A semi-empirical model for adsorption of magnesium ion from magnesium impurity-containing saturated boric acid solutions on Amberlite IR-120 resin
In this study, the use of Amberlite IR-120, strong acidic cation exchange resin, was investigated to remove magnesium impurity from saturated boric acid solutions. The magnesium impurity caused by magnesium compounds in raw colemanite is a very important problem, which has to be solved by the indust...
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Veröffentlicht in: | Fresenius environmental bulletin 2007-01, Vol.16 (7), p.720-725 |
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description | In this study, the use of Amberlite IR-120, strong acidic cation exchange resin, was investigated to remove magnesium impurity from saturated boric acid solutions. The magnesium impurity caused by magnesium compounds in raw colemanite is a very important problem, which has to be solved by the industry. The experiments were carried out in a batch reactor. Adsorption kinetics of magnesium was studied as a function of resin/solution ratio (g/100 mL), initial solution pH and temperature (K). The obtained kinetic data were employed with pseudo-first order and pseudo-second order models. It was determined that the pseudo-second order model was the best fitting kinetic model. Furthermore, a semi empirical model was developed to predict operational conditions of the batch process in the following form; t/ sub(q1)=313.737x[H] super(0.0055)x(S/L) super(0.9228)xexp(-5209.856/RT)x t super(1.0129). |
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The magnesium impurity caused by magnesium compounds in raw colemanite is a very important problem, which has to be solved by the industry. The experiments were carried out in a batch reactor. Adsorption kinetics of magnesium was studied as a function of resin/solution ratio (g/100 mL), initial solution pH and temperature (K). The obtained kinetic data were employed with pseudo-first order and pseudo-second order models. It was determined that the pseudo-second order model was the best fitting kinetic model. Furthermore, a semi empirical model was developed to predict operational conditions of the batch process in the following form; t/ sub(q1)=313.737x[H] super(0.0055)x(S/L) super(0.9228)xexp(-5209.856/RT)x t super(1.0129).</description><identifier>ISSN: 1018-4619</identifier><language>eng</language><subject>Adsorption ; Cations ; Kinetics ; Magnesium ; Magnesium compounds ; Q1 ; Resins ; Temperature</subject><ispartof>Fresenius environmental bulletin, 2007-01, Vol.16 (7), p.720-725</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784</link.rule.ids></links><search><creatorcontrib>Oezmetin, C</creatorcontrib><creatorcontrib>Aydin, Oe</creatorcontrib><title>A semi-empirical model for adsorption of magnesium ion from magnesium impurity-containing saturated boric acid solutions on Amberlite IR-120 resin</title><title>Fresenius environmental bulletin</title><description>In this study, the use of Amberlite IR-120, strong acidic cation exchange resin, was investigated to remove magnesium impurity from saturated boric acid solutions. The magnesium impurity caused by magnesium compounds in raw colemanite is a very important problem, which has to be solved by the industry. The experiments were carried out in a batch reactor. Adsorption kinetics of magnesium was studied as a function of resin/solution ratio (g/100 mL), initial solution pH and temperature (K). The obtained kinetic data were employed with pseudo-first order and pseudo-second order models. It was determined that the pseudo-second order model was the best fitting kinetic model. Furthermore, a semi empirical model was developed to predict operational conditions of the batch process in the following form; t/ sub(q1)=313.737x[H] super(0.0055)x(S/L) super(0.9228)xexp(-5209.856/RT)x t super(1.0129).</description><subject>Adsorption</subject><subject>Cations</subject><subject>Kinetics</subject><subject>Magnesium</subject><subject>Magnesium compounds</subject><subject>Q1</subject><subject>Resins</subject><subject>Temperature</subject><issn>1018-4619</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNqFz81KxDAQB_AeFFzWfYc5eQskadomx7L4sbAgiJ6XtJ0skXzUJD34Gj6xXfTgzbkM85_hB3NVbRhlkoiWqZtql_M7XavlHW_rTfXVQ0ZvCfrZJjtqBz5O6MDEBHrKMc3FxgDRgNfngNkuHi6BSdH_jfy8JFs-yRhD0TbYcIasy5J0wQmGuNKgRztBjm65iBlWpPcDJmcLwuGFME4hrVq4ra6Ndhl3v31bvT3cv-6fyPH58bDvj2TmrCtENKjUwLkUOCk9ctm1oqFKML7OlKrxsqsnw8wg1nelHBsjZWOY7HjXUqy31d2PO6f4sWAuJ2_ziM7pgHHJp5oypgSV_x5yylUnVFt_A1LDcVo</recordid><startdate>20070101</startdate><enddate>20070101</enddate><creator>Oezmetin, C</creator><creator>Aydin, Oe</creator><scope>8FD</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>20070101</creationdate><title>A semi-empirical model for adsorption of magnesium ion from magnesium impurity-containing saturated boric acid solutions on Amberlite IR-120 resin</title><author>Oezmetin, C ; Aydin, Oe</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-p217t-45e99b2284ed9ac28764509412ed9009cb2283df1fb406288c5f885f1872760e3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Adsorption</topic><topic>Cations</topic><topic>Kinetics</topic><topic>Magnesium</topic><topic>Magnesium compounds</topic><topic>Q1</topic><topic>Resins</topic><topic>Temperature</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Oezmetin, C</creatorcontrib><creatorcontrib>Aydin, Oe</creatorcontrib><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Fresenius environmental bulletin</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Oezmetin, C</au><au>Aydin, Oe</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A semi-empirical model for adsorption of magnesium ion from magnesium impurity-containing saturated boric acid solutions on Amberlite IR-120 resin</atitle><jtitle>Fresenius environmental bulletin</jtitle><date>2007-01-01</date><risdate>2007</risdate><volume>16</volume><issue>7</issue><spage>720</spage><epage>725</epage><pages>720-725</pages><issn>1018-4619</issn><abstract>In this study, the use of Amberlite IR-120, strong acidic cation exchange resin, was investigated to remove magnesium impurity from saturated boric acid solutions. The magnesium impurity caused by magnesium compounds in raw colemanite is a very important problem, which has to be solved by the industry. The experiments were carried out in a batch reactor. Adsorption kinetics of magnesium was studied as a function of resin/solution ratio (g/100 mL), initial solution pH and temperature (K). The obtained kinetic data were employed with pseudo-first order and pseudo-second order models. It was determined that the pseudo-second order model was the best fitting kinetic model. Furthermore, a semi empirical model was developed to predict operational conditions of the batch process in the following form; t/ sub(q1)=313.737x[H] super(0.0055)x(S/L) super(0.9228)xexp(-5209.856/RT)x t super(1.0129).</abstract><tpages>6</tpages></addata></record> |
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subjects | Adsorption Cations Kinetics Magnesium Magnesium compounds Q1 Resins Temperature |
title | A semi-empirical model for adsorption of magnesium ion from magnesium impurity-containing saturated boric acid solutions on Amberlite IR-120 resin |
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