<p>In this study, three processes, Fenton, photo-Fenton, and photo-Fenton/adsorption hybrid, were evaluated for their ability to remove the fungicide Metalaxyl (MTX) from water. For the photo-Fenton and Fenton processes, three parameters (<i>i.e.</i> ferrous ion concentration, hydrogen peroxide and the pH of the aquatic medium) were optimized using the Doehlert three-parameter experimental design and response surface methodology. Metalaxyl degradation was determined by Liquid chromatography instrument coupled with a diode array detector. The mathematical models obtained were validated for each process. The optimal conditions were <InlineEquation ID="IEq1"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq1.gif" Format="GIF" Height="18" Rendition="HTML" Resolution="72" Type="Linedraw" Width="59" /> </InlineMediaObject> <EquationSource Format="TEX">\({C}_{{Fe}^{2+}}=\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mi>C</mi> <msup> <mrow> <mi mathvariant="italic">Fe</mi> </mrow> <mrow> <mn>2</mn> <mo>+</mo> </mrow> </msup> </msub> <mo>=</mo> </mrow> </math></EquationSource> </InlineEquation> 225&#xa0;mg L<sup>−1</sup>, <InlineEquation ID="IEq2"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq2.gif" Format="GIF" Height="19" Rendition="HTML" Resolution="72" Type="Linedraw" Width="102" /> </InlineMediaObject> <EquationSource Format="TEX">\({C}_{{H}_{2}{O}_{2}}=365.4\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mi>C</mi> <mrow> <msub> <mi>H</mi> <mn>2</mn> </msub> <msub> <mi>O</mi> <mn>2</mn> </msub> </mrow> </msub> <mo>=</mo> <mn>365.4</mn> </mrow> </math></EquationSource> </InlineEquation> mg L<sup>−1</sup> and pH = 3.4 for the both Fenton and photo-Fenton process. Under these conditions, 22% of Metalaxyl degraded during the photo-Fenton process and 20% during the Fenton process. The adsorption/photo-Fenton hybrid process was developed to achieve total removal of Metalaxyl using activated carbon elaborate from vegetable waste. This objective was reached after 240&#xa0;min using a two-stage process, 120&#xa0;min per stage, under the following conditions: <InlineEquation ID="IEq3"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq3.gif" Format="GIF" Height="18" Rendition="HTML" Resolution="72" Type="Linedraw" Width="41" /> </InlineMediaObject> <EquationSource Format="TEX">\({C}_{{Fe}^{2+}}\)</EquationSource> <EquationSource Format="MATHML"><math> <msub> <mi>C</mi> <msup> <mrow> <mi mathvariant="italic">Fe</mi> </mrow> <mrow> <mn>2</mn> <mo>+</mo> </mrow> </msup> </msub> </math></EquationSource> </InlineEquation>=25&#xa0;mg L<sup>−1</sup>, <InlineEquation ID="IEq4"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq4.gif" Format="GIF" Height="19" Rendition="HTML" Resolution="72" Type="Linedraw" Width="61" /> </InlineMediaObject> <EquationSource Format="TEX">\({C}_{{H}_{2}{O}_{2}}=\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mi>C</mi> <mrow> <msub> <mi>H</mi> <mn>2</mn> </msub> <msub> <mi>O</mi> <mn>2</mn> </msub> </mrow> </msub> <mo>=</mo> </mrow> </math></EquationSource> </InlineEquation> 382&#xa0;mg L<sup>−1</sup>and <InlineEquation ID="IEq5"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq5.gif" Format="GIF" Height="16" Rendition="HTML" Resolution="72" Type="Linedraw" Width="31" /> </InlineMediaObject> <EquationSource Format="TEX">\({D}_{Ac}\)</EquationSource> <EquationSource Format="MATHML"><math> <msub> <mi>D</mi> <mrow> <mi mathvariant="italic">Ac</mi> </mrow> </msub> </math></EquationSource> </InlineEquation>=100&#xa0;mg L<sup>−1</sup> for the first stage and <InlineEquation ID="IEq6"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq3.gif" Format="GIF" Height="18" Rendition="HTML" Resolution="72" Type="Linedraw" Width="41" /> </InlineMediaObject> <EquationSource Format="TEX">\({C}_{{Fe}^{2+}}\)</EquationSource> <EquationSource Format="MATHML"><math> <msub> <mi>C</mi> <msup> <mrow> <mi mathvariant="italic">Fe</mi> </mrow> <mrow> <mn>2</mn> <mo>+</mo> </mrow> </msup> </msub> </math></EquationSource> </InlineEquation>=10&#xa0;mg L<sup>−1</sup>, <InlineEquation ID="IEq7"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq4.gif" Format="GIF" Height="19" Rendition="HTML" Resolution="72" Type="Linedraw" Width="61" /> </InlineMediaObject> <EquationSource Format="TEX">\({C}_{{H}_{2}{O}_{2}}=\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mi>C</mi> <mrow> <msub> <mi>H</mi> <mn>2</mn> </msub> <msub> <mi>O</mi> <mn>2</mn> </msub> </mrow> </msub> <mo>=</mo> </mrow> </math></EquationSource> </InlineEquation> 133&#xa0;mg L<sup>−1</sup>and <InlineEquation ID="IEq8"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="13762_2025_6407_Article_IEq5.gif" Format="GIF" Height="16" Rendition="HTML" Resolution="72" Type="Linedraw" Width="31" /> </InlineMediaObject> <EquationSource Format="TEX">\({D}_{Ac}\)</EquationSource> <EquationSource Format="MATHML"><math> <msub> <mi>D</mi> <mrow> <mi mathvariant="italic">Ac</mi> </mrow> </msub> </math></EquationSource> </InlineEquation>= 34&#xa0;mg L<sup>−1</sup> for the second one. A novel combination of a quick, easy, cheap, effective, rugged, and safe extraction method, pre-concentration by evaporation and Gas Chromatography coupled with triple quadrupole Mass Spectrometry analysis was used to identify the photo-degradation by-products at ultra-trace levels. Five by-products were identified and three possible degradation pathways were also proposed.</p>

