<?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>S1665-27382013000200011</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Coffee grain rotary drying optimization]]></article-title>
<article-title xml:lang="es"><![CDATA[Optimización del secado de granos de café en un secador rotatorio]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Hernández-Díaz]]></surname>
<given-names><![CDATA[W.N.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Hernández-Campos]]></surname>
<given-names><![CDATA[F.J.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vargas-Galarza]]></surname>
<given-names><![CDATA[Z.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Rodríguez-Jimenes]]></surname>
<given-names><![CDATA[G.C.]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[García-Alvarado]]></surname>
<given-names><![CDATA[M.A.]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Instituto Tecnológico de Zacatepec Departamento de Ingeniería Química y Bioquímica ]]></institution>
<addr-line><![CDATA[ Morelos]]></addr-line>
<country>México</country>
</aff>
<aff id="A02">
<institution><![CDATA[,Instituto Tecnológico de Veracruz Unidad de Investigación y Desarrollo en Alimentos ]]></institution>
<addr-line><![CDATA[Veracruz Veracruz]]></addr-line>
<country>México</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2013</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2013</year>
</pub-date>
<volume>12</volume>
<numero>2</numero>
<fpage>315</fpage>
<lpage>325</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382013000200011&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382013000200011&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382013000200011&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[The objective of the present work was to determine the coffee bean Guardiola dryer operating conditions that minimized the energy consumption (Q) and maximized the process thermal efficiency. A mechanistic coffee bean drying model was solved for a complete mixed assumption to simulate the drying. The simulated results reproduced the experimental results obtained with a 7.60 m³ Guardiola dryer loaded with 2675 kg of wet green coffee grains. The thermal second law efficiency of the drying was calculated with an expression that takes into account the exergy air carries before entering the dryer. For the same coffee load, and with restrictions on grain's temperature (T&#946; < 45°C), final water content (X&#946; < 11%) and water activity (a w < 0.80), the drying was simulated for several air fluxes and temperatures to find the optimum drying conditions (T&#947; = 80°C and G&#947; =6560 kg air.h-1). A 15.80% reduction in energy consumption was achieved when optimization results were compared with the normal operation conditions.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[El objetivo del presente trabajo es determinar las condiciones de operación de un secador de café tipo Guardiola que minimicen el consumo de energía (Q) y maximicen la eficiencia térmica del proceso. Para simular el secado se utilizó un modelo mecanístico para secado de café, resolviéndolo de acuerdo a la suposición de mezclado completo. Los resultados de la simulación reprodujeron la conducta experimental obtenida de un secador tipo Guardiola de 7.60 m³ cargado con 2675 kg de granos de café verde húmedo. Se calculó la eficiencia térmica de segunda Ley del secado con una expresión que toma en cuenta la exergía que el aire posee antes de entrar al secador. Para encontrar las condiciones óptimas de secado, para la misma carga de café y con restricciones de temperatura (T&#946; < 45°C), humedad final (X&#946;< 11%) y actividad de agua del grano (a w < 0.80), se simuló el secado para diferentes flujos y temperaturas de aire. Al comparar las condiciones óptimas encontradas (T&#947; = 80°C and G&#947; = 6560 kg aire.h-1) con las normalmente utilizadas en el beneficio se logró una reducción del 15.80% en el consumo de energía.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[optimization]]></kwd>
<kwd lng="en"><![CDATA[thermal efficiency]]></kwd>
<kwd lng="en"><![CDATA[drying]]></kwd>
<kwd lng="en"><![CDATA[exergy]]></kwd>
<kwd lng="en"><![CDATA[coffee]]></kwd>
<kwd lng="es"><![CDATA[optimización]]></kwd>
<kwd lng="es"><![CDATA[eficiencia térmica]]></kwd>
<kwd lng="es"><![CDATA[secado]]></kwd>
<kwd lng="es"><![CDATA[exergía]]></kwd>
<kwd lng="es"><![CDATA[café]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[  	    <p align="justify"><font face="verdana" size="4">Ingenier&iacute;a de procesos</font></p>     <p align="justify">&nbsp;</p>      <p align="center"><font face="verdana" size="4"><b>Coffee grain rotary drying optimization</b></font></p>     <p align="center">&nbsp;</p>     <p align="center"><font face="verdana" size="3"><b>Optimizaci&oacute;n del secado de granos de caf&eacute; en un secador rotatorio</b></font></p>     <p align="center">&nbsp;</p>     <p align="center"><font face="verdana" size="2"><b>W.N. Hern&aacute;ndez&#45;D&iacute;az<sup>1</sup>*, F.J. Hern&aacute;ndez&#45;Campos<sup>1</sup>, Z. Vargas&#45;Galarza<sup>1</sup>, G.C. Rodr&iacute;guez&#45;Jimenes<sup>2</sup> and M.A. Garc&iacute;a&#45;Alvarado<sup>2</sup></b></font></p>     <p align="center">&nbsp;</p>      <p align="justify"><font face="verdana" size="2"><sup>1</sup><i> Depto. Ingenier&iacute;a Qu&iacute;mica y Bioqu&iacute;mica y Depto. De Posgrado e Investigaci&oacute;n del Instituto Tecnol&oacute;gico de Zacatepec. Calzada Tecnol&oacute;gico 27, Col. Centro, Zacatepec, Morelos, 62780, M&eacute;xico. *Corresponding author. E&#45;mail:</i> <a href="mailto:wendynetz@yahoo.com.mx">wendynetz@yahoo.com.mx</a></font></p>     ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><sup>2</sup><i> Unidad de Investigaci&oacute;n y Desarrollo en Alimentos del Instituto Tecnol&oacute;gico de Veracruz, M.A. de Quevedo.2779, Veracruz, Veracruz, 91987, M&eacute;xico.