<?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>0187-893X</journal-id>
<journal-title><![CDATA[Educación química]]></journal-title>
<abbrev-journal-title><![CDATA[Educ. quím]]></abbrev-journal-title>
<issn>0187-893X</issn>
<publisher>
<publisher-name><![CDATA[Universidad Nacional Autónoma de México, Facultad de Química]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0187-893X2020000300060</article-id>
<article-id pub-id-type="doi">10.22201/fq.18708404e.2020.3.75416</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Uso didáctico de reactores agitados continuos para la determinación de cinéticas de reacción heterogénea]]></article-title>
<article-title xml:lang="en"><![CDATA[Didactic use of continuous stirred reactors for determining heterogeneous reaction kinetics]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Baz-Rodríguez]]></surname>
<given-names><![CDATA[Sergio Antonio]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Pérez-Aviña]]></surname>
<given-names><![CDATA[Juan Manuel]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Zitlalpopoca-Soriano]]></surname>
<given-names><![CDATA[Ángel Guillermo]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vilchiz-Bravo]]></surname>
<given-names><![CDATA[Luis Enrique]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad Autónoma de Yucatán  ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Mexico</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2020</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2020</year>
</pub-date>
<volume>31</volume>
<numero>3</numero>
<fpage>60</fpage>
<lpage>72</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S0187-893X2020000300060&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S0187-893X2020000300060&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S0187-893X2020000300060&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen Se describen la modelación, la construcción y el uso de un reactor continuo de tanque agitado para la obtención de datos experimentales de rapidez de reacción heterogénea. En primer lugar, mediante análisis de balances de materia se enfatiza cómo la capacidad de este tipo de reactor de operar en estado estacionario es ventajosa para el estudio de sistemas catalíticos heterogéneos. Consecuentemente, se propone una práctica experimental para determinar ecuaciones de rapidez globales a partir de ecuaciones intrínsecas obtenidas por el método de la etapa limitante. Se emplea un reactor continuo de tanque agitado cuya fabricación y operación son sencillos y se describen a detalle. La hidrólisis de sacarosa se implementa como reacción modelo a 60 °C y 1 atm, siendo de fácil monitoreo. La reacción se cataliza con una resina ácida (Amberlite 120 H, capacidad total de intercambio &#8805; 1.80 eq/L). El experimento ilustra una aplicación del método de la etapa limitante para la obtención de ecuaciones de rapidez de reacción global y es una herramienta didáctica para reforzar el aprendizaje práctico en cursos de ingeniería de reacciones heterogéneas.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract The modeling, construction and use of a continuous stirred tank reactor for obtaining experimental data of heterogeneous reaction rates are described. Firstly, by means of analyses of material balances it is emphasized how the capacity of this reactor type for the steadiness operation is advantageous for studying heterogeneous catalytic systems. Consequently, an experimental practice for determining global rate equations from intrinsic equations obtained by the limiting step method is proposed. It was employed a continuous stirred tank reactor whose construction and operation are simple and described in detail. The sucrose hydrolysis is implemented as model reaction, at 60 °C and 1 atm, being of easy monitoring. The reaction is catalyzed by an acid resin (Amberlite 120 H, total exchange capacity &#8805; 1.80 eq/L). The experiment shows an application of the limiting step method for obtaining global reaction rate equations; it is a didactic tool for reinforcing the practical learning in courses of heterogeneous reaction engineering.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[continuo de tanque agitado]]></kwd>
<kwd lng="es"><![CDATA[reacción heterogénea]]></kwd>
<kwd lng="es"><![CDATA[ecuación de rapidez de reacción]]></kwd>
<kwd lng="es"><![CDATA[práctica de laboratorio]]></kwd>
<kwd lng="en"><![CDATA[reactive mass transfer]]></kwd>
<kwd lng="en"><![CDATA[continuous stirred tank reactor]]></kwd>
<kwd lng="en"><![CDATA[heterogeneous reaction]]></kwd>
<kwd lng="en"><![CDATA[reaction rate equation]]></kwd>
</kwd-group>
</article-meta>
</front><back>
<ref-list>
<ref id="B1">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Belfiore]]></surname>
<given-names><![CDATA[L. A.]]></given-names>
</name>
</person-group>
<source><![CDATA[Transport Phenomena for Chemical Reactor Design]]></source>
<year>2003</year>
<publisher-name><![CDATA[John Wiley &amp; Sons, Inc.]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B2">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Carberry]]></surname>
<given-names><![CDATA[J. J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Designing laboratory catalytic reactors]]></article-title>
<source><![CDATA[Industrial and Engineering Chemistry]]></source>
<year>1964</year>
<volume>56</volume>
<numero>11</numero>
<issue>11</issue>
<page-range>39-46</page-range></nlm-citation>
</ref>
<ref id="B3">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Daniels]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Williams]]></surname>
<given-names><![CDATA[J. W.]]></given-names>
</name>
<name>
<surname><![CDATA[Bender]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Alberty]]></surname>
<given-names><![CDATA[R. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Cornwell]]></surname>
<given-names><![CDATA[C. D.]]></given-names>
</name>
</person-group>
<source><![CDATA[Experimental Physical Chemistry]]></source>
<year>1970</year>
<edition>7</edition>
