<?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>S1665-27382008000200010</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Análisis comparativo de ecuaciones cinéticas tipo ley de potencia y difusión-integración en la cristalización por enfriamiento de azúcar de caña]]></article-title>
<article-title xml:lang="en"><![CDATA[Comparative analysis of power law type and diffusion-integration kinetic equations in batch cooling of sugar cane]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Quintana-Hernández]]></surname>
<given-names><![CDATA[P. A.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Uribe-Martínez]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Rico-Ramírez]]></surname>
<given-names><![CDATA[V.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Bolaños-Reynoso]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Instituto Tecnológico de Celaya Departamento de Ingeniería Química ]]></institution>
<addr-line><![CDATA[Celaya Gto.]]></addr-line>
<country>México</country>
</aff>
<aff id="A02">
<institution><![CDATA[,Instituto Tecnológico de Orizaba División de Estudios de Posgrado ]]></institution>
<addr-line><![CDATA[Orizaba Ver.]]></addr-line>
<country>México</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>08</month>
<year>2008</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>08</month>
<year>2008</year>
</pub-date>
<volume>7</volume>
<numero>2</numero>
<fpage>171</fpage>
<lpage>182</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382008000200010&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382008000200010&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382008000200010&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[En este trabajo se analiza el proceso de cristalización por enfriamiento de azúcar de caña. Los resultados de simulaciones obtenidas con diferentes tipos de ecuaciones cinéticas (tipo ley de potencia, TLP y ecuaciones de difusión-integración, EDI) son comparados contra resultados experimentales. El proceso de cristalización es modelado con un conjunto de ecuaciones algebraico-integro-diferenciales que representan los balances de masa, energía y población y es resuelto usando el método de líneas. Los resultados muestran que cuando se usan ecuaciones TLP los valores generados para las variables de estado son más cercanos a los valores experimentales que cuando se emplean EDI. Además, se observa que para emplear EDI es necesario incluir parámetros que varíen de acuerdo a las condiciones del proceso.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[In this work, the sugar cane cooling crystallization process is analyzed. Simulation results obtained with different kinetic equations (power-law type, PLT and diffusion-integration equations, DIE) are compared against experimental results. The crystallization process is modeled by a set of algebraic-integral-differential equations that represent the mass, energy and population balances; and it is solved using the method of lines. The results show that PLT equations generate values for the state variables that are closer to experimental information than results obtained with DIE. Further, it is clear that DIE equations require parameters that change according to process conditions.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[azúcar de caña]]></kwd>
<kwd lng="es"><![CDATA[modelos de cristalización]]></kwd>
<kwd lng="es"><![CDATA[simulación]]></kwd>
<kwd lng="en"><![CDATA[sugar cane]]></kwd>
<kwd lng="en"><![CDATA[crystallization model]]></kwd>
<kwd lng="en"><![CDATA[simulation]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="justify"><font face="verdana" size="4">Simulaci&oacute;n y control </font></p>     <p align="justify"><font face="verdana" size="4">&nbsp;</font></p>     <p align="center"><font face="verdana" size="4"><b>An&aacute;lisis comparativo de ecuaciones cin&eacute;ticas tipo ley de potencia y difusi&oacute;n&#150;integraci&oacute;n en la cristalizaci&oacute;n por enfriamiento de az&uacute;car de ca&ntilde;a</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="3"><b>Comparative analysis of power law type and diffusion&#150;integration kinetic equations in batch cooling of sugar cane</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="2"><b>P. A. Quintana&#150;Hern&aacute;ndez<sup>1</sup>*, B. Uribe&#150;Mart&iacute;nez<sup>1</sup>,V. Rico&#150;Ram&iacute;rez<sup>1</sup> y E. Bola&ntilde;os&#150;Reynoso<sup>2</sup></b></font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><i><sup>1</sup> Instituto Tecnol&oacute;gico de Celaya, Dpto. de Ingenier&iacute;a Qu&iacute;mica. Av. Tecnol&oacute;gico y Antonio Garc&iacute;a Cubas s/n, 38010 Celaya, Gto., M&eacute;xico. <i>* Autor para la correspondencia. E&#150;mail: </i></i><a href="mailto:pedro@iqcelaya.itc.mx">pedro@iqcelaya.itc.mx</a><i><i> Tel. (461)6117802</i></i></font></p>     <p align="justify"><font face="verdana" size="2"><i><sup>2</sup> Divisi&oacute;n de Estudios de Posgrado, Instituto Tecnol&oacute;gico de Orizaba, Orizaba Ver., M&eacute;xico.</i></font></p>     ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2">Recibido 30 de Agosto 2007    <br> Aceptado 24 de Abril 2008</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 este trabajo se analiza el proceso de cristalizaci&oacute;n por enfriamiento de az&uacute;car de ca&ntilde;a. Los resultados de simulaciones obtenidas con diferentes tipos de ecuaciones cin&eacute;ticas (tipo ley de potencia, TLP y ecuaciones de difusi&oacute;n&#150;integraci&oacute;n, EDI) son comparados contra resultados experimentales. El proceso de cristalizaci&oacute;n es modelado con un conjunto de ecuaciones algebraico&#150;integro&#150;diferenciales que representan los balances de masa, energ&iacute;a y poblaci&oacute;n y es resuelto usando el m&eacute;todo de l&iacute;neas. Los resultados muestran que cuando se usan ecuaciones TLP los valores generados para las variables de estado son m&aacute;s cercanos a los valores experimentales que cuando se emplean EDI. Adem&aacute;s, se observa que para emplear EDI es necesario incluir par&aacute;metros que var&iacute;en de acuerdo a las condiciones del proceso.</font></p>     <p align="justify"><font face="verdana" size="2"><b>Palabras clave: </b>az&uacute;car de ca&ntilde;a, modelos de cristalizaci&oacute;n, simulaci&oacute;n.</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, the sugar cane cooling crystallization process is analyzed. Simulation results obtained with different kinetic equations (power&#150;law type, PLT and diffusion&#150;integration equations, DIE) are compared against experimental results. The crystallization process is modeled by a set of algebraic&#150;integral&#150;differential equations that represent the mass, energy and population balances; and it is solved using the method of lines. The results show that PLT equations generate values for the state variables that are closer to experimental information than results obtained with DIE. Further, it is clear that DIE equations require parameters that change according to process conditions.</font></p>     ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><b>Keywords: </b>sugar cane, crystallization model, simulation.</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/v7n2/v7n2a10.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>Agradecimientos</b></font></p>     <p align="justify"><font face="verdana" size="2">Los autores agradecen sinceramente los apoyos econ&oacute;micos del Consejo Nacional de Ciencia y Tecnolog&iacute;a (CONACYT), Direcci&oacute;n General de Educaci&oacute;n Superior Tecnol&oacute;gica (DGEST), Instituto Tecnol&oacute;gico de Celaya (ITC) e Instituto Tecnol&oacute;gico de Orizaba (ITO).</font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><b>Referencias</b></font></p>     <!-- ref --><p align="justify"><font face="verdana" size="2">Bola&ntilde;os, R. E. (2000). <i>Control y Optimizaci&oacute;n de las Condiciones de Operaci&oacute;n de Cristalizadores Batch por Enfriamiento. </i>Tesis Doctoral en Ingenier&iacute;a Qu&iacute;mica, Instituto Tecnol&oacute;gico de Celaya, M&eacute;xico.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8585812&pid=S1665-2738200800020001000001&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>     ]]></body>
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