<?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>S1665-27382014000300009</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Effect of initial substrate/inoculum ratio on cell yield in the removal of hydrophobic vocs in fungal biofilters]]></article-title>
<article-title xml:lang="es"><![CDATA[Efecto de la razón sustrato/inóculo sobre el rendimiento celular en la remoción de covs hidrofóbicos en biofiltros fúngicos]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vergara-Fernández]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[San Martín-Davison]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<xref ref-type="aff" rid="A03"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Díaz-Robles]]></surname>
<given-names><![CDATA[L.A.]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Soto-Sánchez]]></surname>
<given-names><![CDATA[O.]]></given-names>
</name>
<xref ref-type="aff" rid="A03"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universidad de Los Andes Facultad de Ingeniería y Ciencias Aplicadas ]]></institution>
<addr-line><![CDATA[Santiago de Chile ]]></addr-line>
<country>Chile</country>
</aff>
<aff id="A02">
<institution><![CDATA[,Universidad de Santiago de Chile Facultad de Ingeniería Departamento de Ingeniería Química]]></institution>
<addr-line><![CDATA[Santiago de Chile ]]></addr-line>
<country>Chile</country>
</aff>
<aff id="A03">
<institution><![CDATA[,Universidad Católica de Temuco Facultad de Ingeniería Escuela de Ingeniería Ambiental]]></institution>
<addr-line><![CDATA[Temuco Cautín]]></addr-line>
<country>Chile</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2014</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2014</year>
</pub-date>
<volume>13</volume>
<numero>3</numero>
<fpage>749</fpage>
<lpage>755</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382014000300009&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382014000300009&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382014000300009&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Different kinetic models have been proposed to describe the elimination of hydrophobic volatile organic compounds (VOCs) by fungal biofiltration. In this process the ratio of the initial substrate concentration (Cp b0) to the initial biomass (X0) has been shown to influence the cell yield. This papers presents a study of the efect of the Cp b0/X0 ratio on observed cell yield (Yobs) in a fixed bed batch system (microcosm) using a gaseous carbon source, as an approximation to its application in the fungal biofiltration of hydrophobic VOCs. Essays were carried out in fixed-bed microcosms using the filamentous fungus Fusarium solani as a biological agent and n-pentane as a carbon and energy source. The results indicated that Yobs in the gas phase is inversely proportional to the Cp b0/X0 ratio, with values of 0.9 to 0.35 g biomass g-1pentane being obtained when the Cp b0/X0 ratio is changed from 0.1 to 1.0 g pentane g-1biomass. The results indicate that more than 60% of n-pentane was consumed due to energy spilling, and that strong dissociation of catabolism from anabolism occurred at higher Cb0/X0 ratios.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[Diferentes modelos cinéticos han sido propuestos para describir la eliminación de compuestos orgánicos volátiles hidrofóbicos (COVs) en biofiltros fúngicos. En este proceso la razón de la concentración inicial de sustrato (Cp b0) a la biomasa inicial (X0) ha mostrado influir en el rendimiento celular. Este artículo presenta el estudio del efecto de la razón Cp b0/X0 en el rendimiento celular observado (Yobs) en un sistema por lote de lecho fijo (microcosmo) utilizando una fuente de carbono gaseosa, como una aproximación a su aplicación en la biofiltración fúngica de COVs hidrofóbicos. Los ensayos fueron