<?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>S1665-27382014000200026</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Planteamiento de una métrica de la representación linealizada de un sistema no lineal: Aplicación para reactores (bio)químicos]]></article-title>
<article-title xml:lang="en"><![CDATA[Approach of a measurement of linearized representation of a nonlinear system: Application to (bio)chemical reactors]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Carrillo-Ahumada]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Páramo-Calderón]]></surname>
<given-names><![CDATA[D.E.]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Aparicio-Saguilán]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Rodríguez-Jimenes]]></surname>
<given-names><![CDATA[G.C.]]></given-names>
</name>
<xref ref-type="aff" rid="A03"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[García-Alvarado]]></surname>
<given-names><![CDATA[M.A.]]></given-names>
</name>
<xref ref-type="aff" rid="A03"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universidad del Papaloapan Instituto de Química Aplicada ]]></institution>
<addr-line><![CDATA[Tuxtepec Oaxaca]]></addr-line>
<country>México</country>
</aff>
<aff id="A02">
<institution><![CDATA[,Universidad del Papaloapan Instituto de Biotecnología ]]></institution>
<addr-line><![CDATA[Tuxtepec Oaxaca]]></addr-line>
<country>México</country>
</aff>
<aff id="A03">
<institution><![CDATA[,Instituto Tecnológico de Veracruz Departamento de Ingeniería Química y Bioquímica ]]></institution>
<addr-line><![CDATA[Veracruz ]]></addr-line>
<country>México</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2014</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2014</year>
</pub-date>
<volume>13</volume>
<numero>2</numero>
<fpage>631</fpage>
<lpage>647</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382014000200026&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382014000200026&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382014000200026&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Se plantea un métrica para determinar la representación de un sistema linealizado con respecto al sistema no lineal. Esta métrica está basada en la expansión en series de Taylor de un sistema no lineal y fue aplicada para tres reactores (bio)químicos entre ellos el biorreactor de Cholette con multiplicidad de entradas, salidas y de estados estacionarios; un biorreactor con reacción enzimática y un reactor químico, aunque puede aplicarse para cualquier sistema no lineal. Se considera que el cociente de las matrices de primeras y segundas derivadas debe ser menor a la matriz de desviación de los valores nominales. Con este análisis, es posible determinar la influencia de cada parámetro en el sistema no lineal de estudio y su aplicación se encuentra en simulación y control.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[A new criterion of measurement was proposed to determine the representation of a linearized system with respect to nonlinear system. This criterion is based on the Taylor series expansion of nonlinear system and was applied to three (bio)chemical reactors including the Cholette's bioreactor with multiple inputs, outputs and steady states; a reactor with enzymatic reaction and a chemical reactor. Current approach considers that matrix elements resulting from left division of matrices containing second-order and first-order partial derivatives should be smaller than deviations from the nominal values. With this analysis, is possible to determine the influence of each bifurcation parameter on the nonlinear system for simulation and control applications.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[sistemas no lineales]]></kwd>
<kwd lng="es"><![CDATA[linealización]]></kwd>
<kwd lng="es"><![CDATA[series de Taylor]]></kwd>
<kwd lng="es"><![CDATA[reactores (bio)químicos]]></kwd>
<kwd lng="en"><![CDATA[nonlinear systems]]></kwd>
<kwd lng="en"><![CDATA[linearization]]></kwd>
<kwd lng="en"><![CDATA[Taylor series]]></kwd>
