Amberlite IRA-93 and modified Amberlite IRA-93 resins for the uranyl ions extraction: optimization through factorial design methodology
This work reports the uranyl (UO22+) extraction from water by the resins Amberlite IRA-93 (A-IRA-93) and the new modified Amberlite IRA-93 (mA-IRA-93), by liquid-solid extraction. A comparative study investigated the extraction procedure for the solid phase extraction of toxic uranyl ions by both th...
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Veröffentlicht in: | Desalination and water treatment 2022-02, Vol.249, p.281-296 |
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description | This work reports the uranyl (UO22+) extraction from water by the resins Amberlite IRA-93 (A-IRA-93) and the new modified Amberlite IRA-93 (mA-IRA-93), by liquid-solid extraction. A comparative study investigated the extraction procedure for the solid phase extraction of toxic uranyl ions by both the Amberlite IRA-93 (A-IRA-93) and the modified Amberlite IRA-93 (mA-IRA-93) resins in a batch process. The effect of solution pH, contact time, initial uranyl concentration, ionic strength and temperature were evaluated. The extraction process followed a pseudo-second-order kinetics models for both resins. The thermodynamics data led to an endothermic process for the sorption of uranyl ions by both resins. Thermodynamic study showed a negative ΔG values for A-IRA-93 and mA-IRA-93, which indicated that the sorption process of uranyl ions was spontaneous. The ratio ΔGmA-IRA-93/ΔGA-IRA-93 = 10.58 shows that the extraction by the mA-IRA-93 was more spontaneous than the extraction by the A-IRA-93. The outcomes have shown that the optimal experimental conditions without addition of sodium acetate for the present study recommend the use of 0.03 g of A-IRA-93 and 0.02 g of mA-IRA-93 resins for initial uranyl concentration 10–4 mol L–1. Fractional experimental design 3(3–1) may provide a valuable basis for industrial scale applications and was adequate in this study. The best extraction yield for mA-IRA-93 resin was 100% at 3.5 pHi and an equilibration time of 30 min at 250 rpm, provided by experiment: w(mA-IRA-93) = 0.01 g, [UO22+] = 10–5 mol L–1 and [CH3COONa] = 0.2 mol L–1. Modified Amberlite IRA-93 showed better affinity towards UO22+ (a maximal capacity of 8.34 mg g–1) under optimum conditions. Modification of the resin Amberlite IRA-93 increases the retention capacity by a factor of 2.21. The two proposed adsorbents are cost-effective and environmentally friendly and potential candidates for treatment of water containing UO22+. The functionalized adsorbent (mA-IRA-93) has research value and application potential in real waste water treatment. |
doi_str_mv | 10.5004/dwt.2022.28145 |
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A comparative study investigated the extraction procedure for the solid phase extraction of toxic uranyl ions by both the Amberlite IRA-93 (A-IRA-93) and the modified Amberlite IRA-93 (mA-IRA-93) resins in a batch process. The effect of solution pH, contact time, initial uranyl concentration, ionic strength and temperature were evaluated. The extraction process followed a pseudo-second-order kinetics models for both resins. The thermodynamics data led to an endothermic process for the sorption of uranyl ions by both resins. Thermodynamic study showed a negative ΔG values for A-IRA-93 and mA-IRA-93, which indicated that the sorption process of uranyl ions was spontaneous. The ratio ΔGmA-IRA-93/ΔGA-IRA-93 = 10.58 shows that the extraction by the mA-IRA-93 was more spontaneous than the extraction by the A-IRA-93. The outcomes have shown that the optimal experimental conditions without addition of sodium acetate for the present study recommend the use of 0.03 g of A-IRA-93 and 0.02 g of mA-IRA-93 resins for initial uranyl concentration 10–4 mol L–1. Fractional experimental design 3(3–1) may provide a valuable basis for industrial scale applications and was adequate in this study. The best extraction yield for mA-IRA-93 resin was 100% at 3.5 pHi and an equilibration time of 30 min at 250 rpm, provided by experiment: w(mA-IRA-93) = 0.01 g, [UO22+] = 10–5 mol L–1 and [CH3COONa] = 0.2 mol L–1. Modified Amberlite IRA-93 showed better affinity towards UO22+ (a maximal capacity of 8.34 mg g–1) under optimum conditions. Modification of the resin Amberlite IRA-93 increases the retention capacity by a factor of 2.21. The two proposed adsorbents are cost-effective and environmentally friendly and potential candidates for treatment of water containing UO22+. The functionalized adsorbent (mA-IRA-93) has research value and application potential in real waste water treatment.