</i></font></p>     <p align="justify">&nbsp;</p>  	    <p align="justify"><font face="verdana" size="2">Received September 26, 2012    <br> 	</font><font face="verdana" size="2"> Accepted March 18, 2013</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">The objective of the present work was to determine the coffee bean Guardiola dryer operating conditions that minimized the energy consumption (<i>Q</i>) and maximized the process thermal efficiency. A mechanistic coffee bean drying model was solved for a complete mixed assumption to simulate the drying. The simulated results reproduced the experimental results obtained with a 7.60 m<sup>3</sup> Guardiola dryer loaded with 2675 kg of wet green coffee grains. The thermal second law efficiency of the drying was calculated with an expression that takes into account the exergy air carries before entering the dryer. For the same coffee load, and with restrictions on grain's temperature <i>(T<sub>&#946;</sub></i> &lt; 45&deg;C), final water content (<i>X<sub>&#946;</sub></i> &lt; 11&#37;) and water activity (<i>a<sub>w</sub></i> &lt; 0.80), the drying was simulated for several air fluxes and temperatures to find the optimum drying conditions <i>(T<sub>&#947;</sub></i> = 80&deg;C and <i>G<sub>&#947;</sub></i> =6560 kg air.h<sup>&#45;1</sup>). A 15.80&#37; reduction in energy consumption was achieved when optimization results were compared with the normal operation conditions.</font></p>      <p align="justify"><font face="verdana" size="2"><b>Keywords:</b> optimization, thermal efficiency, drying, exergy, coffee.</font></p>     <p align="justify">&nbsp;</p>     <p align="justify"><font face="verdana" size="2"><b>Resumen</b></font></p>      ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2">El objetivo del presente trabajo es determinar las condiciones de operaci&oacute;n de un secador de caf&eacute; tipo Guardiola que minimicen el consumo de energ&iacute;a (<i>Q</i>) y maximicen la eficiencia t&eacute;rmica del proceso. Para simular el secado se utiliz&oacute; un modelo mecan&iacute;stico para secado de caf&eacute;, resolvi&eacute;ndolo de acuerdo a la suposici&oacute;n de mezclado completo. Los resultados de la simulaci&oacute;n reprodujeron la conducta experimental obtenida de un secador tipo Guardiola de 7.60 m<sup>3</sup> cargado con 2675 kg de granos de caf&eacute; verde h&uacute;medo. Se calcul&oacute; la eficiencia t&eacute;rmica de segunda Ley del secado con una expresi&oacute;n que toma en cuenta la exerg&iacute;a que el aire posee antes de entrar al secador. Para encontrar las condiciones &oacute;ptimas de secado, para la misma carga de caf&eacute; y con restricciones de temperatura (<i>T<sub>&#946;</sub></i> &lt; 45&deg;C), humedad final (<i>X<sub>&#946;</sub></i>&lt; 11&#37;) y actividad de agua del grano (<i>a<sub>w</sub></i> &lt; 0.80), se simul&oacute; el secado para diferentes flujos y temperaturas de aire. Al comparar las condiciones &oacute;ptimas encontradas (<i>T<sub>&#947;</sub></i> = 80&deg;C and<i> G<sub>&#947;</sub> </i>= 6560 kg aire.h<sup>&#45;1</sup>) con las normalmente utilizadas en el beneficio se logr&oacute; una reducci&oacute;n del 15.80&#37; en el consumo de energ&iacute;a.</font></p>      <p align="justify"><font face="verdana" size="2"><b>Palabras clave:</b> optimizaci&oacute;n, eficiencia t&eacute;rmica, secado, exerg&iacute;a, caf&eacute;.</font></p>     <p align="justify">&nbsp;</p>     <p align="justify"><font size="2" face="verdana"><a href="/pdf/rmiq/v12n2/v12n2a11.pdf" target="_blank">DESCARGAR ART&Iacute;CULO EN FORMATO PDF</a></font></p>     <p align="justify">&nbsp;</p>     <p align="justify"><font face="verdana" size="2"><b>Referencias</b></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">Akpinar, E.K, Midilli, A. and Bicer, Y. (2005). Energy and exergy of potato drying process via cyclone type drier. <i>Energy Conversion and Management 46,</i> 2530&#45;2552.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8566018&pid=S1665-2738201300020001100001&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">Akpinar, E.K, Midilli, A. and Bicer, Y. (2006). The first and second law analyses of thermodynamic of pumpkin drying process. <i>Journal of Food Engineering 72,</i> 320&#45;331.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8566020&pid=S1665-2738201300020001100002&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    ]]></body>
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