realizados en microcosmos de lecho fijo utilizando el hongo filamentoso Fusarium solani como agente biológico y n-pentano como fuente de carbono y energía. Los resultados indican que Yobs en la fase gaseosa es inversamente proporcional a la razón Cp b0/X0, con valores de 0.9 a 0.35 g biomasa g-1pentano siendo obtenido cuando la razón Cp b0/X0 es cambiada desde 0.1 a 1.0 g pentano g-1biomasa. Los resultados indican que más del 60% del n-pentano fue consumido debido a pérdida de energía, y que una fuerte disociación del catabolismo y anabolismo ocurre para altas razones Cp b0/X0.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[hydrophobic VOCs]]></kwd>
<kwd lng="en"><![CDATA[fungal biofiltration]]></kwd>
<kwd lng="en"><![CDATA[substrate/inoculum ratio]]></kwd>
<kwd lng="en"><![CDATA[growth yield]]></kwd>
<kwd lng="es"><![CDATA[COVs hidrofóbicos]]></kwd>
<kwd lng="es"><![CDATA[biofiltración fúngica]]></kwd>
<kwd lng="es"><![CDATA[razón sustrato/inoculo]]></kwd>
<kwd lng="es"><![CDATA[rendimiento de crecimiento]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[  	    <p align="justify"><font face="verdana" size="4">Biotecnolog&iacute;a</font></p> 	    <p align="center"><font face="verdana" size="4">&nbsp;</font></p> 	    <p align="center"><font face="verdana" size="4"><b>Effect of initial substrate/inoculum ratio on cell yield in the removal of hydrophobic vocs in fungal biofilters</b></font></p>     <p align="center"><font face="verdana" size="4">&nbsp;</font></p> 	    <p align="center"><font face="verdana" size="3"><b>Efecto de la raz&oacute;n sustrato/in&oacute;culo sobre el rendimiento celular en la remoci&oacute;n de covs hidrof&oacute;bicos en biofiltros f&uacute;ngicos</b></font></p>     <p align="center"><font face="verdana" size="3">&nbsp;</font></p> 	    <p align="center"><font face="verdana" size="2"><b>A. Vergara&#45;Fern&aacute;ndez<sup>1</sup>*, J. San Mart&iacute;n&#45;Davison<sup>3</sup>, L.A. D&iacute;az&#45;Robles<sup>2</sup>, O. Soto&#45;S&aacute;nchez<sup>3</sup></b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p> 	    <p align="justify"><font face="verdana" size="2"><sup><i>1</i></sup> <i>Facultad de Ingenier&iacute;a y Ciencias Aplicadas, Universidad de los Andes, Mons. &Aacute;lvaro del Portillo 12455, Las Condes. Santiago, 7620001 Chile * Corresponding author. E&#45;mail:</i> <a href="mailto:aovergara@miuandes.cl">aovergara@miuandes.cl</a> <i>telephone/fax: 56&#45;02&#45;2618 1000.</i></font></p> 	    ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><i> <sup>2</sup> Departamento de Ingenier&iacute;a Qu&iacute;mica, Facultad de Ingenier&iacute;a, Universidad de Santiago de Chile.</i></font></p> 	    <p align="justify"><font face="verdana" size="2"> <sup>3</sup><i> Escuela de Ingenier&iacute;a Ambiental, Facultad de Ingenier&iacute;a, Universidad Cat&oacute;lica de Temuco.</i></font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>      <p align="justify"><font face="verdana" size="2">Received September 30, 2013.     <br> Accepted June 19, 2014.</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">Different kinetic models have been proposed to describe the elimination of hydrophobic volatile organic compounds (VOCs) by fungal biofiltration. In this process the ratio of the initial substrate concentration (C<i><sup>p</sup><sub>b0</sub></i>) to the initial biomass (<i>X</i><sub>0</sub>) has been shown to influence the cell yield. This  papers presents a study of the efect of the C<i><sup>p</sup><sub>b0</sub></i>/<i>X</i><sub>0</sub> ratio on observed cell yield <i>(Y<sub>obs</sub></i>) in a fixed bed batch system (microcosm) using a gaseous carbon source, as an approximation to its application in the fungal biofiltration of hydrophobic VOCs. Essays were carried out in fixed&#45;bed microcosms using the filamentous fungus <i>Fusarium solani</i> as a biological agent and <i>n</i>&#45;pentane as a carbon and energy source. The results indicated that <i>Y<sub>obs</sub></i> in the gas phase is inversely proportional to the C<i><sup>p</sup><sub>b0</sub></i>/<i>X</i><sub>0</sub> ratio, with values of 0.9 to 0.35 <i>g<sub>biomass</sub> g<sup>&#45;1</sup><sub>pentane</sub></i> being obtained when the C<i><sup>p</sup><sub>b0</sub></i>/<i>X</i><sub>0</sub> ratio is changed from 0.1 to 1.0<i> g<sub>pentane</sub> g<sup>&#45;1</sup><sub>biomass</sub>.