Reduction of perchlorate using zero-valent titanium (ZVT) anode: Kinetic models

[Display omitted] ► Chloride showed a much higher adsorption affinity to chloride oxidation sites. ► Rate of perchlorate reduction and chloride oxidation was proportional to current. ► The rate constant of Ti(II) production was directly proportional to current. The kinetics of perchlorate reduction...

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Veröffentlicht in:Journal of colloid and interface science 2012-11, Vol.385 (1), p.122-129
Hauptverfasser: Lee, Chunwoo, Batchelor, Bill, Park, Sung Hyuk, Han, Dong Suk, Abdel-Wahab, Ahmed, Kramer, Timothy A.
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container_end_page 129
container_issue 1
container_start_page 122
container_title Journal of colloid and interface science
container_volume 385
creator Lee, Chunwoo
Batchelor, Bill
Park, Sung Hyuk
Han, Dong Suk
Abdel-Wahab, Ahmed
Kramer, Timothy A.
description [Display omitted] ► Chloride showed a much higher adsorption affinity to chloride oxidation sites. ► Rate of perchlorate reduction and chloride oxidation was proportional to current. ► The rate constant of Ti(II) production was directly proportional to current. The kinetics of perchlorate reduction by zero-valent titanium (ZVT) undergoing electrical pitting corrosion was described by interactions of two domains (pit and solution). Two kinetic models were developed based on two possible inhibition mechanisms. A competitive adsorption model was developed based on surface coverage of perchlorate and chloride on bare ZVT, and a Ti(II) consumption model was developed based on Ti(II) oxidation by electrochemically developed chlorine. Both models well predicted perchlorate concentration changes in the solution. The competitive adsorption model showed that chloride has a higher adsorption affinity on both sites where oxidative dissolution of ZVT occurs and where chloride oxidation occurs. Also, the rates of perchlorate removal and chloride oxidation were directly proportional to current applied. For the Ti(II) consumption model, the rate constant of Ti(II) production was dependent on current. The rate of chloride oxidation is also believed to be proportional to current, but this conclusion cannot be made with confidence. Both kinetic models described changes in perchlorate concentration well. However, the Ti(II) consumption model was limited in its ability to predict chloride concentration. This limitation was probably caused by a lack of available information like electrochemical oxidation of chloride on bare ZVT and Ti(II) oxidation by chlorine.
doi_str_mv 10.1016/j.jcis.2012.06.075
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The kinetics of perchlorate reduction by zero-valent titanium (ZVT) undergoing electrical pitting corrosion was described by interactions of two domains (pit and solution). Two kinetic models were developed based on two possible inhibition mechanisms. A competitive adsorption model was developed based on surface coverage of perchlorate and chloride on bare ZVT, and a Ti(II) consumption model was developed based on Ti(II) oxidation by electrochemically developed chlorine. Both models well predicted perchlorate concentration changes in the solution. The competitive adsorption model showed that chloride has a higher adsorption affinity on both sites where oxidative dissolution of ZVT occurs and where chloride oxidation occurs. Also, the rates of perchlorate removal and chloride oxidation were directly proportional to current applied. For the Ti(II) consumption model, the rate constant of Ti(II) production was dependent on current. The rate of chloride oxidation is also believed to be proportional to current, but this conclusion cannot be made with confidence. Both kinetic models described changes in perchlorate concentration well. However, the Ti(II) consumption model was limited in its ability to predict chloride concentration. 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The kinetics of perchlorate reduction by zero-valent titanium (ZVT) undergoing electrical pitting corrosion was described by interactions of two domains (pit and solution). Two kinetic models were developed based on two possible inhibition mechanisms. A competitive adsorption model was developed based on surface coverage of perchlorate and chloride on bare ZVT, and a Ti(II) consumption model was developed based on Ti(II) oxidation by electrochemically developed chlorine. Both models well predicted perchlorate concentration changes in the solution. The competitive adsorption model showed that chloride has a higher adsorption affinity on both sites where oxidative dissolution of ZVT occurs and where chloride oxidation occurs. Also, the rates of perchlorate removal and chloride oxidation were directly proportional to current applied. For the Ti(II) consumption model, the rate constant of Ti(II) production was dependent on current. The rate of chloride oxidation is also believed to be proportional to current, but this conclusion cannot be made with confidence. Both kinetic models described changes in perchlorate concentration well. However, the Ti(II) consumption model was limited in its ability to predict chloride concentration. This limitation was probably caused by a lack of available information like electrochemical oxidation of chloride on bare ZVT and Ti(II) oxidation by chlorine.