Differentiating the reaction mechanism of three-dimensionally electrocatalytic system packed with different particle electrodes: Electro-oxidation versus electro-fenton

Recently, there are still some controversial mechanisms of the 3D electrocatalytic oxidation system, which would probably confound its industrial application. From the conventional viewpoint, the Ti4O7 material may be the desired particle electrodes in the 3D system since its high oxygen evolution p...

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Veröffentlicht in:Chemosphere (Oxford) 2023-06, Vol.325, p.138423-138423, Article 138423
Hauptverfasser: Xiao, Huiji, Hao, Yongjie, Wu, Jingli, Meng, Xianzhe, Feng, Fei, Xu, Fengqi, Luo, Siyi, Jiang, Bo
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container_start_page 138423
container_title Chemosphere (Oxford)
container_volume 325
creator Xiao, Huiji
Hao, Yongjie
Wu, Jingli
Meng, Xianzhe
Feng, Fei
Xu, Fengqi
Luo, Siyi
Jiang, Bo
description Recently, there are still some controversial mechanisms of the 3D electrocatalytic oxidation system, which would probably confound its industrial application. From the conventional viewpoint, the Ti4O7 material may be the desired particle electrodes in the 3D system since its high oxygen evolution potential favors the production of •OH via H2O splitting reaction at the anode side of Ti4O7 particle electrodes. In fact, the incorporation of Ti4O7 particles showed phenol degradation of 88% and COD removal of 51% within 120 min, under the optimum conditions at energy consumption of 0.668 kWh g−1 COD, the performance of which was much lower than those in many previous literatures. In contrast, the prepared carbon black-polytetrafluoroethylene composite (CB-PTFE) particles with abundant oxygen-containing functional groups could yield considerable amounts of H2O2 (200 mg L−1) in the 3D reactor and achieved a complete degradation of phenol and COD removal of 80% in the presence of Fe2+, accompanying a low energy consumption of only 0.080 kWh g−1 COD. It was estimated that only 20% of Ti4O7 particles near the anode attained the potential over 2.73 V/SCE at 30 mA cm−2 based on the potential test and simulation, responsible for the low yield of •OH via the H2O splitting on Ti4O7 (1.74 × 10−14 M), and the main role of Ti4O7 particle electrodes in phenol degradation was through direct oxidation. For the CB-PTFE-based 3D system, current density of 10 mA cm−2 was sufficient for all the CB-PTFE particles to attain cathodic potential of −0.67 V/SCE, conducive to the high yield of H2O2 and •OH (9.11 × 10−14 M) in the presence of Fe2+, and the •OH-mediated indirect oxidation was mainly responsible for the phenol degradation. Generally, this study can provide a deep insight into the 3D electrocatalytic oxidation technology and help to develop the high-efficiency and cost-efficient 3D technologies for industrial application. [Display omitted] •Mechanism of 3D electrocatalytic oxidation system with particles was clarified.•Only 20% of Ti4O7 particles obtain sufficient induction potential for .•OH production.•Ti4O7 particles used for phenol degradation was mainly via direct oxidation.•Carbon black-PTFE particles-based 3D system follows an electro-Fenton regime.•Carbon black-PTFE particles achieved a complete phenol degradation.
