pt forms lower concentrations of ClO 4 – byproducts compared to BDD. However, if the removal efficiency of PFOA is emphasized, BDD electrode is undoubtedly a better choice than Pt electrode, because BDD electrode has better removal efficiency of PFOA than Pt, even that the presence of Cl – can inhibit the degradation of PFOA by BDD electrode. In summary, further evaluation is needed on the economic and environmental benefits of PFOA degradation systems involving active chlorine.…”
Section: Resultsmentioning
confidence: 92%
“…The formation of ClO 4 – during the electrochemical oxidation of chlorinated wastewater is a long-standing problem. , However, previous studies implied that the Pt electrode used in this study may have certain advantages in treating wastewater containing chlorine compared to the widely acclaimed BDD electrode in the degradation of PFOA, as Pt forms lower concentrations of ClO 4 – byproducts compared to BDD. However, if the removal efficiency of PFOA is emphasized, BDD electrode is undoubtedly a better choice than Pt electrode, because BDD electrode has better removal efficiency of PFOA than Pt, even that the presence of Cl – can inhibit the degradation of PFOA by BDD electrode. In summary, further evaluation is needed on the economic and environmental benefits of PFOA degradation systems involving active chlorine.…”
Section: Resultsmentioning
confidence: 92%
“…7c), TOC removal efficiency was diminished for treatment of SWE. The decrease in mineralization efficiency during the treatment of SWE can be explained by (i) the presence of natural organic matter in SWE which could scavenge hydroxyl radicals that reduce the amount of • OH available for oxidation of OFLO and (ii) consumption of • OH in reactions with inorganic ions such as Cland HCO3present in SWE, with generation of less reactive radicals such as ClOH •and CO3 •- [23], [40].…”
Section: Synergistic Effects Of • Oh and Bdd( • Oh) On Oxidation Of Oflomentioning
confidence: 99%
“…The contribution of M( • OH) to EF process is strongly related to the nature of anode material, as well as in the overall performance of AO [23]. Anodes characterized with high O2-evolution overpotential are regarded as "non-active" anodes, while those with low O2-evolution overpotential are of the "active anodes" type.…”
Section: Introductionmentioning
confidence: 99%
“…Electrochemical degradation has been widely investigated based on the oxidation of pollutants by hydroxy radical (OH•) generated, which has been applied in the treatment of textile effluent [11]. So far, tank electrolyzers have been widely used in then the treatment of textile effluent [12]. The tube electrolyzer with high mass transfer efficiency and compact structure is regarded as a potential electrolyzer type for the electrochemical degradation [13].…”
Section: Introductionmentioning
confidence: 99%