<?xml version="1.0" encoding="ISO-8859-1"?><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance">
<front>
<journal-meta>
<journal-id>2007-8196</journal-id>
<journal-title><![CDATA[Epistemus (Sonora)]]></journal-title>
<abbrev-journal-title><![CDATA[Epistemus (Sonora)]]></abbrev-journal-title>
<issn>2007-8196</issn>
<publisher>
<publisher-name><![CDATA[Universidad de Sonora, División de Ingeniería]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S2007-81962022000100002</article-id>
<article-id pub-id-type="doi">10.36790/epistemus.v16i32.216</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Análisis de los extractantes CYANEX 272 y CYANEX 926p para la extracción del ion litio]]></article-title>
<article-title xml:lang="en"><![CDATA[Analysis of the Extractants CYANEX 272 and CYANEX 926p for the Extraction of Lithium Ion]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Solís Hernández]]></surname>
<given-names><![CDATA[Yezica J.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Valenzuela García]]></surname>
<given-names><![CDATA[Jesús L.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Santos Munguía]]></surname>
<given-names><![CDATA[P.C.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad Estatal de Sonora  ]]></institution>
<addr-line><![CDATA[Hermosillo Sonora]]></addr-line>
<country>Mexico</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad de Sonora Departamento de Ingeniería Química y Metalurgia ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Mexico</country>
</aff>
<aff id="Af3">
<institution><![CDATA[,Universidad Estatal de Sonora  ]]></institution>
<addr-line><![CDATA[Hermosillo Sonora]]></addr-line>
<country>Mexico</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2022</year>
</pub-date>
<volume>16</volume>
<numero>32</numero>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S2007-81962022000100002&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S2007-81962022000100002&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S2007-81962022000100002&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen La recuperación del ion de Litio se ha vuelto una búsqueda constante debido al incremento de demanda de baterías recargables. El objetivo de este trabajo fue evaluar los extractantes; Cyanex 272 y Cyanex 936P para determinar el extractante con mayor afinidad al ion Li. Se analizó la eficiencia de extracción de ambos extractantes utilizando licores de lixiviación sintéticas que contenían Li, K y Al, donde se evaluó el pH y el porcentaje de concentración del extractante, donde resulto que al 10% de extractante Cyanex 936P al estar en contacto con una solución acusa a un pH de 2, obtuvo el 44 % de extracción del ion Li, a comparación del extractante Cyanex 272 donde a las mismas condiciones, este obtuvo el 1.93% de extracción del ion Li.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract Lithium-ion recovery has become a constant quest due to the increasing demand for rechargeable batteries. The objective of this work was to evaluate the extractants; Cyanex 272 and Cyanex 936P to determine the extractant with the highest affinity to the Li-ion. The extraction efficiency of both extractants was analyzed using synthetic leaching liquors that contained Li, K, and Al, where the pH and the percentage of concentration of the extractant were evaluated, where it turned out that 10% of Cyanex 936P extractant when in contact with A solution with a pH of 2, obtained 44% extraction of the Li-ion, a comparison of the extractant Cyanex 272 where the same conditions, this obtained 1.93% extraction of the Li-ion.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[Litio]]></kwd>
<kwd lng="es"><![CDATA[Cyanex 272]]></kwd>
<kwd lng="es"><![CDATA[Cyanex 936P]]></kwd>
<kwd lng="es"><![CDATA[extracción por solventes]]></kwd>
<kwd lng="en"><![CDATA[Lithium]]></kwd>
<kwd lng="en"><![CDATA[Cyanex 272]]></kwd>
<kwd lng="en"><![CDATA[Cyanex 936P]]></kwd>
<kwd lng="en"><![CDATA[solvent extraction]]></kwd>
</kwd-group>
</article-meta>
</front><back>
<ref-list>
<ref id="B1">
<label>[1]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Yang]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Liu]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Wang]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Cui]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Chen]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Recovery of lithium from alkaline brine by solvent extraction with functionalized ionic liquid]]></article-title>
<source><![CDATA[Fluid Phase Equilibria]]></source>
<year>2019</year>
<volume>493</volume>
<page-range>129-36</page-range></nlm-citation>
</ref>
<ref id="B2">
<label>[2]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zhao]]></surname>
<given-names><![CDATA[J. M.]]></given-names>
</name>
<name>
<surname><![CDATA[Shen]]></surname>
<given-names><![CDATA[X. Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Deng]]></surname>
<given-names><![CDATA[F. L.]]></given-names>
</name>
<name>
<surname><![CDATA[Wang]]></surname>
<given-names><![CDATA[F. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Wu]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Liu]]></surname>
<given-names><![CDATA[H. Z.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Synergistic extraction and separation of valuable metals from waste cathodic material of llithium-ion batteries using CYANEX272 and PC-88a]]></article-title>
<source><![CDATA[Separation and purification technology]]></source>
<year>2011</year>
<volume>78</volume>
<numero>3</numero>
<issue>3</issue>
<page-range>345-51</page-range></nlm-citation>
</ref>
<ref id="B3">
<label>[3]</label><nlm-citation citation-type="">
<collab>Ministerio de Energía y Minería de Argentina</collab>
<source><![CDATA[El litio argentino. Situación actual y perspectivas]]></source>
<year>2017</year>
</nlm-citation>
</ref>
<ref id="B4">
<label>[4]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[El-Eswed]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Sunjuk]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Al-Degs]]></surname>
<given-names><![CDATA[Y. S.]]></given-names>
</name>
<name>
<surname><![CDATA[Shtaiwi]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Solvent Extraction of Li+ using Organophosphorus Ligands in the Presence of Ammonia]]></article-title>
<source><![CDATA[Separation Science and Technology]]></source>
<year>2014</year>
<volume>49</volume>
<numero>9</numero>
<issue>9</issue>
<page-range>1342-8</page-range></nlm-citation>
</ref>
<ref id="B5">
<label>[5]</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ritcey]]></surname>
<given-names><![CDATA[G.M.]]></given-names>
</name>
<name>
<surname><![CDATA[Ashbrook]]></surname>
<given-names><![CDATA[A.W.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Cap. 2 Y 3]]></article-title>
<source><![CDATA[Solvent Extraction in Process Metallurgy]]></source>
<year>1984</year>
<publisher-name><![CDATA[Elsevier]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B6">
<label>[6]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Meshram]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Pandey]]></surname>
<given-names><![CDATA[B. D.]]></given-names>
</name>
<name>
<surname><![CDATA[Mankhand]]></surname>
<given-names><![CDATA[T. R.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Extraction of lithium from primary and secondary sources by pre-treatment, leaching and separation: a comprehensive review]]></article-title>
<source><![CDATA[Hydrometallurgy]]></source>
<year>2014</year>
<volume>150</volume>
<page-range>192-208</page-range></nlm-citation>
</ref>
<ref id="B7">
<label>[7]</label><nlm-citation citation-type="">
<collab>Solvey</collab>
<source><![CDATA[Cyanex 272]]></source>
<year>2021</year>
</nlm-citation>
</ref>
<ref id="B8">
<label>[8]</label><nlm-citation citation-type="">
<collab>Solvey</collab>
<source><![CDATA[Cyanex 936P]]></source>
<year>2021</year>
</nlm-citation>
</ref>
</ref-list>
</back>
</article>
