Continuous Heterogeneous Fenton-Type Process for Dye Pollution Abatement Intensified by Hydrodynamic Cavitation
The heterogeneous Fenton-type process was investigated in a continuous upflow fixed-bed reactor (UFBR) of a nano Prussian Blue catalyst supported on γ-alumina beads. Temperature and oxidant concentration strongly increased dye discoloration and total organic carbon (TOC) conversion. The long-term st...
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Veröffentlicht in: | Industrial & engineering chemistry research 2021-11, Vol.60 (46), p.16653-16664 |
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creator | Salierno, Gabriel Napoleone, Stefanía Maisterrena, María Agustina Cassanello, Miryan Pellasio, Maximiliano Doumic, Lucila Ayude, María Alejandra |
description | The heterogeneous Fenton-type process was investigated in a continuous upflow fixed-bed reactor (UFBR) of a nano Prussian Blue catalyst supported on γ-alumina beads. Temperature and oxidant concentration strongly increased dye discoloration and total organic carbon (TOC) conversion. The long-term stability of the catalyst was confirmed. The best performance was found with a residence time of 2 min at 353 K and an inlet hydrogen peroxide concentration twice the stoichiometric one required for mineralization, attaining complete discoloration and 45% TOC conversion. The formed reactive species continued the reaction after leaving the UFBR. Hydrodynamic cavitation (HC) of the collected outlet stream led immediately to complete discoloration and doubled the TOC conversion in 40 min. Short-chain carboxylic acids accounted for about 70% of the remaining TOC. The UFBR in-series with the HC reactor led to complete discoloration and intensified the TOC conversion. The subsequent HC step thoroughly consumed the remnant oxidant, increasing its efficiency. |
doi_str_mv | 10.1021/acs.iecr.1c02571 |
format | Article |
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Temperature and oxidant concentration strongly increased dye discoloration and total organic carbon (TOC) conversion. The long-term stability of the catalyst was confirmed. The best performance was found with a residence time of 2 min at 353 K and an inlet hydrogen peroxide concentration twice the stoichiometric one required for mineralization, attaining complete discoloration and 45% TOC conversion. The formed reactive species continued the reaction after leaving the UFBR. Hydrodynamic cavitation (HC) of the collected outlet stream led immediately to complete discoloration and doubled the TOC conversion in 40 min. Short-chain carboxylic acids accounted for about 70% of the remaining TOC. The UFBR in-series with the HC reactor led to complete discoloration and intensified the TOC conversion. The subsequent HC step thoroughly consumed the remnant oxidant, increasing its efficiency.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/acs.iecr.1c02571</identifier><language>eng</language><publisher>American Chemical Society</publisher><subject>Kinetics, Catalysis, and Reaction Engineering</subject><ispartof>Industrial & engineering chemistry research, 2021-11, Vol.60 (46), p.16653-16664</ispartof><rights>2021 American Chemical Society</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a280t-8863bcb6bd85b35df9035083fa04061522890d93d18472fe13c53dada367156f3</citedby><cites>FETCH-LOGICAL-a280t-8863bcb6bd85b35df9035083fa04061522890d93d18472fe13c53dada367156f3</cites><orcidid>0000-0001-8233-3797 ; 0000-0002-2903-0575 ; 0000-0002-3804-8179</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/acs.iecr.1c02571$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/acs.iecr.1c02571$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,776,780,2752,27053,27901,27902,56713,56763</link.rule.ids></links><search><creatorcontrib>Salierno, Gabriel</creatorcontrib><creatorcontrib>Napoleone, Stefanía</creatorcontrib><creatorcontrib>Maisterrena, María Agustina</creatorcontrib><creatorcontrib>Cassanello, Miryan</creatorcontrib><creatorcontrib>Pellasio, Maximiliano</creatorcontrib><creatorcontrib>Doumic, Lucila</creatorcontrib><creatorcontrib>Ayude, María Alejandra</creatorcontrib><title>Continuous Heterogeneous Fenton-Type Process for Dye Pollution Abatement Intensified by Hydrodynamic Cavitation</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>The heterogeneous Fenton-type process was investigated in a continuous upflow fixed-bed reactor (UFBR) of a nano Prussian Blue catalyst supported on γ-alumina beads. Temperature and oxidant concentration strongly increased dye discoloration and total organic carbon (TOC) conversion. The long-term stability of the catalyst was confirmed. The best performance was found with a residence time of 2 min at 353 K and an inlet hydrogen peroxide concentration twice the stoichiometric one required for mineralization, attaining complete discoloration and 45% TOC conversion. The formed reactive species continued the reaction after leaving the UFBR. Hydrodynamic cavitation (HC) of the collected outlet stream led immediately to complete discoloration and doubled the TOC conversion in 40 min. Short-chain carboxylic acids accounted for about 70% of the remaining TOC. The UFBR in-series with the HC reactor led to complete discoloration and intensified the TOC conversion. 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Eng. Chem. Res</addtitle><date>2021-11-24</date><risdate>2021</risdate><volume>60</volume><issue>46</issue><spage>16653</spage><epage>16664</epage><pages>16653-16664</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><abstract>The heterogeneous Fenton-type process was investigated in a continuous upflow fixed-bed reactor (UFBR) of a nano Prussian Blue catalyst supported on γ-alumina beads. Temperature and oxidant concentration strongly increased dye discoloration and total organic carbon (TOC) conversion. The long-term stability of the catalyst was confirmed. The best performance was found with a residence time of 2 min at 353 K and an inlet hydrogen peroxide concentration twice the stoichiometric one required for mineralization, attaining complete discoloration and 45% TOC conversion. The formed reactive species continued the reaction after leaving the UFBR. Hydrodynamic cavitation (HC) of the collected outlet stream led immediately to complete discoloration and doubled the TOC conversion in 40 min. Short-chain carboxylic acids accounted for about 70% of the remaining TOC. The UFBR in-series with the HC reactor led to complete discoloration and intensified the TOC conversion. The subsequent HC step thoroughly consumed the remnant oxidant, increasing its efficiency.</abstract><pub>American Chemical Society</pub><doi>10.1021/acs.iecr.1c02571</doi><tpages>12</tpages><orcidid>https://orcid.org/0000-0001-8233-3797</orcidid><orcidid>https://orcid.org/0000-0002-2903-0575</orcidid><orcidid>https://orcid.org/0000-0002-3804-8179</orcidid></addata></record> |
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subjects | Kinetics, Catalysis, and Reaction Engineering |
title | Continuous Heterogeneous Fenton-Type Process for Dye Pollution Abatement Intensified by Hydrodynamic Cavitation |
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