<?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>S1665-27382007000300008</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Análisis de problemas de transporte de masa y reacción mediante funciones de green]]></article-title>
<article-title xml:lang="en"><![CDATA[Analysis of mass transport and reaction problems using green's functions]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Valdés-Parada]]></surname>
<given-names><![CDATA[F. J.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Alvarez-Ramírez]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Ochoa-Tapia]]></surname>
<given-names><![CDATA[J. A.]]></given-names>
</name>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universidad Autónoma Metropolitana-Iztapalapa Departamento de Ingeniería de Procesos e Hidráulica ]]></institution>
<addr-line><![CDATA[México D.F.]]></addr-line>
<country>México</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>12</month>
<year>2007</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>12</month>
<year>2007</year>
</pub-date>
<volume>6</volume>
<numero>3</numero>
<fpage>283</fpage>
<lpage>294</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382007000300008&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382007000300008&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382007000300008&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Se presenta una metodología para resolver problemas típicos de transferencia de masa y reacción en ingeniería de las reacciones químicas en términos de funciones de Green. La idea fundamental consiste en invertir analíticamente un operador diferencial a partir de la solución de un problema de valor a la frontera asociado al problema original de transporte y reacción. La variable dependiente queda expresada en función de la solución de dicho problema asociado que es la función de Green. Entre las ventajas que presenta esta metodología son el suavizado de los errores de redondeo así como la incorporación en forma exacta de las condiciones de frontera. Un requisito indispensable para la aplicación de la metodología es que el operador diferencial sea autoadjunto. Para ilustrar la habilidad del método, se estudian problemas de difusión y reacción en una partícula catalítica involucrando cinéticas tanto lineales como no lineales; además se analiza el efecto de las resistencias externas a la transferencia de masa y se discute la aplicación a problemas de transporte no isotérmico, convectivo, en estrado transitorio y multicomponentes. Las predicciones se comparan con las que resultan de la solución numérica mediante diferencias finitas. El análisis se lleva a cabo en términos de parámetros tanto numéricos (tiempo de cómputo, tamaño de malla) como de transporte (módulo de Thiele, número de Biot).]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[A methodology to solve typical problems of mass transfer and chemical reaction engineering in terms of Green's functions is presented. The fundamental idea consists on analytically inverting a differential operator by means of the solution of a boundary value problem associated to the original transport and reaction problem. The dependent variable is expressed then as function of the solution of such associated problem, which is the Green's function. Among the advantages that this methodology presents are the smoothing of round-off errors as well as the exact incorporation of boundary conditions. A mandatory requirement for the application of this methodology is that the differential operator must me self-adjoint. To illustrate the potential of the method, diffusion and reaction problems are studied in a catalytic particle involving both linear and non-linear reaction kinetics; in addition, the effect of the external mass transfer resistances is analyzed and the application to non-isothermal, convective, transient and multicomponent problems is discussed. The predictions are compared with those resulting from the numeric solution using finite differences. The analysis is carried out in terms of both numeric (computer time, mesh size) and transport (Thiele modulus, Biot number) parameters.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[transporte de masa y reacción]]></kwd>
<kwd lng="es"><![CDATA[función de Green]]></kwd>
<kwd lng="es"><![CDATA[diferencias finitas]]></kwd>
<kwd lng="es"><![CDATA[métodos numéricos]]></kwd>
<kwd lng="en"><![CDATA[mass transport and reaction]]></kwd>
<kwd lng="en"><![CDATA[Green's function]]></kwd>
<kwd lng="en"><![CDATA[finite differences]]></kwd>
<kwd lng="en"><![CDATA[numeric methods]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="justify"><font face="verdana" size="4">Fen&oacute;menos de transporte </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 de problemas de transporte de masa y reacci&oacute;n mediante funciones de green</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="3"><b>Analysis of mass transport and reaction problems using green's functions</b></font></p>     <p align="center"><font face="verdana" size="2">&nbsp;</font></p>     <p align="center"><font face="verdana" size="2"><b>F. J. Vald&eacute;s&#150;Parada*, J. Alvarez&#150;Ram&iacute;rez y J. A. Ochoa&#150;Tapia</b></font></p>     <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>     <p align="justify"><font face="verdana" size="2"><i>Departamento de Ingenier&iacute;a de Procesos e Hidr&aacute;ulica, Universidad Aut&oacute;noma Metropolitana&#150;Iztapalapa, Apartado Postal 55&#150;534, 09340 M&eacute;xico D.F., M&eacute;xico. <i>* Autor para la correspondencia: E&#150;mail: </i></i><a href="mailto:iqfv@xanum.uam.mx">iqfv@xanum.uam.mx</a><i><i> Tel. 58 04 46 48 ext 219, Fax 58 04 49 00</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 10 de Septiembre 2007    <br> Aceptado 31 de Octubre 2007</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 presenta una metodolog&iacute;a para resolver problemas t&iacute;picos de transferencia de masa y reacci&oacute;n en ingenier&iacute;a de las reacciones qu&iacute;micas en t&eacute;rminos de funciones de Green. La idea fundamental consiste en invertir anal&iacute;ticamente un operador diferencial a partir de la soluci&oacute;n de un problema de valor a la frontera asociado al problema original de transporte y reacci&oacute;n. La variable dependiente queda expresada en funci&oacute;n de la soluci&oacute;n de dicho problema asociado que es la funci&oacute;n de Green. Entre las ventajas que presenta esta metodolog&iacute;a son el suavizado de los errores de redondeo as&iacute; como la incorporaci&oacute;n en forma exacta de las condiciones de frontera. Un requisito indispensable para la aplicaci&oacute;n de la metodolog&iacute;a es que el operador diferencial sea autoadjunto. Para ilustrar la habilidad del m&eacute;todo, se estudian problemas de difusi&oacute;n y reacci&oacute;n en una part&iacute;cula catal&iacute;tica involucrando cin&eacute;ticas tanto lineales como no lineales; adem&aacute;s se analiza el efecto de las resistencias externas a la transferencia de masa y se discute la aplicaci&oacute;n a problemas de transporte no isot&eacute;rmico, convectivo, en estrado transitorio y multicomponentes. Las predicciones se comparan con las que resultan de la soluci&oacute;n num&eacute;rica mediante diferencias finitas. El an&aacute;lisis se lleva a cabo en t&eacute;rminos de par&aacute;metros tanto num&eacute;ricos (tiempo de c&oacute;mputo, tama&ntilde;o de malla) como de transporte (m&oacute;dulo de Thiele, n&uacute;mero de Biot).