<?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>1665-2738</journal-id>
<journal-title><![CDATA[Revista mexicana de ingeniería química]]></journal-title>
<abbrev-journal-title><![CDATA[Rev. Mex. Ing. Quím]]></abbrev-journal-title>
<issn>1665-2738</issn>
<publisher>
<publisher-name><![CDATA[Universidad Autónoma Metropolitana, División de Ciencias Básicas e Ingeniería]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1665-27382015000300015</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Evaluación de coeficientes volumétricos de transferencia de hidrocarburos poliaromáticos y oxígeno en sistemas multifásicos (líquido-líquido y líquido-líquido-gas): efecto de la carga volumétrica de solventes biocompatibles]]></article-title>
<article-title xml:lang="en"><![CDATA[Evaluation of polyaromatic hydrocarbon and oxygen volumetric transfer coefficient on multi-phase system (liquid-liquid and liquid-liquid-gas): biocompatible solvent charge effect]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Jiménez-González]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vargas-García]]></surname>
<given-names><![CDATA[V.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Lizardi-Jiménez]]></surname>
<given-names><![CDATA[M.A]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Medina-Moreno]]></surname>
<given-names><![CDATA[S.A.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universidad Politécnica de Pachuca  ]]></institution>
<addr-line><![CDATA[Zempoala Hidalgo]]></addr-line>
<country>México</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>12</month>
<year>2015</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>12</month>
<year>2015</year>
</pub-date>
<volume>14</volume>
<numero>3</numero>
<fpage>723</fpage>
<lpage>734</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382015000300015&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382015000300015&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382015000300015&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[En el presente trabajo, se determinaron en un sistema de tanque agitado con las fases inmiscibles aceite de silicón y heptametilnonano, los coeficientes volumétricos de transferencia de masa (K LaH) de naftaleno y fenantreno (sistema líquido-líquido). Los valores de K LaH se correlacionaron con el número de Reynolds (N Re) y se observó que en el sistema de agitación utilizado, el K LaH es independiente de la hidrodinámica del sistema para N Re &#8805; 17,000. Los K LaH alcanzados fueron de 52 y 44 h-1 para naftaleno y de 69 y 62 h-1 para fenantreno, con aceite de silicón y heptametilnonano respectivamente. También, se evaluó el efecto de la carga volumétrica de las fases inmiscibles en el coeficiente volumétrico de transferencia de oxígeno (K La) para el mismo sistema de tanque agitado con aireación (sistema líquido-líquido-gas). La adición de cada solvente, condujo a una fuerte disminución en el K La, incrementándose este efecto con el aumento de la carga volumétrica de los solventes. El K La decreció de un máximo de 49 h-1 en un medio sin solvente, hasta mínimos de 22 h-1 con aceite de silicón y 7 h-1 con heptametilnonano, teniéndose en ambos casos una carga volumétrica del 5%. La disminución en el K La, se asoció a un efecto negativo de las viscosidades dinámica y cinemática de los solventes sobre: la difusividad del oxígeno, el espesor de la capa límite y el área específica interfacial de las burbujas de aire.