<?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>S1665-27382008000300016</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Mejora en el control en cascada para reactores tubulares]]></article-title>
<article-title xml:lang="en"><![CDATA[Improved cascade control scheme for tubular reactors]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Hernández-Martínez]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Urrea]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Alvarez-Ramirez]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universidad Autónoma Metropolitana-Iztapalapa  ]]></institution>
<addr-line><![CDATA[ DF]]></addr-line>
<country>México</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>12</month>
<year>2008</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>12</month>
<year>2008</year>
</pub-date>
<volume>7</volume>
<numero>3</numero>
<fpage>309</fpage>
<lpage>318</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382008000300016&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382008000300016&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382008000300016&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Los reactores tubulares son difíciles de operar debido al acoplamiento intrínsico entre los procesos de transporte, cinética no lineal y su naturaleza distribuida. Debido a las numerosas aplicaciones industriales de los reactores tubulares, el problema de monitoreo y control efectivo es de gran importancia económica y de seguridad. En este trabajo introducimos una nueva configuración del esquema de control en cascada basada en el promedio de la medición de tres temperaturas distribuidas a lo largo de la posición axial del reactor tubular (w av). La configuración del control explota la información provista por dos sensores de temperatura adicionales localizados cerca de la alimentación y salida del reactor. La configuración con (w av) mejora el comportamiento del esquema clásico de control en cascada frente a perturbaciones e incertidumbre de los parámetros del modelo. Mediante simulaciones numéricas se ilustra y compara el desempeño del control propuesto.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Tubular reactors are difficult to operate due the intricate coupling between transport processes, nonlinear chemical kinetics, and their distributed nature. However, due to numerous industrial applications for chemical tubular reactors, the problem of monitoring and controlling them effectively is of great safety and economical importance. In this work, we introduce a new cascade control scheme based on three-temperature measurement distributed along the axial position of the tubular reactor with respect to a weighted average temperature (w av). The control configuration exploits the information provided by two additional temperatures sensor located at the feed and the output of the tubular reactor. The configuration with w av improves the behavior of the control scheme by enhancing the disturbance and parameter's uncertainty. Numerical simulations are used to illustrate and compare the control performance.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[control en cascada]]></kwd>
<kwd lng="es"><![CDATA[temperatura promedio]]></kwd>
<kwd lng="es"><![CDATA[reactor tubular]]></kwd>
<kwd lng="en"><![CDATA[cascade control]]></kwd>
<kwd lng="en"><![CDATA[average temperature]]></kwd>
<kwd lng="en"><![CDATA[tubular reactor]]></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>Mejora en el control en cascada para reactores tubulares</b></font><font face="verdana" size="2"><b> </b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="3"><b>Improved cascade control scheme for tubular reactors</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="2"><b>E. Hern&aacute;ndez&#150;Mart&iacute;nez , R. Urrea y J. Alvarez&#150;Ramirez</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><i>Universidad Aut&oacute;noma Metropolitana&#151;Iztapalapa, Apartado postal 55&#150;534, lztapalapa, DF., 09340 M&eacute;xico </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 26 de Junio 2008    <br> Aceptado 28 de Octubre 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 reactores tubulares son dif&iacute;ciles de operar debido al acoplamiento intr&iacute;nsico entre los procesos de transporte, cin&eacute;tica no lineal y su naturaleza distribuida. Debido a las numerosas aplicaciones industriales de los reactores tubulares, el problema de monitoreo y control efectivo es de gran importancia econ&oacute;mica y de seguridad. En este trabajo introducimos una nueva configuraci&oacute;n del esquema de control en cascada basada en el promedio de la medici&oacute;n de tres temperaturas distribuidas a lo largo de la posici&oacute;n axial del reactor tubular (w<i><sub>av</sub></i>). La configuraci&oacute;n del control explota la informaci&oacute;n provista por dos sensores de temperatura adicionales localizados cerca de la alimentaci&oacute;n y salida del reactor. La configuraci&oacute;n con (w<i><sub>av</sub></i>) mejora el comportamiento del esquema cl&aacute;sico de control en cascada frente a perturbaciones e incertidumbre de los par&aacute;metros del modelo. Mediante simulaciones num&eacute;ricas se ilustra y compara el desempe&ntilde;o del control propuesto.</font></p>     <p align="justify"><font face="verdana" size="2"><b>Palabras clave: </b>control en cascada, temperatura promedio, reactor tubular.</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">Tubular reactors are difficult to operate due the intricate coupling between transport processes, nonlinear chemical kinetics, and their distributed nature. However, due to numerous industrial applications for chemical tubular reactors, the problem of monitoring and controlling them effectively is of great safety and economical importance. In this work, we introduce a new cascade control scheme based on three&#150;temperature measurement distributed along the axial position of the tubular reactor with respect to a weighted average temperature (w<i><sub>av</sub></i>). The control configuration exploits the information provided by two additional temperatures sensor located at the feed and the output of the tubular reactor. The configuration with w<i><sub>av</sub></i> improves the behavior of the control scheme by enhancing the disturbance and parameter's uncertainty. Numerical simulations are used to illustrate and compare the control performance.</font></p>      <p align="justify"><font face="verdana" size="2"><b>Keywords: </b>cascade control, average temperature, tubular reactor.</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/v7n3/v7n3a16.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>Referencias</b></font></p>     <!-- ref --><p align="justify"><font face="verdana" size="2">Alvarez&#150;Ramirez J., Suarez R., and Morales A. (2000). 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