<publisher-name><![CDATA[McGraw-Hill]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B4">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Gilliland]]></surname>
<given-names><![CDATA[E. R.]]></given-names>
</name>
<name>
<surname><![CDATA[Bixler]]></surname>
<given-names><![CDATA[H. J.]]></given-names>
</name>
<name>
<surname><![CDATA[O´Connell]]></surname>
<given-names><![CDATA[J. E.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Catalysis of Sucrose Inversion in Ion- Exchange Resins]]></article-title>
<source><![CDATA[Industrial Engineering Chemistry Fundam]]></source>
<year>1971</year>
<volume>10</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>185-91</page-range></nlm-citation>
</ref>
<ref id="B5">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Heinzerling]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Schrader]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Schanze]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Measurement of enzyme kinetics by use of a blood glucometer: hydrolysis of sucrose and lactose]]></article-title>
<source><![CDATA[Journal of Chemical Education]]></source>
<year>2012</year>
<volume>89</volume>
<page-range>1582-6</page-range></nlm-citation>
</ref>
<ref id="B6">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Hougen]]></surname>
<given-names><![CDATA[O. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Watson]]></surname>
<given-names><![CDATA[K. M.]]></given-names>
</name>
</person-group>
<source><![CDATA[Chemical Process Principles]]></source>
<year>1947</year>
<publisher-name><![CDATA[John Wiley &amp; Sons]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B7">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Khan]]></surname>
<given-names><![CDATA[S. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Rahman]]></surname>
<given-names><![CDATA[K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Inversion of sucrose solution by ion exchange: evaluation of reaction rate and diffusivity]]></article-title>
<source><![CDATA[Chemical Engineering J]]></source>
<year>1996</year>
<volume>61</volume>
<page-range>7-12</page-range></nlm-citation>
</ref>
<ref id="B8">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Kim]]></surname>
<given-names><![CDATA[J. H.]]></given-names>
</name>
<name>
<surname><![CDATA[El-Aasser]]></surname>
<given-names><![CDATA[M. S.]]></given-names>
</name>
<name>
<surname><![CDATA[Klein]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Vanderhoff]]></surname>
<given-names><![CDATA[J. W.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Sulfonated latex particle as acid catalysts for the continuous inversion of sucrose]]></article-title>
<source><![CDATA[Journal of Applied Polymer Science]]></source>
<year>1988</year>
<volume>35</volume>
<page-range>2117-31</page-range></nlm-citation>
</ref>
<ref id="B9">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Mahoney]]></surname>
<given-names><![CDATA[J. A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The use of a gradientless reactor in petroleum reaction engineering studies]]></article-title>
<source><![CDATA[Journal of Catalysis]]></source>
<year>1974</year>
<volume>32</volume>
<page-range>247-53</page-range></nlm-citation>
</ref>
<ref id="B10">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Mendes]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Magalhaes]]></surname>
<given-names><![CDATA[F. D.]]></given-names>
</name>
<name>
<surname><![CDATA[Madeira]]></surname>
<given-names><![CDATA[L. M.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Sucrose inversion: An experiment on heterogeneous catalysis]]></article-title>
<source><![CDATA[International Journal of Engineering Education]]></source>
<year>2003</year>
<volume>19</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>893-901</page-range></nlm-citation>
</ref>
<ref id="B11">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Reed]]></surname>
<given-names><![CDATA[E. W.]]></given-names>
</name>
<name>
<surname><![CDATA[Dranoff]]></surname>
<given-names><![CDATA[J. S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Ion exchange resin catalysis of sucrose inversion in fixed beds]]></article-title>
<source><![CDATA[Industrial and Engineering Chemistry Fundamentals]]></source>
<year>1964</year>
<volume>3</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>304-7</page-range></nlm-citation>
</ref>
<ref id="B12">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Tajbl]]></surname>
<given-names><![CDATA[D. G.]]></given-names>
</name>
<name>
<surname><![CDATA[Simons]]></surname>
<given-names><![CDATA[J. B.]]></given-names>
</name>
<name>
<surname><![CDATA[Carberry]]></surname>
<given-names><![CDATA[J. J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Heterogeneous catalysis in a continuous stirred tank reactor]]></article-title>
<source><![CDATA[Industrial and Engineering Chemistry Fundamentals]]></source>
<year>1966</year>
<volume>5</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>171-5</page-range></nlm-citation>
</ref>
<ref id="B13">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Tiscareño-Lechuga]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
</person-group>
<source><![CDATA[ABC para Comprender Reactores Químicos con Multireacción]]></source>
<year>2008</year>
<publisher-name><![CDATA[Editorial Reverté]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B14">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Vannice]]></surname>
<given-names><![CDATA[M. A.]]></given-names>
</name>
</person-group>
<source><![CDATA[Kinetics of Catalytic Reactions]]></source>
<year>2005</year>
<publisher-name><![CDATA[Bussiness Media, Inc.]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B15">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Weekman]]></surname>
<given-names><![CDATA[V. W.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Laboratory reactors and their limitations]]></article-title>
<source><![CDATA[AIChE Journal]]></source>
<year>1974</year>
<volume>20</volume>
<numero>5</numero>
<issue>5</issue>
<page-range>833-40</page-range></nlm-citation>
</ref>
</ref-list>
</back>
</article>
