<?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>S1665-27382016000100193</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Reactive McCabe-Thiele: Short cut method including reactive vapor - liquid efficiency]]></article-title>
<article-title xml:lang="es"><![CDATA[McCabe-Thiele reactivo: Método corto incluyendo eficiencia vapor líquido reactivo]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Flores-Estrella]]></surname>
<given-names><![CDATA[R.A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Iglesias-Silva]]></surname>
<given-names><![CDATA[G.A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,IPICyT División de Matemáticas Aplicadas ]]></institution>
<addr-line><![CDATA[San Luis Potosí S.L.P.]]></addr-line>
<country>México</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Instituto Tecnológico de Celaya Departamento de Ingeniería Química ]]></institution>
<addr-line><![CDATA[Celaya Gto.]]></addr-line>
<country>Mexico</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2016</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2016</year>
</pub-date>
<volume>15</volume>
<numero>1</numero>
<fpage>193</fpage>
<lpage>207</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1665-27382016000100193&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1665-27382016000100193&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1665-27382016000100193&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract: A graphic McCabe-Thiele method is developed for application to fully reactive column configuration. The extended method takes in to account several aspects as classic McCabe-Thiele method under transformed reaction-invariant composition variables as: minimum number of reactive theoretical stages, number of reactive theoretical stages, minimum reflux ratio, feed tray location, to and / or bottom flow. Reaction equilibrium is assumed on each stage, vapor-liquid equilibrium is assumed on all stages and is also considered a reactive Murphree vapor tray efficiency. The methodology is illustrated in two ideal reactive systems. The results of the reactive McCabe-Thiele method agree with those obtained using a rigorous method in commercial simulator AspenONE Aspen Plus (Radfrac module).]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen: Un método gráfico basado en el método McCabe-Thiele es desarrollado para la aplicación del diseño de columnas reactivas. El método toma en cuenta varios aspectos del método clásico McCabe-Thiele bajo variables reactivas transformadas: número mínimo de etapas reactivas teóricas, número de etapas reactivas, reflujo mínimo, ubicación del plato de alimentación flujos de destilado y fondos. Se asume: equilibrio reactivo para cada etapa, equilibrio vapor líquido y es considerado una eficiencia reactiva Murphee para la fase de vapor. La metodología es ilustrada en dos sistemas reativos ideales. Los resultados del método McCabe-Thiele reactivo concuerdan con los obtenidos usando un método riguroso en un simulador comercial AspenONE Aspen Plus (Radfrac module).]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[reactive McCabe-Thiele]]></kwd>
<kwd lng="en"><![CDATA[reactive distillation]]></kwd>
<kwd lng="en"><![CDATA[transformed composition]]></kwd>
<kwd lng="en"><![CDATA[reactive Murphree efficiency]]></kwd>
<kwd lng="en"><![CDATA[reactive system]]></kwd>
<kwd lng="es"><![CDATA[McCabe-Thiele reactivo]]></kwd>
<kwd lng="es"><![CDATA[destilación reactiva]]></kwd>
<kwd lng="es"><![CDATA[composiciones transformadas]]></kwd>
<kwd lng="es"><![CDATA[eficiencia reactiva Murphee]]></kwd>
<kwd lng="es"><![CDATA[sistema reactivo]]></kwd>
</kwd-group>
</article-meta>
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