<kwd lng="en"><![CDATA[(bio)chemical reactors]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="justify"><font face="verdana" size="4">Art&iacute;culos regulares/Simulaci&oacute;n y control</font></p>              <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>         <p align="center"><font face="verdana" size="4"><b>Planteamiento de una m&eacute;trica de la representaci&oacute;n linealizada de un sistema no lineal. Aplicaci&oacute;n para reactores (bio)qu&iacute;micos</b></font></p>         <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>         <p align="center"><font face="verdana" size="3"><b>Approach of a measurement of linearized representation of a nonlinear system. Application to (bio)chemical reactors</b></font></p>         <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>         <p align="center"><font face="verdana" size="2"><b>J. Carrillo&#45;Ahumada<sup>1</sup>*, D.E. P&aacute;ramo&#45;Calder&oacute;n<sup>2</sup>, A. Aparicio&#45;Saguil&aacute;n<sup>2</sup>, G.C. Rodr&iacute;guez&#45;Jimenes<sup>3</sup> y M.A. Garc&iacute;a&#45;Alvarado<sup>3</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 de Qu&iacute;mica Aplicada. Universidad del Papaloapan. Circuito Central 200, colonia Parque Industrial, Tuxtepec, Oax. 688301, M&eacute;xico. *E&#45;mail:</i> <a href="mailto:jcarrillo@unpa.edu.mx">jcarrillo@unpa.edu.mx</a>; <a href="mailto:jesuscarrillo18@yahoo.com">jesuscarrillo18@yahoo.com</a><i> Tel. 01 (287) 8 75 92 40 Ext. 230</i></font></p>         <p align="justify"><font face="verdana" size="2"><i><sup>2</sup> Instituto de Biotecnolog&iacute;a. Universidad del Papaloapan. Circuito Central 200, colonia Parque Industrial, Tuxtepec, Oax. 68301, M&eacute;xico. </i></font></p>         ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><i><sup>3</sup> Departamento de Ingenier&iacute;a Qu&iacute;mica y Bioqu&iacute;mica. Instituto Tecnol&oacute;gico de Veracruz. Av. Miguel &Aacute;ngel de </i><i>Quevedo 2779, Veracruz, Ver. 91860, M&eacute;xico.</i></font></p>         <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>         <p align="justify"><font face="verdana" size="2">Recibido 12 de Diciembre de 2013.    <br> Aceptado 16 de Marzo de 2014.</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">Se plantea un m&eacute;trica para determinar la representaci&oacute;n de un sistema linealizado con respecto al sistema no lineal. Esta m&eacute;trica est&aacute; basada en la expansi&oacute;n en series de Taylor de un sistema no lineal y fue aplicada para tres reactores (bio)qu&iacute;micos entre ellos el biorreactor de Cholette con multiplicidad de entradas, salidas y de estados estacionarios; un biorreactor con reacci&oacute;n enzim&aacute;tica y un reactor qu&iacute;mico, aunque puede aplicarse para cualquier sistema no lineal. Se considera que el cociente de las matrices de primeras y segundas derivadas debe ser menor a la matriz de desviaci&oacute;n de los valores nominales. Con este an&aacute;lisis, es posible determinar la influencia de cada par&aacute;metro en el sistema no lineal de estudio y su aplicaci&oacute;n se encuentra en simulaci&oacute;n y control.</font></p>              <p align="justify"><font face="verdana" size="2"><b>Palabras clave:</b> sistemas no lineales, linealizaci&oacute;n, series de Taylor, reactores (bio)qu&iacute;micos. </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>         ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2">A new criterion of measurement was proposed to determine the representation of a linearized system with respect to nonlinear system. This criterion is based on the Taylor series expansion of nonlinear system and was applied to three (bio)chemical reactors including the Cholette's bioreactor with multiple inputs, outputs and steady states; a reactor with enzymatic reaction and a chemical reactor. Current approach considers that matrix elements resulting from left division of matrices containing second&#45;order and first&#45;order partial derivatives should be smaller than deviations from the nominal values. With this analysis, is possible to determine the influence of each bifurcation parameter on the nonlinear system for simulation and control applications.</font></p>              <p align="justify"><font face="verdana" size="2"><b>Keywords:</b> nonlinear systems, linearization, Taylor series, (bio)chemical reactors.</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/v13n2/v13n2a26.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 al Programa de Mejoramiento del Profesorado (PROMEP) por el financiamiento parcial para esta investigaci&oacute;n mediante el proyecto "An&aacute;lisis de Estabilidad de Procesos Qu&iacute;micos y Alimentarios con Controladores &Oacute;ptimo&#45;Robustos" (PROMEP/103.5/12/7959; UNPA&#45;PTC&#45;119).</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">Carrillo&#45;Ahumada, J., Rodr&iacute;guez&#45;Jimenes, G.C. y Garc&iacute;a&#45;Alvarado, M.A. (2011). 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