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Novel approach based on removal of Metalaxyl by Advanced Oxidation process and hybrid-process: identification and mechanism pathway

  • C. Zekkaoui,
  • T. Berrama,
  • D. Dumoulin,
  • G. Billon,
  • Y. Kadmi

摘要

In this study, three processes, Fenton, photo-Fenton, and photo-Fenton/adsorption hybrid, were evaluated for their ability to remove the fungicide Metalaxyl (MTX) from water. For the photo-Fenton and Fenton processes, three parameters (i.e. ferrous ion concentration, hydrogen peroxide and the pH of the aquatic medium) were optimized using the Doehlert three-parameter experimental design and response surface methodology. Metalaxyl degradation was determined by Liquid chromatography instrument coupled with a diode array detector. The mathematical models obtained were validated for each process. The optimal conditions were \({C}_{{Fe}^{2+}}=\) C Fe 2 + = 225 mg L−1, \({C}_{{H}_{2}{O}_{2}}=365.4\) C H 2 O 2 = 365.4 mg L−1 and pH = 3.4 for the both Fenton and photo-Fenton process. Under these conditions, 22% of Metalaxyl degraded during the photo-Fenton process and 20% during the Fenton process. The adsorption/photo-Fenton hybrid process was developed to achieve total removal of Metalaxyl using activated carbon elaborate from vegetable waste. This objective was reached after 240 min using a two-stage process, 120 min per stage, under the following conditions: \({C}_{{Fe}^{2+}}\) C Fe 2 + =25 mg L−1, \({C}_{{H}_{2}{O}_{2}}=\) C H 2 O 2 = 382 mg L−1and \({D}_{Ac}\) D Ac =100 mg L−1 for the first stage and \({C}_{{Fe}^{2+}}\) C Fe 2 + =10 mg L−1, \({C}_{{H}_{2}{O}_{2}}=\) C H 2 O 2 = 133 mg L−1and \({D}_{Ac}\) D Ac = 34 mg L−1 for the second one. A novel combination of a quick, easy, cheap, effective, rugged, and safe extraction method, pre-concentration by evaporation and Gas Chromatography coupled with triple quadrupole Mass Spectrometry analysis was used to identify the photo-degradation by-products at ultra-trace levels. Five by-products were identified and three possible degradation pathways were also proposed.