<?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>S1665-27382009000100010</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Efecto de las cargas hidráulica y orgánica sobre la remoción masica de un empaque estructurado en un filtro percolador]]></article-title>
<article-title xml:lang="en"><![CDATA[Effect of hydraulic and organic loads on the mass removal of a structured packing in a trickling filter]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Reyes-Lara]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Reyes-Mazzoco]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universidad de las Américas Departamento de Ingeniería Química y de Alimentos ]]></institution>
<addr-line><![CDATA[ Puebla]]></addr-line>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>04</month>
<year>2009</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>04</month>
<year>2009</year>
</pub-date>
<volume>8</volume>
<numero>1</numero>
<fpage>101</fpage>
<lpage>109</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382009000100010&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382009000100010&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382009000100010&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Se realizó un estudio a escala de banco del comportamiento de un nuevo empaque plástico estructurado para un filtro percolador que se diseñó siguiendo el modelo del módulo de Thiele para aumentar su eficiencia de remoción de contaminantes presentes en el agua. Para determinar la remoción másica de DQO del sistema operando en estado estable se aplicaron distintas cargas orgánicas, (L, kg DQO/m³s), e hidráulicas, (Q, m³/m² d), de acuerdo a un diseño factorial de experimentos y dos tipos de agua residual. Se probaron valores de L entre 5 y 72 kg DQO/m³ d, más de diez veces mayores a los normalmente utilizados en filtros percoladores para depuración de aguas sanitarias, para demostrar que el diseño del empaque es capaz de manejarlos. La remoción másica se obtuvo entre 3 y 10 kg DQO/m³ d sin limitación en la transferencia de oxígeno. Usando el modelo cinético propuesto por Eckenfelder basado en L y en el área específica del empaque, la depuración del agua residual sintética produjo un valor de la constante cinética de 0.0423 kg DQO/m² d y el agua residual preparada con suero de leche de 0.0867 kg DQO/m² d.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[A bench scale study was performed on the behavior of a new structured packing for a trickling filter designed from the model of Thiele's modulus for increasing the removal efficiency of pollutants present in wastewater. For determining the mass removal of COD from the system working at steady state, several organic, (L, kg DQO/m³s), and hydraulic loads, (Q, m³/m² d), were applied according to a factorial experimental design and two types of wastewater. L values were tested in the range of 5 to 72 kg DQO/m³ d, more than ten times higher than values used in sanitary wastewater treatment, to demonstrate that the packing's design is able to handle them. Mass removal was obtained from 3 to 10 kg DQO/m³ d with no limitation of oxygen transfer. Using the kinetic model proposed by Eckenfelder based on L and the specific area of the packing, the treatment of synthetic wastewater produced a value of the kinetic constant of 0.0423 kg DQO/m² d and for the wastewater prepared from whey was 0.0867 kg DQO/m² d.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[filtro percolador]]></kwd>
<kwd lng="es"><![CDATA[carga orgánica]]></kwd>
<kwd lng="es"><![CDATA[carga hidráulica]]></kwd>
<kwd lng="es"><![CDATA[empaque estructurado]]></kwd>
<kwd lng="en"><![CDATA[trickling filter]]></kwd>
<kwd lng="en"><![CDATA[organic load]]></kwd>
<kwd lng="en"><![CDATA[hydraulic load]]></kwd>
<kwd lng="en"><![CDATA[structured packing]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="justify"><font face="verdana" size="4">Ingenier&iacute;a ambiental</font></p>     <p align="justify"><font face="verdana" size="4">&nbsp;</font></p>     <p align="center"><font face="verdana" size="4"><strong>Efecto de las cargas hidr&aacute;ulica y org&aacute;nica sobre la remoci&oacute;n masica de un empaque estructurado en un filtro percolador</strong></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="3"><strong>Effect of hydraulic and organic loads on the mass removal of a structured packing in a trickling filter</strong></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="2"><strong>S. Reyes&#150;Lara y R. Reyes&#150;Mazzoco*</strong></font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><i>Departamento de Ingenier&iacute;a Qu&iacute;mica y de Alimentos, Universidad de las Am&eacute;ricas, Puebla.</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 27 de Octubre 2008    <br> Aceptado 17 de Febrero 2009</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">Se realiz&oacute; un estudio a escala de banco del comportamiento de un nuevo empaque pl&aacute;stico estructurado para un filtro percolador que se dise&ntilde;&oacute; siguiendo el modelo del m&oacute;dulo de Thiele para aumentar su eficiencia de remoci&oacute;n de contaminantes presentes en el agua. Para determinar la remoci&oacute;n m&aacute;sica de DQO del sistema operando en estado estable se aplicaron distintas cargas org&aacute;nicas, (L, kg DQO/m<sup>3</sup>s), e hidr&aacute;ulicas, (Q, m<sup>3</sup>/m<sup>2</sup> d), de acuerdo a un dise&ntilde;o factorial de experimentos y dos tipos de agua residual. Se probaron valores de L entre 5 y 72 kg DQO/m<sup>3 </sup>d, m&aacute;s de diez veces mayores a los normalmente utilizados en filtros percoladores para depuraci&oacute;n de aguas sanitarias, para demostrar que el dise&ntilde;o del empaque es capaz de manejarlos. La remoci&oacute;n m&aacute;sica se obtuvo entre 3 y 10 kg DQO/m<sup>3</sup> d sin limitaci&oacute;n en la transferencia de ox&iacute;geno. Usando el modelo cin&eacute;tico propuesto por Eckenfelder basado en L y en el &aacute;rea espec&iacute;fica del empaque, la depuraci&oacute;n del agua residual sint&eacute;tica produjo un valor de la constante cin&eacute;tica de 0.0423 kg DQO/m<sup>2</sup> d y el agua residual preparada con suero de leche de 0.0867 kg DQO/m<sup>2</sup> d.</font></p>     <p align="justify"><font face="verdana" size="2"><strong>Palabras clave: </strong>filtro percolador, carga org&aacute;nica, carga hidr&aacute;ulica, empaque estructurado.</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">A bench scale study was performed on the behavior of a new structured packing for a trickling filter designed from the model of Thiele's modulus for increasing the removal efficiency of pollutants present in wastewater. For determining the mass removal of COD from the system working at steady state, several organic, (L, kg DQO/m<sup>3</sup>s), and hydraulic loads, (Q, m<sup>3</sup>/m<sup>2</sup> d), were applied according to a factorial experimental design and two types of wastewater. L values were tested in the range of 5 to 72 kg DQO/m<sup>3</sup> d, more than ten times higher than values used in sanitary wastewater treatment, to demonstrate that the packing's design is able to handle them. Mass removal was obtained from 3 to 10 kg DQO/m<sup>3</sup> d with no limitation of oxygen transfer. Using the kinetic model proposed by Eckenfelder based on L and the specific area of the packing, the treatment of synthetic wastewater produced a value of the kinetic constant of 0.0423 kg DQO/m<sup>2</sup> d and for the wastewater prepared from whey was 0.0867 kg DQO/m<sup>2</sup> d.</font></p>     <p align="justify"><font face="verdana" size="2"><strong>Keywords: </strong>trickling filter, organic load, hydraulic load, structured packing.</font></p>     ]]></body>
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