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A Usable Kinetic Model of Suspended Ion Exchange Processes for Natural Organic Matter Removal
AbstractThe suspended ion exchange (SIEX) process is an emerging technology for the removal of dissolved natural organic matter (NOM). To facilitate the SIEX selection, design, and operation, a usable mechanistic model is proposed. The simple kinetic model unifies the Lagergren equation and the Glue...
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Published in: | Journal of environmental engineering (New York, N.Y.) N.Y.), 2021-12, Vol.147 (12) |
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creator | Qi, Shaoying S Boyer, Treavor H Hu, Yue |
description | AbstractThe suspended ion exchange (SIEX) process is an emerging technology for the removal of dissolved natural organic matter (NOM). To facilitate the SIEX selection, design, and operation, a usable mechanistic model is proposed. The simple kinetic model unifies the Lagergren equation and the Glueckauf model and has analytical solutions for common SIEX processes. It is shown, through comparison with experimental data, that the proposed model describes SIEX effectively. The plug-flow and the mixed-flow processes, such as SIX and MIEX, treat the removable NOM well. At (removable NOM) removal efficiency above 50%, though, both SIEX processes increasingly run into poor resin capacity utilization due to the process thermodynamic constraint and, to a lesser extent, the kinetic effect. The choice of chloride-form or bicarbonate-form resin has little effect on the adsorption distribution constant of removable NOM. Replacing chloride with bicarbonate as the counterion, however, increases the nonremovable NOM fraction, i.e., causes an additional amount of NOM unable to access the adsorption sites. The result of counterion binding suggests that the nonremovable NOM fraction is just a mixture of the NOM compounds that have insufficient affinity to displace resin counterion from adsorption sites and raises question on the hypothesis in the literature that attributes the nonremovable NOM to the uncharged NOM species only. |
doi_str_mv | 10.1061/(ASCE)EE.1943-7870.0001954 |
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To facilitate the SIEX selection, design, and operation, a usable mechanistic model is proposed. The simple kinetic model unifies the Lagergren equation and the Glueckauf model and has analytical solutions for common SIEX processes. It is shown, through comparison with experimental data, that the proposed model describes SIEX effectively. The plug-flow and the mixed-flow processes, such as SIX and MIEX, treat the removable NOM well. At (removable NOM) removal efficiency above 50%, though, both SIEX processes increasingly run into poor resin capacity utilization due to the process thermodynamic constraint and, to a lesser extent, the kinetic effect. The choice of chloride-form or bicarbonate-form resin has little effect on the adsorption distribution constant of removable NOM. Replacing chloride with bicarbonate as the counterion, however, increases the nonremovable NOM fraction, i.e., causes an additional amount of NOM unable to access the adsorption sites. The result of counterion binding suggests that the nonremovable NOM fraction is just a mixture of the NOM compounds that have insufficient affinity to displace resin counterion from adsorption sites and raises question on the hypothesis in the literature that attributes the nonremovable NOM to the uncharged NOM species only.</description><identifier>ISSN: 0733-9372</identifier><identifier>EISSN: 1943-7870</identifier><identifier>DOI: 10.1061/(ASCE)EE.1943-7870.0001954</identifier><language>eng</language><publisher>New York: American Society of Civil Engineers</publisher><subject>Adsorption ; Bicarbonates ; Chlorides ; Exact solutions ; Ion exchange ; New technology ; Organic matter ; Plug flow ; Resins ; Technical Papers</subject><ispartof>Journal of environmental engineering (New York, N.Y.), 2021-12, Vol.147 (12)</ispartof><rights>2021 American Society of Civil Engineers</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a337t-3c7bde1f793003362a092bce3b7b0576a68532120fe518606f593e8caf1f24363</citedby><cites>FETCH-LOGICAL-a337t-3c7bde1f793003362a092bce3b7b0576a68532120fe518606f593e8caf1f24363</cites><orcidid>0000-0003-0818-5604</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttp://ascelibrary.org/doi/pdf/10.1061/(ASCE)EE.1943-7870.0001954$$EPDF$$P50$$Gasce$$H</linktopdf><linktohtml>$$Uhttp://ascelibrary.org/doi/abs/10.1061/(ASCE)EE.1943-7870.0001954$$EHTML$$P50$$Gasce$$H</linktohtml><link.rule.ids>314,780,784,3252,10068,27924,27925,76191,76199</link.rule.ids></links><search><creatorcontrib>Qi, Shaoying S</creatorcontrib><creatorcontrib>Boyer, Treavor H</creatorcontrib><creatorcontrib>Hu, Yue</creatorcontrib><title>A Usable Kinetic Model of Suspended Ion Exchange Processes for Natural Organic Matter Removal</title><title>Journal of environmental engineering (New York, N.Y.)