</description><identifier>ISSN: 1944-3986</identifier><identifier>EISSN: 1944-3986</identifier><identifier>DOI: 10.5004/dwt.2022.28145</identifier><language>eng</language><publisher>Elsevier Inc</publisher><subject>Amberlite IRA-93 resin ; Extraction ; Optimization ; UO22</subject><ispartof>Desalination and water treatment, 2022-02, Vol.249, p.281-296</ispartof><rights>2022 Elsevier Inc.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c258t-b7fb5a4b4d6a318c0b55d5a5fa8632092d736361ec923b6dd25b49a3dd7eb0643</citedby><cites>FETCH-LOGICAL-c258t-b7fb5a4b4d6a318c0b55d5a5fa8632092d736361ec923b6dd25b49a3dd7eb0643</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Benmansour, Yasmine</creatorcontrib><creatorcontrib>Didi, Mohamed Amine</creatorcontrib><creatorcontrib>Abderarhim, Omar</creatorcontrib><title>Amberlite IRA-93 and modified Amberlite IRA-93 resins for the uranyl ions extraction: optimization through factorial design methodology</title><title>Desalination and water treatment</title><description>This work reports the uranyl (UO22+) extraction from water by the resins Amberlite IRA-93 (A-IRA-93) and the new modified Amberlite IRA-93 (mA-IRA-93), by liquid-solid extraction. A comparative study investigated the extraction procedure for the solid phase extraction of toxic uranyl ions by both the Amberlite IRA-93 (A-IRA-93) and the modified Amberlite IRA-93 (mA-IRA-93) resins in a batch process. The effect of solution pH, contact time, initial uranyl concentration, ionic strength and temperature were evaluated. The extraction process followed a pseudo-second-order kinetics models for both resins. The thermodynamics data led to an endothermic process for the sorption of uranyl ions by both resins. Thermodynamic study showed a negative ΔG values for A-IRA-93 and mA-IRA-93, which indicated that the sorption process of uranyl ions was spontaneous. The ratio ΔGmA-IRA-93/ΔGA-IRA-93 = 10.58 shows that the extraction by the mA-IRA-93 was more spontaneous than the extraction by the A-IRA-93. The outcomes have shown that the optimal experimental conditions without addition of sodium acetate for the present study recommend the use of 0.03 g of A-IRA-93 and 0.02 g of mA-IRA-93 resins for initial uranyl concentration 10–4 mol L–1. Fractional experimental design 3(3–1) may provide a valuable basis for industrial scale applications and was adequate in this study. The best extraction yield for mA-IRA-93 resin was 100% at 3.5 pHi and an equilibration time of 30 min at 250 rpm, provided by experiment: w(mA-IRA-93) = 0.01 g, [UO22+] = 10–5 mol L–1 and [CH3COONa] = 0.2 mol L–1. Modified Amberlite IRA-93 showed better affinity towards UO22+ (a maximal capacity of 8.34 mg g–1) under optimum conditions. Modification of the resin Amberlite IRA-93 increases the retention capacity by a factor of 2.21. The two proposed adsorbents are cost-effective and environmentally friendly and potential candidates for treatment of water containing UO22+. The functionalized adsorbent (mA-IRA-93) has research value and application potential in real waste water treatment.</description><subject>Amberlite IRA-93 resin</subject><subject>Extraction</subject><subject>Optimization</subject><subject>UO22</subject><issn>1944-3986</issn><issn>1944-3986</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2022</creationdate><recordtype>article</recordtype><recordid>eNp1UMtKA0EQXETBEHP1PD-w6-w89uEtBB-BgCB6HubRm4zs7oSZiRp_wN92YjwIYl-6uquraCrLLktccIzZlXmLBcGEFKQpGT_JJmXLWE7bpjr9hc-zWQgvOBVnNWdkkn3OBwW-txHQ8nGetxTJ0aDBGdtZMOgP6yHYMaDOeRQ3gHZejvseWZd28B691DHha-S20Q72Qx6mdOjdbr1BXWKdt7JHJrmsRzRA3DjjerfeX2RnnewDzH76NHu-vXla3Oerh7vlYr7KNeFNzFXdKS6ZYqaStGw0VpwbLnknm4oS3BJT04pWJeiWUFUZQ7hiraTG1KBwxeg0K46-2rsQPHRi6-0g_V6UWBySFClJcUhSfCeZBM1RAOmrVwteBG1h1GCsBx2FcfY_6Rc39Hvd</recordid><startdate>202202</startdate><enddate>202202</enddate><creator>Benmansour, Yasmine</creator><creator>Didi, Mohamed Amine</creator><creator>Abderarhim, Omar</creator><general>Elsevier Inc</general><scope>6I.