<?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>S1665-27382009000100014</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Desempeño dinámico de esquemas alternativos a la columna petlyuk (columna de pared divisoria) para la separación de mezclas ternarias]]></article-title>
<article-title xml:lang="en"><![CDATA[Dynamic behavior of alternate schemes to petlyuk column (dividing wall column) for separation of ternary mixtures]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Martínez-Cisneros]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Hernández-Sánchez]]></surname>
<given-names><![CDATA[A. A.]]></given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Segovia-Hernández]]></surname>
<given-names><![CDATA[J.G.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Hernández]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Hernández]]></surname>
<given-names><![CDATA[H]]></given-names>
</name>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universidad de Guanajuato Departamento de Ingeniería Química ]]></institution>
<addr-line><![CDATA[Guanajuato Gto.]]></addr-line>
<country>México</country>
</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>135</fpage>
<lpage>144</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382009000100014&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382009000100014&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382009000100014&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Los sistemas de destilación térmicamente acoplados han sido propuestos ya que pueden efectuar la tarea de separación de una mezcla utilizando bajos consumos energéticos en comparación con los esquemas convencionales de destilación. La estructura de estos sistemas complejos ofrece retos en el área de control debido a la transferencia de corrientes de vapor (o líquido) entre las columnas. En particular, la presencia de los reciclos en estos sistemas acoplados ha generado la noción de que algunos problemas de control pueden ser detectados durante la operación de dichos sistemas en comparación con el buen desempeño de las secuencias de destilación convencionales. Esta es una de las principales razones para que no haya un amplio uso de las columnas térmicamente acopladas a nivel industrial. Recientemente algunos esquemas alternos a la columna Petlyuk han sido propuestos. En este trabajo se analiza las propiedades de control de dos esquemas alternativos a la columna Petlyuk. El desempeño dinámico de los sistemas es analizado utilizando la técnica de la descomposición en valores singulares y mediante simulaciones dinámicas rigurosas. Los resultados muestran que las estructuras alternativas muestran mejores propiedades de control que la estructura Petlyuk convencional.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Thermally coupled distillation systems have been proposed to perform distillation separation tasks with the incentive of achieving lower energy consumption levels with respect to conventional distillation sequences. The structure of the complex systems offers some control challenges arising from the transfer of vapor (or liquid) streams between the columns. In particular, the presence of recycle streams in the coupled schemes has influenced the notion that control problems might be expected during the operation of those systems with respect to the rather well-known behavior of conventional distillation sequences. That has been one of the main reasons for the lack of industrial implementation of thermally coupled distillation schemes. Recently, some alternate schemes to Petlyuk column have been proposed. In this work, we analyze the control properties of two alternative distillation schemes to the Petlyuk column. The dynamic behavior is analyzed using the technique of singular value decomposition and rigorous dynamic simulations. The results indicate that alternate structures show better control properties than traditional Petlyuk structure.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[columna Petlyuk]]></kwd>
<kwd lng="es"><![CDATA[propiedades de control]]></kwd>
<kwd lng="es"><![CDATA[ahorro de energía]]></kwd>
<kwd lng="es"><![CDATA[columnas alternativas]]></kwd>
<kwd lng="es"><![CDATA[diseño]]></kwd>
<kwd lng="en"><![CDATA[Petlyuk column]]></kwd>
<kwd lng="en"><![CDATA[control properties]]></kwd>
<kwd lng="en"><![CDATA[energy savings]]></kwd>
<kwd lng="en"><![CDATA[alternative sequences]]></kwd>
<kwd lng="en"><![CDATA[design]]></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>Desempe&ntilde;o din&aacute;mico de esquemas alternativos a la columna petlyuk (columna de pared divisoria) para la separaci&oacute;n de mezclas ternarias</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="3"><b>Dynamic behavior of alternate schemes to petlyuk column (dividing wall column) for separation of ternary mixtures</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="2"><b>J. Mart&iacute;nez&#150;Cisneros, A. A. Hern&aacute;ndez&#150;S&aacute;nchez, J.G. Segovia&#150;Hern&aacute;ndez*, S. Hern&aacute;ndez, H. Hern&aacute;ndez</b></font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><i>Universidad de Guanajuato, Departamento de Ingenier&iacute;a Qu&iacute;mica, Noria Alta s/n, Guanajuato, Gto., M&eacute;xico 36050. <i>* Autor para la correspondencia. E&#150;mail: </i></i><a href="mailto:gsegovia@quijote.ugto.mx">gsegovia@quijote.ugto.mx</a><i><i> Tel: (52) 473 73 20006 ext 8142</i></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 25 de Julio 2008    <br>   Aceptado 8 de Diciembre 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">Los sistemas de destilaci&oacute;n t&eacute;rmicamente acoplados han sido propuestos ya que pueden efectuar la tarea de separaci&oacute;n de una mezcla utilizando bajos consumos energ&eacute;ticos en comparaci&oacute;n con los esquemas convencionales de destilaci&oacute;n. La estructura de estos sistemas complejos ofrece retos en el &aacute;rea de control debido a la transferencia de corrientes de vapor (o l&iacute;quido) entre las columnas. En particular, la presencia de los reciclos en estos sistemas acoplados ha generado la noci&oacute;n de que algunos problemas de control pueden ser detectados durante la operaci&oacute;n de dichos sistemas en comparaci&oacute;n con el buen desempe&ntilde;o de las secuencias de destilaci&oacute;n convencionales. Esta es una de las principales razones para que no haya un amplio uso de las columnas t&eacute;rmicamente acopladas a nivel industrial. Recientemente algunos esquemas alternos a la columna Petlyuk han sido propuestos. En este trabajo se analiza las propiedades de control de dos esquemas alternativos a la columna Petlyuk. El desempe&ntilde;o din&aacute;mico de los sistemas es analizado utilizando la t&eacute;cnica de la descomposici&oacute;n en valores singulares y mediante simulaciones din&aacute;micas rigurosas. Los resultados muestran que las estructuras alternativas muestran mejores propiedades de control que la estructura Petlyuk convencional.</font></p>     <p align="justify"><font face="verdana" size="2"><b>Palabras clave: </b>columna Petlyuk, propiedades de control, ahorro de energ&iacute;a, columnas alternativas, dise&ntilde;o.</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">Thermally coupled distillation systems have been proposed to perform distillation separation tasks with the incentive of achieving lower energy consumption levels with respect to conventional distillation sequences. The structure of the complex systems offers some control challenges arising from the transfer of vapor (or liquid) streams between the columns. In particular, the presence of recycle streams in the coupled schemes has influenced the notion that control problems might be expected during the operation of those systems with respect to the rather well&#150;known behavior of conventional distillation sequences. That has been one of the main reasons for the lack of industrial implementation of thermally coupled distillation schemes. Recently, some alternate schemes to Petlyuk column have been proposed. In this work, we analyze the control properties of two alternative distillation schemes to the Petlyuk column. The dynamic behavior is analyzed using the technique of singular value decomposition and rigorous dynamic simulations. The results indicate that alternate structures show better control properties than traditional Petlyuk structure.</font></p>     <p align="justify"><font face="verdana" size="2"><b>Keywords: </b>Petlyuk column, control properties, energy savings, alternative sequences, design.</font></p>     ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><a href="/pdf/rmiq/v8n1/v8n1a14.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 muestran un agradecimiento a la Universidad de Guanajuato, CONACyT y CONCyTEG por el apoyo brindado para la realizaci&oacute;n de este trabajo.</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">Agrawal, R., Fidkowski, Z. (1998). 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