</title><description>AbstractThe suspended ion exchange (SIEX) process is an emerging technology for the removal of dissolved natural organic matter (NOM). To facilitate the SIEX selection, design, and operation, a usable mechanistic model is proposed. The simple kinetic model unifies the Lagergren equation and the Glueckauf model and has analytical solutions for common SIEX processes. It is shown, through comparison with experimental data, that the proposed model describes SIEX effectively. The plug-flow and the mixed-flow processes, such as SIX and MIEX, treat the removable NOM well. At (removable NOM) removal efficiency above 50%, though, both SIEX processes increasingly run into poor resin capacity utilization due to the process thermodynamic constraint and, to a lesser extent, the kinetic effect. The choice of chloride-form or bicarbonate-form resin has little effect on the adsorption distribution constant of removable NOM. Replacing chloride with bicarbonate as the counterion, however, increases the nonremovable NOM fraction, i.e., causes an additional amount of NOM unable to access the adsorption sites. The result of counterion binding suggests that the nonremovable NOM fraction is just a mixture of the NOM compounds that have insufficient affinity to displace resin counterion from adsorption sites and raises question on the hypothesis in the literature that attributes the nonremovable NOM to the uncharged NOM species only.</description><subject>Adsorption</subject><subject>Bicarbonates</subject><subject>Chlorides</subject><subject>Exact solutions</subject><subject>Ion exchange</subject><subject>New technology</subject><subject>Organic matter</subject><subject>Plug flow</subject><subject>Resins</subject><subject>Technical Papers</subject><issn>0733-9372</issn><issn>1943-7870</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNp1kFFLwzAUhYMoOKf_IeiLPnQmvW2y-DZG1eF04tyjhLS9mRu1mUkn-u9d2dQnny4czncufIScctbjTPDL88F0mF1kWY-rBCLZl6zHGOMqTfZI5zfbJx0mASIFMj4kRyEsN51EKNkhLwM6CyavkN4tamwWBb13JVbUWTpdhxXWJZZ05GqafRavpp4jffSuwBAwUOs8fTDN2puKTvzc1C1tmgY9fcI392GqY3JgTRXwZHe7ZHadPQ9vo_HkZjQcjCMDIJsICpmXyK1UwBiAiA1TcV4g5DJnqRRG9FOIecwsprwvmLCpAuwXxnIbJyCgS862uyvv3tcYGr10a19vXuo4lUopAEg3rattq_AuBI9Wr_zizfgvzZludWrd6tRZplt1ulWndzo3sNjCJhT4N_9D_g9-AxmQd-0</recordid><startdate>20211201</startdate><enddate>20211201</enddate><creator>Qi, Shaoying S</creator><creator>Boyer, Treavor H</creator><creator>Hu, Yue</creator><general>American Society of Civil Engineers</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7ST</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope><scope>SOI</scope><orcidid>https://orcid.org/0000-0003-0818-5604</orcidid></search><sort><creationdate>20211201</creationdate><title>A Usable Kinetic Model of Suspended Ion Exchange Processes for Natural Organic Matter Removal</title><author>Qi, Shaoying S ; Boyer, Treavor H ; Hu, Yue</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a337t-3c7bde1f793003362a092bce3b7b0576a68532120fe518606f593e8caf1f24363</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Adsorption</topic><topic>Bicarbonates</topic><topic>Chlorides</topic><topic>Exact solutions</topic><topic>Ion exchange</topic><topic>New technology</topic><topic>Organic matter</topic><topic>Plug flow</topic><topic>Resins</topic><topic>Technical Papers</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Qi, Shaoying S</creatorcontrib><creatorcontrib>Boyer, Treavor H</creatorcontrib><creatorcontrib>Hu, Yue</creatorcontrib><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Environment Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>Environment Abstracts</collection><jtitle>Journal of environmental engineering (New York, N.Y.)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Qi, Shaoying S</au><au>Boyer, Treavor H</au><au>Hu, Yue</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A Usable Kinetic Model of Suspended Ion Exchange Processes for Natural Organic Matter Removal</atitle><jtitle>Journal of environmental engineering (New York, N.Y.)</jtitle><date>2021-12-01</date><risdate>2021</risdate><volume>147</volume><issue>12</issue><issn>0733-9372</issn><eissn>1943-7870</eissn><abstract>AbstractThe suspended ion exchange (SIEX) process is an emerging technology for the removal of dissolved natural organic matter (NOM). To facilitate the SIEX selection, design, and operation, a usable mechanistic model is proposed. The simple kinetic model unifies the Lagergren equation and the Glueckauf model and has analytical solutions for common SIEX processes. It is shown, through comparison with experimental data, that the proposed model describes SIEX effectively. The plug-flow and the mixed-flow processes, such as SIX and MIEX, treat the removable NOM well. At (removable NOM) removal efficiency above 50%, though, both SIEX processes increasingly run into poor resin capacity utilization due to the process thermodynamic constraint and, to a lesser extent, the kinetic effect. The choice of chloride-form or bicarbonate-form resin has little effect on the adsorption distribution constant of removable NOM. Replacing chloride with bicarbonate as the counterion, however, increases the nonremovable NOM fraction, i.e., causes an additional amount of NOM unable to access the adsorption sites. The result of counterion binding suggests that the nonremovable NOM fraction is just a mixture of the NOM compounds that have insufficient affinity to displace resin counterion from adsorption sites and raises question on the hypothesis in the literature that attributes the nonremovable NOM to the uncharged NOM species only.</abstract><cop>New York</cop><pub>American Society of Civil Engineers</pub><doi>10.1061/(ASCE)EE.1943-7870.0001954</doi><orcidid>https://orcid.org/0000-0003-0818-5604</orcidid></addata></record> |
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subjects | Adsorption Bicarbonates Chlorides Exact solutions Ion exchange New technology Organic matter Plug flow Resins Technical Papers |
title | A Usable Kinetic Model of Suspended Ion Exchange Processes for Natural Organic Matter Removal |
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