<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-09-18T22:15:46Z</responseDate><request verb="GetRecord" identifier="oai:dspace.mit.edu:1721.1/98756" metadataPrefix="dim">https://dspace.mit.edu/server/oai/request</request><GetRecord><record><header><identifier>oai:dspace.mit.edu:1721.1/98756</identifier><datestamp>2022-01-13T07:54:05Z</datestamp><setSpec>com_1721.1_91570</setSpec><setSpec>com_1721.1_7582</setSpec><setSpec>com_1721.1_7581</setSpec><setSpec>col_1721.1_91571</setSpec><setSpec>col_1721.1_131024</setSpec></header><metadata><dim:dim xmlns:dim="http://www.dspace.org/xmlns/dspace/dim" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:doc="http://www.lyncode.com/xoai" xsi:schemaLocation="http://www.dspace.org/xmlns/dspace/dim http://www.dspace.org/schema/dim.xsd">
   <dim:field mdschema="dc" element="contributor" qualifier="advisor" lang="en_US">Amos Winter.</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="author" lang="en_US">Van de Zande, Georgia D</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="other" lang="en_US">Massachusetts Institute of Technology. Department of Mechanical Engineering.</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="department">Massachusetts Institute of Technology. Department of Mechanical Engineering</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="accessioned">2015-09-17T19:09:57Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="available">2015-09-17T19:09:57Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="copyright" lang="en_US">2015</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="issued" lang="en_US">2015</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="uri">http://hdl.handle.net/1721.1/98756</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="oclc" lang="en_US">920898848</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">Thesis: S.B., Massachusetts Institute of Technology, Department of Mechanical Engineering, 2015.</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">Cataloged from PDF version of thesis.</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">Includes bibliographical references (pages 39-40).</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="abstract" lang="en_US">This thesis tested and analyzed the removal rates of six different electrolytes: NaCl, Na2SO4 , MgCl2 , K2SO4 , Ca(NO3 )2, and CaSO4 when using electrodialysis reversal (EDR) desalination. A bench top EDR set-up was designed and built, and this set-up was used to desalinate feed water with initial concentrations of about 1000 ppm of each of the electrolytes. The tests ran until the diluate stream reached a concentration of 415 ppm. These results were then compared to a mathematical model that predicts the electrolyte removal behavior, and the experimental results did align with the model. When the mathematical model was used to estimate the electrolytes' behaviors for beginning concentrations of exactly 900 ppm, it was shown that the ranking of electrolytes with highest to lowest removal rates is NaCl (38.8 ppm/min when the diluate concentration is 415 ppm), K2SO4 (36.0 ppm/min), CaSO4 (33.6 ppm/min), Na2SO4 (33.4 ppm/min), MgCl2 (32.7 ppm/min), and Ca(NO3)2 (31.8 ppm/min).</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="statementofresponsibility" lang="en_US">by Georgia D. Van de Zande.</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="degree" lang="en_US">S.B.</dim:field>
   <dim:field mdschema="dc" element="format" qualifier="extent" lang="en_US">40 pages</dim:field>
   <dim:field mdschema="dc" element="language" qualifier="iso" lang="en_US">eng</dim:field>
   <dim:field mdschema="dc" element="publisher" lang="en_US">Massachusetts Institute of Technology</dim:field>
   <dim:field mdschema="dc" element="rights" lang="en_US">M.I.T. theses are protected by copyright. They may be viewed from this source for any purpose, but reproduction or distribution in any format is prohibited without written permission. See provided URL for inquiries about permission.</dim:field>
   <dim:field mdschema="dc" element="rights" qualifier="uri" lang="en_US">http://dspace.mit.edu/handle/1721.1/7582</dim:field>
   <dim:field mdschema="dc" element="subject" lang="en_US">Mechanical Engineering.</dim:field>
   <dim:field mdschema="dc" element="title" lang="en_US">Removal rates of electrolytes commonly found in brackish groundwater by means of electrodialysis reversal desalination</dim:field>
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	&lt;Language>eng&lt;/Language>
   	&lt;Title>Removal rates of electrolytes commonly found in brackish groundwater by means of electrodialysis reversal desalination&lt;/Title>
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   	&lt;PublicationDate>2015&lt;/PublicationDate>
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        	&lt;DisplayName>Van de Zande, Georgia D&lt;/DisplayName>
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            &lt;DisplayName>Massachusetts Institute of Technology&lt;/DisplayName>
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    &lt;Keyword>Mechanical Engineering.&lt;/Keyword>
   	&lt;Abstract>This thesis tested and analyzed the removal rates of six different electrolytes: NaCl, Na2SO4 , MgCl2 , K2SO4 , Ca(NO3 )2, and CaSO4 when using electrodialysis reversal (EDR) desalination. A bench top EDR set-up was designed and built, and this set-up was used to desalinate feed water with initial concentrations of about 1000 ppm of each of the electrolytes. The tests ran until the diluate stream reached a concentration of 415 ppm. These results were then compared to a mathematical model that predicts the electrolyte removal behavior, and the experimental results did align with the model. When the mathematical model was used to estimate the electrolytes&amp;apos; behaviors for beginning concentrations of exactly 900 ppm, it was shown that the ranking of electrolytes with highest to lowest removal rates is NaCl (38.8 ppm/min when the diluate concentration is 415 ppm), K2SO4 (36.0 ppm/min), CaSO4 (33.6 ppm/min), Na2SO4 (33.4 ppm/min), MgCl2 (32.7 ppm/min), and Ca(NO3)2 (31.8 ppm/min).&lt;/Abstract>
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