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[In this work were determined in a stirred tank system with the phases non-miscible silicon oil and heptamethylnonane, the mass transfer volumetric coefficient (K LaH) of naphthalene and phenanthrene (liquid-liquid system). The K LaH values were correlated with the Reynolds number, observing that K LaH let of be a function of the Reynols for values N Re &#8805; 17,000. The values reached of K LaH were 52 and 44 h-1 for naphthalene and 69 and 62 h-1 for phenanthrene both with silicon oil and heptamethylnonane respectively. Also was evaluated the volumetric charge effect of the non-miscible solvents, in the volumetric oxygen transfer coefficient (K La) for the same stirred tank system with aeration (liquid-liquid-gas system). The addition of each one of the solvents led to strong decrease of the K La, being more marked the effect with the increase in the volumetric charge of the solvents. The K La in the aqueous medium without solvent decreased of a maximum of 49 h-1 up to minimums of 22 h-1 with oil silicon and 7 h-1 with heptamethylnonane, in both cases with a volumetric charge of 5% of each solvent. The decrease in the K La was probably due to a negative effect of the dynamic and kinematic viscosities of both solvents over: the oxygen diffusivity, thickness of the boundary layer and the specific interfacial area of the bubbles air.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[naftaleno]]></kwd>
<kwd lng="es"><![CDATA[fenantreno]]></kwd>
<kwd lng="es"><![CDATA[coeficientes volumétricos de transferencia de masa]]></kwd>
<kwd lng="es"><![CDATA[aceite de silicón]]></kwd>
<kwd lng="es"><![CDATA[heptametilnonano]]></kwd>
<kwd lng="en"><![CDATA[naphthalene]]></kwd>
<kwd lng="en"><![CDATA[phenanthrene]]></kwd>
<kwd lng="en"><![CDATA[volumetric mass transfer coefficients]]></kwd>
<kwd lng="en"><![CDATA[silicone oil]]></kwd>
<kwd lng="en"><![CDATA[heptamethylnonane]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="justify"><font face="verdana" size="4">Fen&oacute;menos de transporte</font></p>        <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>        <p align="center"><font face="verdana" size="4"><b>Evaluaci&oacute;n de coeficientes volum&eacute;tricos de transferencia de hidrocarburos poliarom&aacute;ticos y ox&iacute;geno en sistemas multif&aacute;sicos (l&iacute;quido&#45;l&iacute;quido y l&iacute;quido&#45;l&iacute;quido&#45;gas): efecto de la carga volum&eacute;trica de solventes biocompatibles</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>        <p align="center"><font face="verdana" size="3"><b>Evaluation of polyaromatic hydrocarbon and oxygen volumetric transfer coefficient on multi&#45;phase system (liquid&#45;liquid and liquid&#45;liquid&#45;gas): biocompatible solvent charge effect</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>        <p align="center"><font face="verdana" size="2"><b>A. Jim&eacute;nez&#45;Gonz&aacute;lez, V. Vargas&#45;Garc&iacute;a, M.A Lizardi&#45;Jim&eacute;nez*, S.A. Medina&#45;Moreno</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>        <p align="justify"><font face="verdana" size="2"><i>Universidad Polit&eacute;cnica de Pachuca, Carretera Pachuca&#45;Cd. Sahag&uacute;n, km 20, Ex&#45;Hacienda de Santa B&aacute;rbara, Municipio de Zempoala Hidalgo. * Autor para la correspondencia. </i>E&#45;mail: <a href=   "mailto:chamarripas@yahoo.com.mx">chamarripas@yahoo.com.mx</a><i>.</i></font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>       ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2">Recibido 20 de mayo, 2015;     <br>  Aceptado 20 de octubre, 2015.</font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>      <p align="justify"><font face="verdana" size="2"><b>Resumen</b></font></p>        <p align="justify"><font face="verdana" size="2">En el presente trabajo, se determinaron en un   sistema de tanque agitado con las fases inmiscibles aceite de   silic&oacute;n y heptametilnonano, los coeficientes volum&eacute;tricos de   transferencia de masa (K<i><sub>L</sub>a<sub>H</sub></i>) de naftaleno y fenantreno (sistema   l&iacute;quido&#45;l&iacute;quido). Los valores de <i>K<sub>L</sub>a<sub>H</sub><sub></sub></i> se correlacionaron con el n&uacute;mero de Reynolds   (N<sub><i>Re</i></sub>) y se observ&oacute; que en el sistema de agitaci&oacute;n   utilizado, el <i>K<sub>L</sub>a<sub>H</sub><sub></sub></i> es