</font></p>     <p align="justify"><font face="verdana" size="2"><b>Palabras clave: </b>transporte de masa y reacci&oacute;n, funci&oacute;n de Green, diferencias finitas, m&eacute;todos num&eacute;ricos.</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">A methodology to solve typical problems of mass transfer and chemical reaction engineering in terms of Green's functions is presented. The fundamental idea consists on analytically inverting a differential operator by means of the solution of a boundary value problem associated to the original transport and reaction problem. The dependent variable is expressed then as function of the solution of such associated problem, which is the Green's function. Among the advantages that this methodology presents are the smoothing of round&#150;off errors as well as the exact incorporation of boundary conditions. A mandatory requirement for the application of this methodology is that the differential operator must me self&#150;adjoint. To illustrate the potential of the method, diffusion and reaction problems are studied in a catalytic particle involving both linear and non&#150;linear reaction kinetics; in addition, the effect of the external mass transfer resistances is analyzed and the application to non&#150;isothermal, convective, transient and multicomponent problems is discussed. The predictions are compared with those resulting from the numeric solution using finite differences. The analysis is carried out in terms of both numeric (computer time, mesh size) and transport (Thiele modulus, Biot number) parameters.</font></p>     <p align="justify"><font face="verdana" size="2"><b>Keywords: </b>mass transport and reaction, Green's function, finite differences, numeric methods.</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/v6n3/v6n3a8.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">FJVP desea agradecer al Consejo Nacional de Ciencia y Tecnolog&iacute;a (CONACyT) por la beca de posdoctorado otorgada a trav&eacute;s del convenio 49705&#150;Y.</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., Vald&eacute;s&#150;Parada, F.J., Alvarez, J., Ochoa&#150;Tapia, J.A. (2007). A Green's function formulation for finite difference schemes. <i>Chemical Engineering Science 62, </i>3083&#150;3091.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531243&pid=S1665-2738200700030000800001&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">Amundson, N.R., Schilson, R.E. (1961). Intraparticle reaction and conduction in porous catalysts&#150;I. Single reactions. <i>Chemical Engineering Science 13, </i>226&#150;236.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531245&pid=S1665-2738200700030000800002&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">Aris, R. (1975). <i>The Mathematical Theory of Diffusion and Reaction in Permeable Catalysts, </i>Vol. I. Clarendon Press, Oxford.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531247&pid=S1665-2738200700030000800003&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">Axelsson, O., Gololobov S.V. 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Necessary Conditions and Iterative Technique. <i>Industrial and Engineering Fundamentals 4, </i>7&#150;16.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531251&pid=S1665-2738200700030000800005&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">Denn, M.M., Aris, R. (1965b). Green's functions and optimal systems. 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(1969). An integral equation method for evaluating the effects of film and pore diffusion of heat and mass on reaction rates in porous catalyst particles. <i>AIChE Journal 15, </i>128&#150;131.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531261&pid=S1665-2738200700030000800010&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">Haberman, R. (2004). <i>Applied Partial Differential </i><i>Equations, </i>4<sup>th</sup> edition, Prentice Hall, USA.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531263&pid=S1665-2738200700030000800011&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">Mishra, M., Peiperl L., Reuven Y., Rabitz H., Yetter R.A., Smooke M.D. (1991). Use of Green's functions for the analysis of dynamic couplings: Some examples from chemical kinetics and quantum dynamics. <i>Journal of Physical Chemistry 95, </i>3109&#150;3118.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531265&pid=S1665-2738200700030000800012&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">Mishra M., Yetter R., Reuven Y., Rabitz H., Smooke M.D. (1994). On the role of transport in the combustion kinetics of a steady&#150;state premixed laminar CO + H<sub>2</sub>+ O<sub>2</sub> flame. <i>International Journal of Chemical Kinetics </i><i>26, </i>437&#150;453.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531267&pid=S1665-2738200700030000800013&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">Mukkavilli S., Tavlarides, L.T. &amp; Wittmann, Ch.V. (1987a). Integral method of analysis for chemical reaction in a nonisothermal finite cylindrical catalyst pellet&#150;I. Dirichlet problem. <i>Chemical Engineering Science 42, </i>27&#150;33.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531269&pid=S1665-2738200700030000800014&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">Mukkavilli S., Tavlarides, L.T. &amp; Wittmann, Ch.V. (1987b) Integral method of analysis for chemical reaction in a nonisothermal finite cylindrical catalyst pellet&#150;II. 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On Green's function methods to solve nonlinear reaction&#150;diffusion systems. <i>Computers and Chemical Engineering, en prensa.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=8531273&pid=S1665-2738200700030000800016&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></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"><a href="/img/revistas/rmiq/v6n3/html/a8a1.htm" target="_blank"><b>Ap&eacute;ndice</b></a></font></p>      ]]></body><back>
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