<?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>1870-249X</journal-id>
<journal-title><![CDATA[Journal of the Mexican Chemical Society]]></journal-title>
<abbrev-journal-title><![CDATA[J. Mex. Chem. Soc]]></abbrev-journal-title>
<issn>1870-249X</issn>
<publisher>
<publisher-name><![CDATA[Sociedad Química de México A.C.]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1870-249X2006000300012</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Experiments and Modeling of the Cymbopogon winterianus Essential Oil Extraction by Steam Distillation]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Cassel]]></surname>
<given-names><![CDATA[Eduardo]]></given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vargas]]></surname>
<given-names><![CDATA[Rubem M. F.]]></given-names>
</name>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Pontificia Universidade Catolica do Rio Grande do Sul Engineering Faculty Laboratório de Operacões Unitárias]]></institution>
<addr-line><![CDATA[Porto Alegre Rio Grande do Sul]]></addr-line>
<country>Brasil</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>09</month>
<year>2006</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>09</month>
<year>2006</year>
</pub-date>
<volume>50</volume>
<numero>3</numero>
<fpage>126</fpage>
<lpage>129</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1870-249X2006000300012&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1870-249X2006000300012&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1870-249X2006000300012&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[This work has as objective to optimize and to model the yield of the citronella essential oil extraction processes from twigs and leaves by steam distillation. The process variables evaluated in this study were extraction time, and raw material state (dry or natural). The yield is calculated from the relation between the essential oil mass obtained and the raw material mass used in the extraction and the quantitative and qualitative analyses of the oils were performed by capillary GC/MS. The experimental condition for the maximum yield, 0.942%, is the following one: extraction time, 4 h, state, natural plant, and the results obtained from the factorial experimental planning indicate that the variable that more influences the essential oil yield is the state. The modeling of these results is proposed from the description of the mass transfer from a single plate particle. Yield curves for all studied conditions were fairly well fitted using one adjustable parameter of the model and the experimental monitoring of oil composition as function of extraction time was realized in laboratory steam distillation apparatus and compared with industrial scale results.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[Este trabajo tiene como objetivo optimizar y modelar el rendimiento del proceso de extracción del aceite esencial de citronela, obtenido por destilación por arrastre de vapor a partir de hojas y ramas. Las variables del proceso evaluadas en este estudio fueron el tiempo de extracción y el estado de la materia prima (seca o natural). El rendimiento de aceite esencial es calculado a partir de la relación entre la masa de aceite y la masa de planta aromática usada en la extracción. Los análisis cuantitativo y cualitativo de los aceites fueran determinados por GC/MS. Las condiciones experimentales para el rendimiento máximo, 0,942%, son las siguientes: tiempo de extracción, 4 h; estado, planta natural; y los resultados obtenidos a partir del estudio estadístico indicaron que la variable que más influencia el rendimiento de aceite esencial es el estado de la planta. El modelado propuesto para describir la transferencia de masa del proceso de extracción está centrado en una partícula en forma de placa plana. Las curvas de rendimiento, para todas las condiciones estudiadas, fueron ajustadas usando un modelo con un parámetro ajustable y los resultados del modelado obtenidos a partir de los datos en escala de laboratorio fueron comparables con las informaciones experimentales obtenidas en escala industrial.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[Citronella essential oil]]></kwd>
<kwd lng="en"><![CDATA[steam distillation]]></kwd>
<kwd lng="en"><![CDATA[mass transfer]]></kwd>
<kwd lng="en"><![CDATA[mathematical model]]></kwd>
<kwd lng="es"><![CDATA[citronela]]></kwd>
<kwd lng="es"><![CDATA[destilación por arrastre de vapor]]></kwd>
<kwd lng="es"><![CDATA[transferencia de masa]]></kwd>
<kwd lng="es"><![CDATA[modelado matemático]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[  	    <p align="justify"><font face="verdana" size="4">Article</font></p> 	    <p align="justify">&nbsp;</p> 	    <p align="center"><font face="verdana" size="4"><b>Experiments and Modeling of the <i>Cymbopogon winterianus</i> Essential Oil Extraction by Steam Distillation</b></font></p> 	    <p align="justify">&nbsp;</p> 	    <p align="center"><font face="verdana" size="2"><b>Eduardo Cassel,* Rubem M. F. Vargas</b></font></p> 	    <p align="justify">&nbsp;</p> 	    <p align="justify"><font face="verdana" size="2"><i>Laborat&oacute;rio de Operac&otilde;es Unit&aacute;rias, Engineering Faculty &#45; PUCRS, Av. Ipiranga 6681, CEP 90619&#45;900, Porto Alegre &#45; RS, Brazil, Telephone + (55)(51) 3320&#45;3653, Fax +(55)(51) 3320&#45;3625, E&#45;mail</i>: <a href="mailto:cassel@pucrs.br">cassel@pucrs.br</a></font></p> 	    <p align="justify">&nbsp;</p> 	    <p align="justify"><font face="verdana" size="2">Recibido el 31 de enero del 2005.     ]]></body>