</scope><scope>AAFTH</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>202202</creationdate><title>Amberlite IRA-93 and modified Amberlite IRA-93 resins for the uranyl ions extraction: optimization through factorial design methodology</title><author>Benmansour, Yasmine ; Didi, Mohamed Amine ; Abderarhim, Omar</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c258t-b7fb5a4b4d6a318c0b55d5a5fa8632092d736361ec923b6dd25b49a3dd7eb0643</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2022</creationdate><topic>Amberlite IRA-93 resin</topic><topic>Extraction</topic><topic>Optimization</topic><topic>UO22</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Benmansour, Yasmine</creatorcontrib><creatorcontrib>Didi, Mohamed Amine</creatorcontrib><creatorcontrib>Abderarhim, Omar</creatorcontrib><collection>ScienceDirect Open Access Titles</collection><collection>Elsevier:ScienceDirect:Open Access</collection><collection>CrossRef</collection><jtitle>Desalination and water treatment</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Benmansour, Yasmine</au><au>Didi, Mohamed Amine</au><au>Abderarhim, Omar</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Amberlite IRA-93 and modified Amberlite IRA-93 resins for the uranyl ions extraction: optimization through factorial design methodology</atitle><jtitle>Desalination and water treatment</jtitle><date>2022-02</date><risdate>2022</risdate><volume>249</volume><spage>281</spage><epage>296</epage><pages>281-296</pages><issn>1944-3986</issn><eissn>1944-3986</eissn><abstract>This work reports the uranyl (UO22+) extraction from water by the resins Amberlite IRA-93 (A-IRA-93) and the new modified Amberlite IRA-93 (mA-IRA-93), by liquid-solid extraction. A comparative study investigated the extraction procedure for the solid phase extraction of toxic uranyl ions by both the Amberlite IRA-93 (A-IRA-93) and the modified Amberlite IRA-93 (mA-IRA-93) resins in a batch process. The effect of solution pH, contact time, initial uranyl concentration, ionic strength and temperature were evaluated. The extraction process followed a pseudo-second-order kinetics models for both resins. The thermodynamics data led to an endothermic process for the sorption of uranyl ions by both resins. Thermodynamic study showed a negative ΔG values for A-IRA-93 and mA-IRA-93, which indicated that the sorption process of uranyl ions was spontaneous. The ratio ΔGmA-IRA-93/ΔGA-IRA-93 = 10.58 shows that the extraction by the mA-IRA-93 was more spontaneous than the extraction by the A-IRA-93. The outcomes have shown that the optimal experimental conditions without addition of sodium acetate for the present study recommend the use of 0.03 g of A-IRA-93 and 0.02 g of mA-IRA-93 resins for initial uranyl concentration 10–4 mol L–1. Fractional experimental design 3(3–1) may provide a valuable basis for industrial scale applications and was adequate in this study. The best extraction yield for mA-IRA-93 resin was 100% at 3.5 pHi and an equilibration time of 30 min at 250 rpm, provided by experiment: w(mA-IRA-93) = 0.01 g, [UO22+] = 10–5 mol L–1 and [CH3COONa] = 0.2 mol L–1. Modified Amberlite IRA-93 showed better affinity towards UO22+ (a maximal capacity of 8.34 mg g–1) under optimum conditions. Modification of the resin Amberlite IRA-93 increases the retention capacity by a factor of 2.21. The two proposed adsorbents are cost-effective and environmentally friendly and potential candidates for treatment of water containing UO22+. The functionalized adsorbent (mA-IRA-93) has research value and application potential in real waste water treatment.</abstract><pub>Elsevier Inc</pub><doi>10.5004/dwt.2022.28145</doi><tpages>16</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Amberlite IRA-93 resin Extraction Optimization UO22 |
title | Amberlite IRA-93 and modified Amberlite IRA-93 resins for the uranyl ions extraction: optimization through factorial design methodology |
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