<?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>2026-09-21T13:06:56Z</responseDate><request verb="GetRecord" identifier="oai:dspace.mit.edu:1721.1/68533" metadataPrefix="dim">https://dspace.mit.edu/server/oai/request</request><GetRecord><record><header><identifier>oai:dspace.mit.edu:1721.1/68533</identifier><datestamp>2022-01-13T07:54:36Z</datestamp><setSpec>com_1721.1_7582</setSpec><setSpec>com_1721.1_7581</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">Gang Chen.</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="author" lang="en_US">Kleinguetl, Kevin (Kevin G.)</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="other" lang="en_US">Massachusetts Institute of Technology. Dept. 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">2012-01-12T19:35:16Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="available">2012-01-12T19:35:16Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="copyright" lang="en_US">2010</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="issued" lang="en_US">2011</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="uri">http://hdl.handle.net/1721.1/68533</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="oclc" lang="en_US">770954434</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">Thesis (S.B.)--Massachusetts Institute of Technology, Dept. of Mechanical Engineering, 2011.</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">"June 2011." Cataloged from PDF version of thesis.</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">Includes bibliographical references (p. 18).</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="abstract" lang="en_US">A recently demonstrated directional solvent technique for desalination of water has been tested for desalting seawater and shale gas 'frac' flowback water. The premise behind directional solvent extraction is that when certain organic oils such as decanoic acid are heated, they dissolve water without dissolving some other water soluble substances such as sodium chloride which can later be removed; upon cooling the absorbed water precipitates and is collected. This technique was tested to desalt a 3.5% w/w solution of sodium chloride in water, to simulate seawater salinity. The yield of water recovered as a fraction of the total weight of decanoic acid and its salinity was measured for various high operating temperatures. The average salinity of the recovered water was recorded to be 0.08%, while the yield percentage ranged between 0.32% and 1.65%, increasing with temperature. The same experiment was repeated using a 10.5% w/w solution of sodium chloride in water, to simulate 'frac' water salinity. In order to pave the way to practical application and commercialization of this technique, two industrial processes have been proposed; a one semi-continuous process and a fully continuous process which may be chosen depending on the throughput requirements, desired system size, and resource availability.</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="statementofresponsibility" lang="en_US">by Kevin Kleinguetl.</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">18 p.</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">Experimentation and application of directional solvent extraction for desalination of seawater and shale gas 'frac' flowback water</dim:field>
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   	&lt;Title>Experimentation and application of directional solvent extraction for desalination of seawater and shale gas &amp;apos;frac&amp;apos; flowback water&lt;/Title>
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   	&lt;PublicationDate>2011&lt;/PublicationDate>
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        	&lt;DisplayName>Kleinguetl, Kevin (Kevin G.)&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>A recently demonstrated directional solvent technique for desalination of water has been tested for desalting seawater and shale gas &amp;apos;frac&amp;apos; flowback water. The premise behind directional solvent extraction is that when certain organic oils such as decanoic acid are heated, they dissolve water without dissolving some other water soluble substances such as sodium chloride which can later be removed; upon cooling the absorbed water precipitates and is collected. This technique was tested to desalt a 3.5% w/w solution of sodium chloride in water, to simulate seawater salinity. The yield of water recovered as a fraction of the total weight of decanoic acid and its salinity was measured for various high operating temperatures. The average salinity of the recovered water was recorded to be 0.08%, while the yield percentage ranged between 0.32% and 1.65%, increasing with temperature. The same experiment was repeated using a 10.5% w/w solution of sodium chloride in water, to simulate &amp;apos;frac&amp;apos; water salinity. In order to pave the way to practical application and commercialization of this technique, two industrial processes have been proposed; a one semi-continuous process and a fully continuous process which may be chosen depending on the throughput requirements, desired system size, and resource availability.&lt;/Abstract>
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