<body><![CDATA[<br>     Aceptado el 5 de abril del 2006.</font></p>     <p align="justify">&nbsp;</p> 	    <p align="justify"><font face="verdana" size="2"><b>Abstract</b></font></p> 	    <p align="justify"><font face="verdana" size="2"> This work has as objective to optimize and to model the yield of the citronella essential oil extraction processes from twigs and leaves by steam distillation. The process variables evaluated in this study were extraction time, and raw material state (dry or natural). The yield is calculated from the relation between the essential oil mass obtained and the raw material mass used in the extraction and the quantitative and qualitative analyses of the oils were performed by capillary GC/MS. The experimental condition for the maximum yield, 0.942%, is the following one: extraction time, 4 h, state, natural plant, and the results obtained from the factorial experimental planning indicate that the variable that more influences the essential oil yield is the state. The modeling of these results is proposed from the description of the mass transfer from a single plate particle. Yield curves for all studied conditions were fairly well fitted using one adjustable parameter of the model and the experimental monitoring of oil composition as function of extraction time was realized in laboratory steam distillation apparatus and compared with industrial scale results.</font></p> 	    <p align="justify"><font face="verdana" size="2"><b>Keywords:</b> Citronella essential oil, steam distillation, mass transfer, mathematical model</font>.</p> 	    <p align="justify">&nbsp;</p> 	    <p align="justify"><font face="verdana" size="2"><b>Resumen</b></font></p> 	    <p align="justify"><font face="verdana" size="2"> Este trabajo tiene como objetivo optimizar y modelar el rendimiento del proceso de extracci&oacute;n del aceite esencial de citronela, obtenido por destilaci&oacute;n por arrastre de vapor a partir de hojas y ramas. Las variables del proceso evaluadas en este estudio fueron el tiempo de extracci&oacute;n y el estado de la materia prima (seca o natural). El rendimiento de aceite esencial es calculado a partir de la relaci&oacute;n entre la masa de aceite y la masa de planta arom&aacute;tica usada en la extracci&oacute;n. Los an&aacute;lisis cuantitativo y cualitativo de los aceites fueran determinados por GC/MS. Las condiciones experimentales para el rendimiento m&aacute;ximo, 0,942%, son las siguientes: tiempo de extracci&oacute;n, 4 h; estado, planta natural; y los resultados obtenidos a partir del estudio estad&iacute;stico indicaron que la variable que m&aacute;s influencia el rendimiento de aceite esencial es el estado de la planta. El modelado propuesto para describir la transferencia de masa del proceso de extracci&oacute;n est&aacute; centrado en una part&iacute;cula en forma de placa plana. Las curvas de rendimiento, para todas las condiciones estudiadas, fueron ajustadas usando un modelo con un par&aacute;metro ajustable y los resultados del modelado obtenidos a partir de los datos en escala de laboratorio fueron comparables con las informaciones experimentales obtenidas en escala industrial.</font></p> 	    <p align="justify"><font face="verdana" size="2"><b>Palabras claves:</b> citronela, destilaci&oacute;n por arrastre de vapor, transferencia de masa, modelado matem&aacute;tico. </font></p> 	    <p align="justify">&nbsp;</p> 	    ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><a href="/pdf/jmcs/v50n3/v50n3a12.pdf" target="_blank">DESCARGAR ARCHIVO EN FORMATO PDF</a></font></p> 	    <p align="justify">&nbsp;</p> 	    <p align="justify"><font face="verdana" size="2"><b>References</b></font></p> 	    <!-- ref --><p align="justify"><font face="verdana" size="2">1. Clay, D.V.; Dixon, F.L.; Willoughby, I. <i>Forestry</i> <b>2005,</b> <i>78,</i> 1&#45;9.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894761&pid=S1870-249X200600030001200001&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>     <!-- ref --><p align="justify"><font face="verdana" size="2">2. Spiro, M.; Selwood, R. M. <i>J. Sci. Food Agric.</i> <b>1984,</b> <i>35,</i> 915&#45;924.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894763&pid=S1870-249X200600030001200002&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">3. Spiro, M.; Page, C. <i>J. Sci. Food Agric.</i> <b>1984,</b> <i>35</i>, 925&#45;930.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894765&pid=S1870-249X200600030001200003&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">4. Spiro, M., Kandiah, M.; Price, W. <i>J. Food Sci. Tech.</i> <b>1990,</b> <i>25,</i> 157&#45;167.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894767&pid=S1870-249X200600030001200004&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">5. Reverchon, E. <i>J. Supercrit. Fluids</i> <b>1997,</b> <i>10,</i> 1&#45;37.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894769&pid=S1870-249X200600030001200005&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">6. Benyoussef, E. H.; Hasni, S.; Belabbes, R.; Bessiere, J. M. <i>Chem. Eng. J.</i> <b>2002,</b> <i>85</i>, 1&#45;5.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894771&pid=S1870-249X200600030001200006&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">7. Adams, R. P. <i>Identification of Essential Oil Components by Gas Chromatography/mass Spectrometry.</i> Allured: Illinois, <b>1995.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894773&pid=S1870-249X200600030001200007&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></b></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">8. Kreider, D.L., Kuller, R.G., Ostberg, D.R., Perkins, F.W. <i>An Introduction to Linear Analysis.</i> Addison&#45;Wesley Company Inc., Massachusetts, <b>1966.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894775&pid=S1870-249X200600030001200008&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></b></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">9. Nelder, J.; Mead, R. <i>Comput. J.</i> <b>1965,</b> <i>7</i>, 308, 1965.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4894777&pid=S1870-249X200600030001200009&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>      ]]></body><back>
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