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From the conventional viewpoint, the Ti4O7 material may be the desired particle electrodes in the 3D system since its high oxygen evolution potential favors the production of •OH via H2O splitting reaction at the anode side of Ti4O7 particle electrodes. In fact, the incorporation of Ti4O7 particles showed phenol degradation of 88% and COD removal of 51% within 120 min, under the optimum conditions at energy consumption of 0.668 kWh g−1 COD, the performance of which was much lower than those in many previous literatures. In contrast, the prepared carbon black-polytetrafluoroethylene composite (CB-PTFE) particles with abundant oxygen-containing functional groups could yield considerable amounts of H2O2 (200 mg L−1) in the 3D reactor and achieved a complete degradation of phenol and COD removal of 80% in the presence of Fe2+, accompanying a low energy consumption of only 0.080 kWh g−1 COD. It was estimated that only 20% of Ti4O7 particles near the anode attained the potential over 2.73 V/SCE at 30 mA cm−2 based on the potential test and simulation, responsible for the low yield of •OH via the H2O splitting on Ti4O7 (1.74 × 10−14 M), and the main role of Ti4O7 particle electrodes in phenol degradation was through direct oxidation. For the CB-PTFE-based 3D system, current density of 10 mA cm−2 was sufficient for all the CB-PTFE particles to attain cathodic potential of −0.67 V/SCE, conducive to the high yield of H2O2 and •OH (9.11 × 10−14 M) in the presence of Fe2+, and the •OH-mediated indirect oxidation was mainly responsible for the phenol degradation. Generally, this study can provide a deep insight into the 3D electrocatalytic oxidation technology and help to develop the high-efficiency and cost-efficient 3D technologies for industrial application. [Display omitted] •Mechanism of 3D electrocatalytic oxidation system with particles was clarified.•Only 20% of Ti4O7 particles obtain sufficient induction potential for .•OH production.•Ti4O7 particles used for phenol degradation was mainly via direct oxidation.•Carbon black-PTFE particles-based 3D system follows an electro-Fenton regime.•Carbon black-PTFE particles achieved a complete phenol degradation.</description><identifier>ISSN: 0045-6535</identifier><identifier>EISSN: 1879-1298</identifier><identifier>DOI: 10.1016/j.chemosphere.2023.138423</identifier><identifier>PMID: 36934480</identifier><language>eng</language><publisher>England: Elsevier Ltd</publisher><subject>anodes ; carbon ; Carbon black ; chemical oxygen demand ; cost effectiveness ; Electro-Fenton ; Electrodes ; energy ; Hydrogen Peroxide ; industrial applications ; oxidation ; Oxidation-Reduction ; oxygen production ; Particle electrodes ; Phenol ; Phenols ; reaction mechanisms ; Three-dimensional electrochemical system ; Ti4O7 ; Water Pollutants, Chemical - analysis</subject><ispartof>Chemosphere (Oxford), 2023-06, Vol.325, p.138423-138423, Article 138423</ispartof><rights>2023 Elsevier Ltd</rights><rights>Copyright © 2023 Elsevier Ltd. 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From the conventional viewpoint, the Ti4O7 material may be the desired particle electrodes in the 3D system since its high oxygen evolution potential favors the production of •OH via H2O splitting reaction at the anode side of Ti4O7 particle electrodes. In fact, the incorporation of Ti4O7 particles showed phenol degradation of 88% and COD removal of 51% within 120 min, under the optimum conditions at energy consumption of 0.668 kWh g−1 COD, the performance of which was much lower than those in many previous literatures. In contrast, the prepared carbon black-polytetrafluoroethylene composite (CB-PTFE) particles with abundant oxygen-containing functional groups could yield considerable amounts of H2O2 (200 mg L−1) in the 3D reactor and achieved a complete degradation of phenol and COD removal of 80% in the presence of Fe2+, accompanying a low energy consumption of only 0.080 kWh g−1 COD. It was estimated that only 20% of Ti4O7 particles near the anode attained the potential over 2.73 V/SCE at 30 mA cm−2 based on the potential test and simulation, responsible for the low yield of •OH via the H2O