<?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>0122-5383</journal-id>
<journal-title><![CDATA[CT&F - Ciencia, Tecnología y Futuro]]></journal-title>
<abbrev-journal-title><![CDATA[C.T.F Cienc. Tecnol. Futuro]]></abbrev-journal-title>
<issn>0122-5383</issn>
<publisher>
<publisher-name><![CDATA[Instituto Colombiano del Petróleo (ICP) - ECOPETROL S.A.]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0122-53832022000100095</article-id>
<article-id pub-id-type="doi">10.29047/01225383.402</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[SIMULATION TOOL FOR THE ANALYSIS OF IN-SITU COMBUSTION EXPERIMENTS THAT CONSIDERS COMPLEX KINETIC SCHEMES AND DETAILED MASS TRANSFER-THEORETICAL ANALYSIS OF THE GAS PHASE CO OXIDATION REACTION]]></article-title>
<article-title xml:lang="es"><![CDATA[HERRAMIENTA DE SIMULACIÓN PARA EL ANÁLISIS DE EXPERIMENTOS DE COMBUSTIÓN IN-SITU QUE PERMITE EL ANÁLISIS DE SISTEMAS DE REACCIÓN COMPLEJOS Y TRANSFERENCIA DE MASA - ANÁLISIS TEÓRICO DE LA REACCIÓN DE OXIDACIÓN DE CO EN LA FASE GASEOSA]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Hincapié]]></surname>
<given-names><![CDATA[Juan Felipe]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[López]]></surname>
<given-names><![CDATA[Sebastian]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Molina]]></surname>
<given-names><![CDATA[Alejandro]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad Nacional de Colombia  ]]></institution>
<addr-line><![CDATA[Medellín ]]></addr-line>
<country>Colombia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2022</year>
</pub-date>
<volume>12</volume>
<numero>1</numero>
<fpage>95</fpage>
<lpage>106</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S0122-53832022000100095&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S0122-53832022000100095&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S0122-53832022000100095&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[ABSTRACT A simulation tool was designed for analyzing various experimental setups that include the ability to model detailed chemical reaction schemes for in-situ combustion (ISC) analysis. The simulation tool was illustrated with a theoretical example to the extent of CO oxidation in a gaseous phase takes place during ISC. The models in the simulation tool are based on fundamental conservation laws, physical correlations for porous media properties, and property databases available in literature. Emphasis is made on the analysis of chemical reactions in the gas phase, a characteristic that may be useful when temperatures are above 700°C and oxygen, unburned hydrocarbons, and CO coexist. The three modules of the simulation tool: (i) Kinetic cell, (ii) One-dimensional reactor, and (iii) Combustion tube, can be used to represent in detail the processes taking place in the typical laboratory-scale equipment used to characterize ISC. Tools for the analysis of transport phenomena and multiphase reactions, present in all three models, can support the process of finding chemical kinetic parameters for an easier calculation of device-independent kinetic constants. Four applications have the simulator scope: (i) Analysis of reactions in the gas phase, (ii) Axial gradients in a kinetic cell, (iii) Pressure build-up in a combustion tube, and (iv) Ignition in a combustion tube. These examples highlight the importance that homogeneous reactions may have in these systems and the existence, under certain conditions, of concentration gradients that are normally neglected, and can affect the interpretation of ISC experiments.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[RESUMEN Se desarrolló una herramienta de simulación, diseñada para el análisis de diferentes montajes experimentales que incluye la capacidad de modelar esquemas detallados de reacciones químicas para el análisis de la combustión in-situ (CIS). La herramienta de simulación se ilustró con un ejemplo teórico de la medida en que se produce la oxidación de CO en fase gaseosa durante ISC. Los modelos en el simulador están basados en las leyes fundamentales de conservación, correlaciones físicas para propiedades de medios porosos y bases de datos de propiedades disponibles en literatura libre. Se hace énfasis en el análisis de reacciones químicas en la fase gaseosa, una característica que puede ser útil en casos donde la temperatura exceda los 700°C y, además; el oxígeno, hidrocarburos sin quemar y CO coexistan. Los tres módulos del simulador: (i) Celda cinética, (ii) Reactor unidimensional (iii) Tubo de combustión, pueden ser usados para representar en detalle los procesos que toman lugar en los equipos típicos a escala de laboratorio, usados para caracterizas CIS. Herramientas para el análisis de los fenómenos de transporte y reacciones multifásicas, presentes en los tres modelos, pueden soportar el proceso de encontrar parámetros de cinética química, facilitando el cálculo de parámetros de cinética química independientes del equipo. Cuatro aplicaciones demuestran el alcance del simulador: (i) Análisis de reacciones en fase gaseosa, (ii) Gradientes axiales en una celda cinética, (iii) El desarrollo de presión en un tubo de combustión, y (iv) Ignición en un tubo de combustión, Los ejemplos destacan particularmente la importancia que tienen las reacciones homogéneas y la existencia, bajo ciertas condiciones, de gradientes de concentración que normalmente se desprecian pero pueden afectar la interpretación de experimentos en CIS]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[In situ combustion]]></kwd>
<kwd lng="en"><![CDATA[Reactive porous media]]></kwd>
<kwd lng="en"><![CDATA[Enhanced oil recovery]]></kwd>
<kwd lng="en"><![CDATA[Heavy oil]]></kwd>
<kwd lng="en"><![CDATA[Multiphase flow]]></kwd>
<kwd lng="en"><![CDATA[Simulation Tool]]></kwd>
<kwd lng="es"><![CDATA[Combustión in-situ]]></kwd>
<kwd lng="es"><![CDATA[Medio poroso reactivo]]></kwd>
<kwd lng="es"><![CDATA[Recobro de crudo mejorado]]></kwd>
<kwd lng="es"><![CDATA[Crudo pesado]]></kwd>
<kwd lng="es"><![CDATA[Flujo multifásico]]></kwd>
<kwd lng="es"><![CDATA[Simulador]]></kwd>
</kwd-group>
</article-meta>
</front><back>
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