<?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>S1665-27382010000300008</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Estructura de control jerárquico aplicada a un reactor de amoniaco, tipo tubular, con enfriamiento intermedio]]></article-title>
<article-title xml:lang="en"><![CDATA[A hierarchic control structure applied to an ammonia tubular reactor with cold shot cooling]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[García]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Fernández-Anaya]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vargas-Villamil]]></surname>
<given-names><![CDATA[F.D.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Orduña]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Instituto Mexicano del Petróleo Matemáticas Aplicadas y Computación ]]></institution>
<addr-line><![CDATA[México D.F.]]></addr-line>
</aff>
<aff id="A02">
<institution><![CDATA[,Universidad Iberoamericana Departamento de Física y Matemáticas ]]></institution>
<addr-line><![CDATA[México D. F.]]></addr-line>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>12</month>
<year>2010</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>12</month>
<year>2010</year>
</pub-date>
<volume>9</volume>
<numero>3</numero>
<fpage>329</fpage>
<lpage>341</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382010000300008&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382010000300008&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382010000300008&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Las estructuras de control jerárquicas son útiles en procesos altamente integrados puesto que descomponen un sistema complejo en varios subsistemas que pueden tener diferentes objetivos (e.g. estabilización, desempeño, optimización) o escalas de tiempo. En este trabajo se propone una estructura jerárquica para el control de un reactor de amoniaco con enfriamiento intermedio que es altamente no lineal y está fuertemente acoplado. El sistema de control jerárquico tiene tres niveles. El primer nivel está compuesto de controladores tipo PI y su principal objetivo es la estabilización. El segundo nivel está compuesto de un consolador interpolante que provee la temperatura de referencia para el control de la primera cama del reactor. Su objetivo es ampliar el rango de operación del controlador y por lo tanto mejorar el desempeño. El tercer nivel está compuesto de un optimizador cuyo objetivo es maximizar la producción de amoniaco. Los resultados muestran que la estructura jerárquica permite tener un control robusto y estable en un amplio rango de operación, manteniendo las salidas de control en su valor de referencia y rechazando las perturbaciones.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Hierarchical control fractures eire useful in highly integrated processes, since they decompose a complex system in various subsystems, which may have different objectives (e.g. stabilization, performance, optimization) or scales of time. In this work, a hierarchical straciure ior the control of an ammonia reactor with cold-shot cooling, which is highly nonlinear and strongly coupled, is proposed. This hierarchical control system has three levels. The first level is composed of PI type controllers, and its main objective is stabilization. The second level is composed of an interpolated controller that provides the reference temperature for the control of the first bed of the reactor. Its objective is to extend the operating range of the controller and therefore, "to improve the performance. The Third level is composed of an optimizer whose objective is to maximize the ammonia production. The results show that the hierarchical structure results in a robust and stable controller in a large operating range, keeping the control outputs on its reference while rejecting the disturbances.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[estructura jerárquica]]></kwd>
<kwd lng="es"><![CDATA[control interpolante]]></kwd>
<kwd lng="es"><![CDATA[control en cascada]]></kwd>
<kwd lng="es"><![CDATA[camas de catalizador]]></kwd>
<kwd lng="en"><![CDATA[structure]]></kwd>
<kwd lng="en"><![CDATA[interpolate controller]]></kwd>
<kwd lng="en"><![CDATA[cascade controller]]></kwd>
<kwd lng="en"><![CDATA[catalyst beds]]></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"><font face="verdana" size="4">&nbsp;</font></p>     <p align="center"><font face="verdana" size="4"><b>Estructura de control jer&aacute;rquico aplicada a un reactor de amoniaco, tipo tubular, con enfriamiento intermedio</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="3"><b>A hierarchic control structure applied to an ammonia tubular reactor with cold shot cooling</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="2"><b>J. Garc&iacute;a<sup>1</sup>, G. Fern&aacute;ndez&#150;Anaya<sup>2</sup>*, F.D. Vargas&#150;Villamil<sup>1</sup> y E. Ordu&ntilde;a<sup>1</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>Matem&aacute;ticas Aplicadas y Computaci&oacute;n, Instituto Mexicano del Petr&oacute;leo Eje Central L&aacute;zaro C&aacute;rdenas 152, M&eacute;xico, D.F. 07330</i></font></p>     <p align="justify"><font face="verdana" size="2"><i><sup>2</sup> Depto. de F&iacute;sica y Matem&aacute;ticas, Universidad Iberoamericana, Prolongaci&oacute;n Paseo de la Reforma 880, Col. Lomas de Santa Fe, M&eacute;xico, D. F. 01210. <i>*Autor para la correspondencia. E&#150;mail: </i></i><a href="mailto:guillermo.fernandez@uia.mx">guillermo.fernandez@uia.mx</a></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 31 de Mayo 2010.    <br> Aceptado 18 de Agosto 2010.</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">Las estructuras de control jer&aacute;rquicas son &uacute;tiles en procesos altamente integrados puesto que descomponen un sistema complejo en varios subsistemas que pueden tener diferentes objetivos (e.g. estabilizaci&oacute;n, desempe&ntilde;o, optimizaci&oacute;n) o escalas de tiempo. En este trabajo se propone una estructura jer&aacute;rquica para el control de un reactor de amoniaco con enfriamiento intermedio que es altamente no lineal y est&aacute; fuertemente acoplado. El sistema de control jer&aacute;rquico tiene tres niveles. El primer nivel est&aacute; compuesto de controladores tipo PI y su principal objetivo es la estabilizaci&oacute;n. El segundo nivel est&aacute; compuesto de un consolador interpolante que provee la temperatura de referencia para el control de la primera cama del reactor. Su objetivo es ampliar el rango de operaci&oacute;n del controlador y por lo tanto mejorar el desempe&ntilde;o. El tercer nivel est&aacute; compuesto de un optimizador cuyo objetivo es maximizar la producci&oacute;n de amoniaco. Los resultados muestran que la estructura jer&aacute;rquica permite tener un control robusto y estable en un amplio rango de operaci&oacute;n, manteniendo las salidas de control en su valor de referencia y rechazando las perturbaciones.</font></p>     <p align="justify"><font face="verdana" size="2"><b>Palabras clave: </b>estructura jer&aacute;rquica, control interpolante, control en cascada, camas de catalizador. </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">Hierarchical control fractures eire useful in highly integrated processes, since they decompose a complex system in various subsystems, which may have different objectives (e.g. stabilization, performance, optimization) or scales of time. In this work, a hierarchical straciure ior the control of an ammonia reactor with cold&#150;shot cooling, which is highly nonlinear and strongly coupled, is proposed. This hierarchical control system has three levels. The first level is composed of PI type controllers, and its main objective is stabilization. The second level is composed of an interpolated controller that provides the reference temperature for the control of the first bed of the reactor. Its objective is to extend the operating range of the controller and therefore, "to improve the performance. The Third level is composed of an optimizer whose objective is to maximize the ammonia production. The results show that the hierarchical structure results in a robust and stable controller in a large operating range, keeping the control outputs on its reference while rejecting the disturbances.</font></p>     ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><b>Keywords: </b>structure, interpolate controller, cascade controller, catalyst beds.</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/v9n3/v9n3a8.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">Astr&ouml;m, K.J., H&auml;gglund, T. (2004) Revisiting the Ziegler&#150;Nichols step response method for PID control , Instrument Society of America, Research Triangle Park, NC.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543233&pid=S1665-2738201000030000800001&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">Doyle, J.C., Francis, B.A., Tannenbaum, A.R. (1990) <i>Feedback Control Theory, </i>Macmillan, New York.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543235&pid=S1665-2738201000030000800002&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">Fen&aacute;ndez&#150;Anaya, G., Flores&#150;Tlacuahuac, A. (2006) Interpolated controllers for the robust transition control of a class of reactors. <i>AIChE J. 52(1), </i>247&#150;254.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543237&pid=S1665-2738201000030000800003&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">Froment, G. F., Bischoff, K. B. (1990) <i>Chemical </i><i>Reactor Analysis and Design, </i>2nd ed., Wiley, New York.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543239&pid=S1665-2738201000030000800004&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">Garc&iacute;a, J., Fern&aacute;ndez&#150;Anaya, G., Vargas&#150;Villamil, F. D., Rosales&#150;Quintero, A. (2009) Interpolated control of a fixed&#150;bed reactor with cold&#150;shot cooling. <i>Chemical Engineering Communications196(10), </i>12621277.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543241&pid=S1665-2738201000030000800005&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">Kreith, F., Bohn, M. S. (1993) <i>Principles of Heat Transfer, </i>5th ed., West Publishing Co., St. Paul.