splitting on Ti4O7 (1.74 × 10−14 M), and the main role of Ti4O7 particle electrodes in phenol degradation was through direct oxidation. For the CB-PTFE-based 3D system, current density of 10 mA cm−2 was sufficient for all the CB-PTFE particles to attain cathodic potential of −0.67 V/SCE, conducive to the high yield of H2O2 and •OH (9.11 × 10−14 M) in the presence of Fe2+, and the •OH-mediated indirect oxidation was mainly responsible for the phenol degradation. Generally, this study can provide a deep insight into the 3D electrocatalytic oxidation technology and help to develop the high-efficiency and cost-efficient 3D technologies for industrial application. [Display omitted] •Mechanism of 3D electrocatalytic oxidation system with particles was clarified.•Only 20% of Ti4O7 particles obtain sufficient induction potential for .•OH production.•Ti4O7 particles used for phenol degradation was mainly via direct oxidation.•Carbon black-PTFE particles-based 3D system follows an electro-Fenton regime.•Carbon black-PTFE particles achieved a complete phenol degradation.</description><subject>anodes</subject><subject>carbon</subject><subject>Carbon black</subject><subject>chemical oxygen demand</subject><subject>cost effectiveness</subject><subject>Electro-Fenton</subject><subject>Electrodes</subject><subject>energy</subject><subject>Hydrogen Peroxide</subject><subject>industrial applications</subject><subject>oxidation</subject><subject>Oxidation-Reduction</subject><subject>oxygen production</subject><subject>Particle electrodes</subject><subject>Phenol</subject><subject>Phenols</subject><subject>reaction mechanisms</subject><subject>Three-dimensional electrochemical system</subject><subject>Ti4O7</subject><subject>Water Pollutants, Chemical - analysis</subject><issn>0045-6535</issn><issn>1879-1298</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqNkctuFDEQRS0EIkPgF5DZsenBz26bHRrCQ4rEhqwtj11Ne-huD7YnYf6Iz4yTziB2YVVW1bl15boIvaFkTQlt3-3WboAp5v0ACdaMML6mXAnGn6AVVZ1uKNPqKVoRImTTSi7P0Iucd4RUsdTP0RlvNRdCkRX68zH0fd0yl2BLmH_gMgBOYF0JccYTuMHOIU849nWSABofJphzHdpxPGIYwZUUnS12PJbgcD7mAhPeW_cTPL4JZcD-5FC7qTIjnGQe8nt8sbyb-Dt4e-96DSkf8glq-iqN80v0rLdjhlcP9Rxdfbr4vvnSXH77_HXz4bJxgpLS1M8qJTquNGuZ7BRjmlihpLBdx2UryBakl1xv2y1XzEstoe-07yvlW6UoP0dvl737FH8dIBczhexgHO0M8ZANJ4JwSUirHkVZp2oYWnWkonpBXYo5J-jNPoXJpqOhxNxlanbmn0zNXaZmybRqXz_YHLYT-L_KU4gV2CwA1LtcB0gmuwCzAx9SPaHxMfyHzS0uc7yH</recordid><startdate>20230601</startdate><enddate>20230601</enddate><creator>Xiao, Huiji</creator><creator>Hao, Yongjie</creator><creator>Wu, Jingli</creator><creator>Meng, Xianzhe</creator><creator>Feng, Fei</creator><creator>Xu, Fengqi</creator><creator>Luo, Siyi</creator><creator>Jiang, Bo</creator><general>Elsevier Ltd</general><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope><scope>7S9</scope><scope>L.6</scope><orcidid>https://orcid.org/0000-0001-9500-2145</orcidid></search><sort><creationdate>20230601</creationdate><title>Differentiating the reaction mechanism of three-dimensionally electrocatalytic system packed with different particle electrodes: Electro-oxidation versus electro-fenton</title><author>Xiao, Huiji ; Hao, Yongjie ; Wu, Jingli ; Meng, Xianzhe ; Feng, Fei ; Xu, Fengqi ; Luo, Siyi ; Jiang, Bo</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c410t-53588473892625782290a4854a7735640be5d539b6b382d595ef79df90ad68813</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>anodes</topic><topic>carbon</topic><topic>Carbon black</topic><topic>chemical oxygen demand</topic><topic>cost effectiveness</topic><topic>Electro-Fenton</topic><topic>Electrodes</topic><topic>energy</topic><topic>Hydrogen Peroxide</topic><topic>industrial applications</topic><topic>oxidation</topic><topic>Oxidation-Reduction</topic><topic>oxygen production</topic><topic>Particle electrodes</topic><topic>Phenol</topic><topic>Phenols</topic><topic>reaction mechanisms</topic><topic>Three-dimensional electrochemical system</topic><topic>Ti4O7</topic><topic>Water Pollutants, Chemical - analysis</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Xiao, Huiji</creatorcontrib><creatorcontrib>Hao, Yongjie</creatorcontrib><creatorcontrib>Wu, Jingli</creatorcontrib><creatorcontrib>Meng, Xianzhe</creatorcontrib><creatorcontrib>Feng, Fei</creatorcontrib><creatorcontrib>Xu, Fengqi</creatorcontrib><creatorcontrib>Luo, Siyi</creatorcontrib><creatorcontrib>Jiang, Bo</creatorcontrib><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><collection>AGRICOLA</collection><collection>AGRICOLA - Academic</collection><jtitle>Chemosphere (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Xiao, Huiji</au><au>Hao, Yongjie</au><au>Wu, Jingli</au><au>Meng, Xianzhe</au><au>Feng, Fei</au><au>Xu, Fengqi</au><au>Luo, Siyi</au><au>Jiang, Bo</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Differentiating the reaction mechanism of three-dimensionally electrocatalytic system packed with different particle electrodes: Electro-oxidation versus electro-fenton</atitle><jtitle>Chemosphere (Oxford)</jtitle><addtitle>Chemosphere</addtitle><date>2023-06-01</date><risdate>2023</risdate><volume>325</volume><spage>138423</spage><epage>138423</epage><pages>138423-138423</pages><artnum>138423</artnum><issn>0045-6535</issn><eissn>1879-1298</eissn><abstract>Recently, there are still some controversial mechanisms of the 3D electrocatalytic oxidation system, which would probably confound its industrial application. From the conventional viewpoint, the Ti4O7 material may be the desired particle electrodes in the 3D system since its high oxygen evolution potential favors the production of •OH via H2O splitting reaction at the anode side of Ti4O7 particle electrodes. In fact, the incorporation of Ti4O7 particles showed phenol degradation of 88% and COD removal of 51% within 120 min, under the optimum conditions at energy consumption of 0.668 kWh g−1 COD, the performance of which was much lower than those in many previous literatures. In contrast, the prepared carbon black-polytetrafluoroethylene composite (CB-PTFE) particles with abundant oxygen-containing functional groups could yield considerable amounts of H2O2 (200 mg L−1) in the 3D reactor and achieved a complete degradation of phenol and COD removal of 80% in the presence of Fe2+, accompanying a low energy consumption of only 0.080 kWh g−1 COD. It was estimated that only 20% of Ti4O7 particles near the anode attained the potential over 2.73 V/SCE at 30 mA cm−2 based on the potential test and simulation, responsible for the low yield of •OH via the H2O splitting on Ti4O7 (1.74 × 10−14 M), and the main role of Ti4O7 particle electrodes in phenol degradation was through direct oxidation. For the CB-PTFE-based 3D system, current density of 10 mA cm−2 was sufficient for all the CB-PTFE particles to attain cathodic potential of −0.67 V/SCE, conducive to the high yield of H2O2 and •OH (9.11 × 10−14 M) in the presence of Fe2+, and the •OH-mediated indirect oxidation was mainly responsible for the phenol degradation. Generally, this study can provide a deep insight into the 3D electrocatalytic oxidation technology and help to develop the high-efficiency and cost-efficient 3D technologies for industrial application. [Display omitted] •Mechanism of 3D electrocatalytic oxidation system with particles was clarified.•Only 20% of Ti4O7 particles obtain sufficient induction potential for .•OH production.•Ti4O7 particles used for phenol degradation was mainly via direct oxidation.•Carbon black-PTFE particles-based 3D system follows an electro-Fenton regime.•Carbon black-PTFE particles achieved a complete phenol degradation.</abstract><cop>England</cop><pub>Elsevier Ltd</pub><pmid>36934480</pmid><doi>10.1016/j.chemosphere.2023.138423</doi><tpages>1</tpages><orcidid>https://orcid.org/0000-0001-9500-2145</orcidid></addata></record>
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subjects anodes
carbon
Carbon black
chemical oxygen demand
cost effectiveness
Electro-Fenton
Electrodes
energy
Hydrogen Peroxide
industrial applications
oxidation
Oxidation-Reduction
oxygen production
Particle electrodes
Phenol
Phenols
reaction mechanisms
Three-dimensional electrochemical system
Ti4O7
Water Pollutants, Chemical - analysis
title Differentiating the reaction mechanism of three-dimensionally electrocatalytic system packed with different particle electrodes: Electro-oxidation versus electro-fenton
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