</description><subject>Adsorption</subject><subject>Anode</subject><subject>Chemistry</subject><subject>Chlorides</subject><subject>chlorine</subject><subject>corrosion</subject><subject>Electrochemistry</subject><subject>electrodes</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>Kinetic model</subject><subject>Mathematical models</subject><subject>Oxidation</subject><subject>Perchlorate</subject><subject>Perchlorates</subject><subject>Pitting (corrosion)</subject><subject>Reduction</subject><subject>Surface chemistry</subject><subject>Surface physical chemistry</subject><subject>titanium</subject><subject>Zero-valent titanium</subject><issn>0021-9797</issn><issn>1095-7103</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNqF0E1v1DAQBmALUdGl8Ac4QC6VyiFhHCe2g3pBFV-iUiVoOXCxHGdcvErsxU4qlV-Po116hJM10jPvWC8hLyhUFCh_s622xqWqBlpXwCsQ7SOyodC1paDAHpMNQE3LTnTimDxNaQtAadt2T8hxXUshAdiGXH3FYTGzC74ItthhND_HEPWMxZKcvy1-YwzlnR7Rz8XsZu3dMhVnP75fvy60DwO-Lb44j7MzxZSnMT0jR1aPCZ8f3hNy8-H99cWn8vLq4-eLd5elaRo2lygNt6axlLNh0JJj09hGG6mbltq-54L2HfAWGGphJOdWypprUbPeAOuMYSfkbJ-7i-HXgmlWk0sGx1F7DEtSlDLOOG1r-X8KrM2uAZFpvacmhpQiWrWLbtLxPiO1dq62au1crZ0r4Cp3npdeHvKXfsLhYeVvyRmcHoBORo82ar9mPDjOGir4ev3V3lkdlL6N2dx8y5c4AAghO5rF-V7kpvHOYVTJOPQGBxfRzGoI7l8__QNXO6e3</recordid><startdate>20121101</startdate><enddate>20121101</enddate><creator>Lee, Chunwoo</creator><creator>Batchelor, Bill</creator><creator>Park, Sung Hyuk</creator><creator>Han, Dong Suk</creator><creator>Abdel-Wahab, Ahmed</creator><creator>Kramer, Timothy A.</creator><general>Elsevier Inc</general><general>Elsevier</general><scope>FBQ</scope><scope>IQODW</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope><scope>7SE</scope><scope>7U5</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>20121101</creationdate><title>Reduction of perchlorate using zero-valent titanium (ZVT) anode: Kinetic models</title><author>Lee, Chunwoo ; Batchelor, Bill ; Park, Sung Hyuk ; Han, Dong Suk ; Abdel-Wahab, Ahmed ; Kramer, Timothy A.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c443t-e8c6fc4f163dda86e44f4ac8a451fbb671b906503ea7c866f8826a723bc039cc3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Adsorption</topic><topic>Anode</topic><topic>Chemistry</topic><topic>Chlorides</topic><topic>chlorine</topic><topic>corrosion</topic><topic>Electrochemistry</topic><topic>electrodes</topic><topic>Exact sciences and technology</topic><topic>General and physical chemistry</topic><topic>Kinetic model</topic><topic>Mathematical models</topic><topic>Oxidation</topic><topic>Perchlorate</topic><topic>Perchlorates</topic><topic>Pitting (corrosion)</topic><topic>Reduction</topic><topic>Surface chemistry</topic><topic>Surface physical chemistry</topic><topic>titanium</topic><topic>Zero-valent titanium</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Lee, Chunwoo</creatorcontrib><creatorcontrib>Batchelor, Bill</creatorcontrib><creatorcontrib>Park, Sung Hyuk</creatorcontrib><creatorcontrib>Han, Dong Suk</creatorcontrib><creatorcontrib>Abdel-Wahab, Ahmed</creatorcontrib><creatorcontrib>Kramer, Timothy A.</creatorcontrib><collection>AGRIS</collection><collection>Pascal-Francis</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><collection>Corrosion Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Journal of colloid and interface science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Lee, Chunwoo</au><au>Batchelor, Bill</au><au>Park, Sung Hyuk</au><au>Han, Dong Suk</au><au>Abdel-Wahab, Ahmed</au><au>Kramer, Timothy A.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Reduction of perchlorate using zero-valent titanium (ZVT) anode: Kinetic models</atitle><jtitle>Journal of colloid and interface science</jtitle><addtitle>J Colloid Interface Sci</addtitle><date>2012-11-01</date><risdate>2012</risdate><volume>385</volume><issue>1</issue><spage>122</spage><epage>129</epage><pages>122-129</pages><issn>0021-9797</issn><eissn>1095-7103</eissn><coden>JCISA5</coden><abstract>[Display omitted] ► Chloride showed a much higher adsorption affinity to chloride oxidation sites. ► Rate of perchlorate reduction and chloride oxidation was proportional to current. ► The rate constant of Ti(II) production was directly proportional to current. The kinetics of perchlorate reduction by zero-valent titanium (ZVT) undergoing electrical pitting corrosion was described by interactions of two domains (pit and solution). Two kinetic models were developed based on two possible inhibition mechanisms. A competitive adsorption model was developed based on surface coverage of perchlorate and chloride on bare ZVT, and a Ti(II) consumption model was developed based on Ti(II) oxidation by electrochemically developed chlorine. Both models well predicted perchlorate concentration changes in the solution. The competitive adsorption model showed that chloride has a higher adsorption affinity on both sites where oxidative dissolution of ZVT occurs and where chloride oxidation occurs. Also, the rates of perchlorate removal and chloride oxidation were directly proportional to current applied. For the Ti(II) consumption model, the rate constant of Ti(II) production was dependent on current. The rate of chloride oxidation is also believed to be proportional to current, but this conclusion cannot be made with confidence. Both kinetic models described changes in perchlorate concentration well. However, the Ti(II) consumption model was limited in its ability to predict chloride concentration. This limitation was probably caused by a lack of available information like electrochemical oxidation of chloride on bare ZVT and Ti(II) oxidation by chlorine.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><pmid>22878003</pmid><doi>10.1016/j.jcis.2012.06.075</doi><tpages>8</tpages></addata></record>
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subjects Adsorption
Anode
Chemistry
Chlorides
chlorine
corrosion
Electrochemistry
electrodes
Exact sciences and technology
General and physical chemistry
Kinetic model
Mathematical models
Oxidation
Perchlorate
Perchlorates
Pitting (corrosion)
Reduction
Surface chemistry
Surface physical chemistry
titanium
Zero-valent titanium
title Reduction of perchlorate using zero-valent titanium (ZVT) anode: Kinetic models
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