</i> The results indicate that more than 60% of n&#45;pentane was consumed due to energy spilling, and that strong dissociation of catabolism from anabolism occurred at higher C<i><sub>b0</sub></i>/<i>X</i><sub>0</sub> ratios<i>.</i></font></p>  	    <p align="justify"><font face="verdana" size="2"><b>Keywords:</b> hydrophobic VOCs, fungal biofiltration, substrate/inoculum ratio, growth yield.</font></p>          <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>      ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><b>Resumen</b></font></p>  	    <p align="justify"><font face="verdana" size="2">Diferentes modelos cin&eacute;ticos han sido propuestos para describir la eliminaci&oacute;n de compuestos org&aacute;nicos vol&aacute;tiles hidrof&oacute;bicos (COVs) en biofiltros f&uacute;ngicos. En <i>este</i> proceso la raz&oacute;n de la concentraci&oacute;n inicial de sustrato (C<i><sup>p</sup><sub>b0</sub></i>) a la biomasa inicial (<i>X</i><sub>0</sub>) ha mostrado influir en el rendimiento celular. Este art&iacute;culo presenta el estudio del efecto de la raz&oacute;n C<i><sup>p</sup><sub>b0</sub></i>/<i>X</i><sub>0</sub><sub></sub> en el rendimiento celular observado (Y<sub>obs</sub>) en un sistema por lote de lecho fijo (microcosmo) utilizando una fuente de carbono gaseosa, como una aproximaci&oacute;n a su aplicaci&oacute;n en la biofiltraci&oacute;n f&uacute;ngica de COVs hidrof&oacute;bicos. Los ensayos fueron realizados en microcosmos de lecho fijo utilizando el hongo filamentoso <i>Fusarium solani</i> como agente biol&oacute;gico y <i>n</i>&#45;pentano como fuente de carbono y energ&iacute;a. Los resultados indican que <i>Y<sub>obs</sub></i> en la fase gaseosa es inversamente proporcional a la raz&oacute;n C<i><sup>p</sup><sub>b0</sub></i>/<i>X</i><sub>0</sub><i>,</i> con valores de 0.9 a 0.35<i> g<sub>biomasa</sub> g<sup>&#45;1</sup><sub>pentano </sub></i>siendo obtenido cuando la raz&oacute;n C<i><sup>p</sup><sub>b0</sub></i>/<i>X</i><sub>0</sub> es cambiada desde 0.1 a 1.0 <i>g<sub>pentano</sub> g<sup>&#45;1</sup><sub>biomasa</sub>.</i> Los resultados indican que m&aacute;s del 60% del <i>n</i>&#45;pentano fue consumido debido a p&eacute;rdida de energ&iacute;a, y que una fuerte disociaci&oacute;n del catabolismo y anabolismo ocurre para altas razones C<i><sup>p</sup><sub>b0</sub></i>/<i>X</i><sub>0</sub><i>.</i></font></p>      <p align="justify"><font face="verdana" size="2"><b>Palabras clave:</b> COVs hidrof&oacute;bicos, biofiltraci&oacute;n f&uacute;ngica, raz&oacute;n sustrato/inoculo, rendimiento de crecimiento.</font></p>      <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="justify"><font face="verdana" size="2"><a href="/pdf/rmiq/v13n3/v13n3a9.pdf" target="_blank">DESCARGAR ART&Iacute;CULO EN FORMATO PDF</a></font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>      <p align="justify"><font face="verdana" size="2"><b>Acknowledgements</b></font></p>  	    <p align="justify"><font face="verdana" size="2">The present research was financed by the CONICYT (National Commission for Scientific and Technological Research) (FONDECYT Project N&deg;11080036).</font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><b>References</b></font></p>  	    ]]></body>
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