independiente   de la hidrodin&aacute;mica del sistema para <i>N<sub>Re</sub></i> &#8805;   17,000. Los <i>K<sub>L</sub>a<sub>H</sub><sub></sub></i> alcanzados fueron de   52 y 44 h<sup>&#45;1</sup> para naftaleno y de 69 y 62 h<sup>&#45;1</sup>   para fenantreno, con aceite de silic&oacute;n y heptametilnonano   respectivamente. Tambi&eacute;n, se evalu&oacute; el efecto de la carga   volum&eacute;trica de las fases inmiscibles en el coeficiente   volum&eacute;trico de transferencia de ox&iacute;geno (<i>K<sub>L</sub>a<sub></sub></i>) para el   mismo sistema de tanque agitado con aireaci&oacute;n (sistema   l&iacute;quido&#45;l&iacute;quido&#45;gas). La adici&oacute;n de cada solvente,   condujo a una fuerte disminuci&oacute;n en el <i>K<sub>L</sub>a<sub></sub></i>, increment&aacute;ndose este   efecto con el aumento de la carga volum&eacute;trica de los solventes.   El<i> K<sub>L</sub>a<sub></sub></i> decreci&oacute; de un m&aacute;ximo de 49 h<sup>&#45;1</sup>   en un medio sin solvente, hasta m&iacute;nimos de 22   h<sup>&#45;1</sup> con aceite de silic&oacute;n y 7 h<sup>&#45;1</sup> con   heptametilnonano, teni&eacute;ndose en ambos casos una carga volum&eacute;trica   del 5%. La disminuci&oacute;n en el <i>K<sub>L</sub>a<sub></sub></i>, se asoci&oacute; a un efecto   negativo de <i>las</i> viscosidades din&aacute;mica y cinem&aacute;tica   de los solventes sobre: la difusividad del ox&iacute;geno, el   espesor de la capa l&iacute;mite y el &aacute;rea espec&iacute;fica interfacial de las burbujas de aire.</font></p>       <p align="justify"><font face="verdana" size="2"><b>Palabras clave:</b>   naftaleno, fenantreno, coeficientes volum&eacute;tricos de transferencia   de masa, aceite de silic&oacute;n, heptametilnonano.</font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>      <p align="justify"><font face="verdana" size="2"><b>Abstract</b></font></p>        <p align="justify"><font face="verdana" size="2">In this work were determined in a stirred tank   system with the phases non&#45;miscible silicon oil and   heptamethylnonane, the mass transfer volumetric coefficient   <i>(K<sub>L</sub>a<sub>H</sub><sub></sub></i>) of naphthalene and   phenanthrene (liquid&#45;liquid system). The K<i><sub>L</sub>a<sub>H</sub></i> values were correlated with the   Reynolds number, observing that <i>K<sub>L</sub>a<sub>H</sub></i> let of be a function of the Reynols for values <i>N<sub>Re</sub></i> &#8805; 17,000. The values reached of<i> K<sub>L</sub>a<sub>H</sub><sub></sub></i> were 52 and 44 h<sup>&#45;1</sup>   for naphthalene and 69 and 62 h<sup>&#45;1</sup> for phenanthrene   both with silicon oil and heptamethylnonane respectively. Also   was evaluated the volumetric charge effect of the non&#45;miscible   solvents, in the volumetric oxygen transfer coefficient   <i>(K<sub>L</sub>a)</i> for the same stirred tank system with   aeration (liquid&#45;liquid&#45;gas system). The addition of each one of   the solvents led to strong decrease of the <i>K<sub>L</sub>a,</i> being more marked the effect with the   increase in the volumetric charge of the solvents. The   <i>K<sub>L</sub>a</i> in the aqueous medium without solvent   decreased of a maximum of 49 h<sup>&#45;1</sup> up to minimums of 22   h<sup>&#45;1</sup> with oil silicon and 7 h<sup>&#45;1</sup> with   heptamethylnonane, in both cases with a volumetric charge of 5%   of each solvent. The decrease in the<i> K<sub>L</sub>a</i> was   probably due to a negative effect of the dynamic and kinematic   viscosities of both solvents over: the oxygen diffusivity,   thickness of the boundary layer and the specific interfacial area of the bubbles air. </font></p>        <p align="justify"><font face="verdana" size="2"><b>Keywords:</b> naphthalene, phenanthrene,   volumetric mass transfer coefficients, silicone oil, heptamethylnonane. </font></p>        ]]></body>
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