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543243&pid=S1665-2738201000030000800006&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">Maarleveld,  A.,   Rijnsdorp,   J. E. (1970) Constraint control of distillation columns. <i>Automatica 6, </i>51&#150;58.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543245&pid=S1665-2738201000030000800007&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">Morari, M. Arkun, Y., Stephanoupoulos, G. (1980a) Studies in the synthesis of control structures for chemical processes, Part I. <i>AIChE J. 26 </i>(2), 220&#150;232.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543247&pid=S1665-2738201000030000800008&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">Morari, M., Stephanoupoulos, G. (1980b) Structural aspects in the synthesis of alternative feasible control schemes, Part II. <i>AIChE J. 26 </i>(2), 232&#150;246.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543249&pid=S1665-2738201000030000800009&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">Morud, J. (1995) <i>Studies of the dynamics and operation of integrated plants. </i>Phd thesis, Norwegian Univ. of Science and Technology, Trondheim.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543251&pid=S1665-2738201000030000800010&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">Morud, J. C. Skogestad, S. (1998) Analysis of instability in an industrial ammonia reactor, AIChE J., 44 (4), pp 888&#150;895.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543253&pid=S1665-2738201000030000800011&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">Rivera, D. E., Morari, M., Skogestad, S. (1986) Internal model control: 4 PID controller design. <i>Industrial &amp; Engineering Chemistry </i><i>Research 25 </i>(1), 252&#150;265.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543255&pid=S1665-2738201000030000800012&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">Silverstein, J. L., Shirmar R. (1982) Effect of Design on the Stability and Control of Fixed Bed Reactors with Heat Feedback. <i>Industrial and Engineering Chemistry Process Design and Development 21, </i>241253.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543257&pid=S1665-2738201000030000800013&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">Skogestad, S. (2003) Simple Analytic Rules for Model Reduction and PID Controller Tuning. <i>Journal of Process Control 13, </i>291309.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543259&pid=S1665-2738201000030000800014&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">Stephens, A. D., Richards, R. J. (1973) Steady State and Dynamic Analysis of an Ammonia Synthesis Plant. <i>Automatica 9, </i>65&#150;78.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8543261&pid=S1665-2738201000030000800015&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>      ]]></body><back>
<ref-list>
<ref id="B1">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Aström]]></surname>
<given-names><![CDATA[K.J.]]></given-names>
</name>
<name>
<surname><![CDATA[Hägglund]]></surname>
<given-names><![CDATA[T.]]></given-names>
</name>
</person-group>
<source><![CDATA[Revisiting the Ziegler-Nichols step response method for PID control]]></source>
<year>2004</year>
<publisher-loc><![CDATA[^eNC NC]]></publisher-loc>
<publisher-name><![CDATA[Instrument Society of AmericaResearch Triangle Park]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B2">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Doyle]]></surname>
<given-names><![CDATA[J.C.]]></given-names>
</name>
<name>
<surname><![CDATA[Francis]]></surname>
<given-names><![CDATA[B.A.]]></given-names>
</name>
<name>
<surname><![CDATA[Tannenbaum]]></surname>
<given-names><![CDATA[A.R.]]></given-names>
</name>
</person-group>
<source><![CDATA[Feedback Control Theory]]></source>
<year>1990</year>
<publisher-loc><![CDATA[New York ]]></publisher-loc>
<publisher-name><![CDATA[Macmillan]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B3">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Fenández-Anaya]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Flores-Tlacuahuac]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Interpolated controllers for the robust transition control of a class of reactors]]></article-title>
<source><![CDATA[AIChE J]]></source>
<year>2006</year>
<volume>52</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>247-254</page-range></nlm-citation>
</ref>
<ref id="B4">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Froment]]></surname>
<given-names><![CDATA[G. F.]]></given-names>
</name>
<name>
<surname><![CDATA[Bischoff]]></surname>
<given-names><![CDATA[K. B.]]></given-names>
</name>
</person-group>
<source><![CDATA[Chemical Reactor Analysis and Design]]></source>
<year>1990</year>
<edition>2</edition>
<publisher-loc><![CDATA[New York ]]></publisher-loc>
<publisher-name><![CDATA[Wiley]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B5">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[García]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Fernández-Anaya]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Vargas-Villamil]]></surname>
<given-names><![CDATA[F. D.]]></given-names>
</name>
<name>
<surname><![CDATA[Rosales-Quintero]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Interpolated control of a fixed-bed reactor with cold-shot cooling]]></article-title>
<source><![CDATA[Chemical Engineering Communications]]></source>
<year>2009</year>
<volume>196</volume>
<numero>10</numero>
<issue>10</issue>
<page-range>12621277</page-range></nlm-citation>
</ref>
<ref id="B6">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Kreith]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Bohn]]></surname>
<given-names><![CDATA[M. S.]]></given-names>
</name>
</person-group>
<source><![CDATA[Principles of Heat Transfer]]></source>
<year>1993</year>
<edition>5</edition>
<publisher-loc><![CDATA[St. Paul. ]]></publisher-loc>
<publisher-name><![CDATA[West Publishing Co.]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B7">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Maarleveld]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Rijnsdorp]]></surname>
<given-names><![CDATA[J. E.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Constraint control of distillation columns]]></article-title>
<source><![CDATA[Automatica]]></source>
<year>1970</year>
<volume>6</volume>
<page-range>51-58</page-range></nlm-citation>
</ref>
<ref id="B8">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Morari]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Arkun]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Stephanoupoulos]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Studies in the synthesis of control structures for chemical processes, Part I]]></article-title>
<source><![CDATA[AIChE J]]></source>
<year>1980</year>
<volume>26</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>220-232</page-range></nlm-citation>
</ref>
<ref id="B9">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Morari]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Stephanoupoulos]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Structural aspects in the synthesis of alternative feasible control schemes, Part II]]></article-title>
<source><![CDATA[AIChE J]]></source>
<year>1980</year>
<volume>26</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>232-246</page-range></nlm-citation>
</ref>
<ref id="B10">
<nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Morud]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
</person-group>
<source><![CDATA[Studies of the dynamics and operation of integrated plants]]></source>
<year>1995</year>
</nlm-citation>
</ref>
<ref id="B11">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Morud]]></surname>
<given-names><![CDATA[J. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Skogestad]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Analysis of instability in an industrial ammonia reactor]]></article-title>
<source><![CDATA[AIChE J]]></source>
<year>1998</year>
<volume>44</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>888-895</page-range></nlm-citation>
</ref>
<ref id="B12">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Rivera]]></surname>
<given-names><![CDATA[D. E.]]></given-names>
</name>
<name>
<surname><![CDATA[Morari]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Skogestad]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Internal model control: 4 PID controller design]]></article-title>
<source><![CDATA[Industrial & Engineering Chemistry Research]]></source>
<year>1986</year>
<volume>25</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>252-265</page-range></nlm-citation>
</ref>
<ref id="B13">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Silverstein]]></surname>
<given-names><![CDATA[J. L.]]></given-names>
</name>
<name>
<surname><![CDATA[Shirmar]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Effect of Design on the Stability and Control of Fixed Bed Reactors with Heat Feedback]]></article-title>
<source><![CDATA[Industrial and Engineering Chemistry Process Design and Development]]></source>
<year>1982</year>
<volume>21</volume>
<page-range>241253</page-range></nlm-citation>
</ref>
<ref id="B14">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Skogestad]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Simple Analytic Rules for Model Reduction and PID Controller Tuning]]></article-title>
<source><![CDATA[Journal of Process Control]]></source>
<year>2003</year>
<volume>13</volume>
<page-range>291309</page-range></nlm-citation>
</ref>
<ref id="B15">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Stephens]]></surname>
<given-names><![CDATA[A. D.]]></given-names>
</name>
<name>
<surname><![CDATA[Richards]]></surname>
<given-names><![CDATA[R. J.]]></given-names>
</name>
</person-group>
<article-title xml:lang="en"><![CDATA[Steady State and Dynamic Analysis of an Ammonia Synthesis Plant]]></article-title>
<source><![CDATA[Automatica]]></source>
<year>1973</year>
<volume>9</volume>
<page-range>65-78</page-range></nlm-citation>
</ref>
</ref-list>
</back>
</article>
