<?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>S0122-53832024000100006</article-id>
<article-id pub-id-type="doi">10.29047/01225383.721</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[MODELING PHASE EQUILIBRIA FOR A WATER-CO2-HYDROCARBON MIXTURE USING CPA EQUATION OF STATE IN CO2 INJECTION EOR-STORAGE PROCESSES: A COLOMBIAN CASE STUDY]]></article-title>
<article-title xml:lang="es"><![CDATA[MODELAMIENTO DEL EQUILIBRIO DE FASES PARA MEZCLA AGUA-CO2-HIDROCARBONO UTILIZANDO LA ECUACIÓN DE ESTADO CPA EN PROCESOS DE EOR-ALMACENAMIENTO POR INYECCIÓN DE CO2: UN ESTUDIO DE CASO COLOMBIANO]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Aristizabal]]></surname>
<given-names><![CDATA[J. D.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Cundar]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Guerrero]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Aguirre]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Pasos]]></surname>
<given-names><![CDATA[JA]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Moncayo-Riascos]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Ruiz]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Benjumea]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Agudelo]]></surname>
<given-names><![CDATA[W.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Osorio]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Meridian Consulting Ltda  ]]></institution>
<addr-line><![CDATA[Bogota ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Ecopetrol S.A  ]]></institution>
<addr-line><![CDATA[Bogotá ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af3">
<institution><![CDATA[,SGS Consulting  ]]></institution>
<addr-line><![CDATA[Bogotá ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af4">
<institution><![CDATA[,Universidad Nacional de Colombia  ]]></institution>
<addr-line><![CDATA[Medellín ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af5">
<institution><![CDATA[,Ecopetrol S.A.  ]]></institution>
<addr-line><![CDATA[Piedecuesta Santander]]></addr-line>
<country>Colombia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2024</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2024</year>
</pub-date>
<volume>14</volume>
<numero>1</numero>
<fpage>61</fpage>
<lpage>76</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S0122-53832024000100006&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S0122-53832024000100006&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S0122-53832024000100006&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[ABSTRACT Currently, it is necessary to reduce CO2 emissions into the atmosphere. The oil industry in Colombia can contribute through CO2 injection processes in depleted fields. To achieve this, it is essential to know about the physicochemical interaction of CO2with reservoir fluids. To integrate CO2, water and hydrocarbon phases, advanced models are necessary to capture the phenomenology of thermodynamic equilibrium. The CPA (Cubic-Plus-Association) equation of state adds an associative term to model the interaction of water with the hydrocarbon and CO2 phase. In this work, the CO2 injection process is thermodynamically modelled in a case study of a depleted reservoir in Colombia. There is a compositional fluid with a gradient of PVT properties in a vertical relief of 10,000 ft, at a depletion condition of 2,000 psi @ 15,374 ft and an oil-water contact (OWC) at 17,000 ft. CO2 injections between 10 and 80 mol% were conducted, and through the CPA equation of state, the swelling conditions of the crude oil, the solubility of CO2 in the formation water, and the pressurization of the system were evaluated. The associative parameters of the equation were taken from literature and estimated through molecular dynamics simulations of water-CO2-Hydrocarbon interaction. Scheme 4C_1, at CO2 injection conditions greater than 40%, predicts CO2 solubility values greater than 2000 scf/bbl compared to the other literature schemes and experimental data. Scheme 2B_2 presents inconsistencies in saturation pressure calculations at high CO2 injection contents since at 60% it reports a value of 2800 psia and at 80% a value of 2600 psia. This behavior is opposite to that reported in literature. Therefore, association schemes 4C_1 and 2B_2 presented thermodynamic problems for the calculation of properties such solubilities and saturation pressures. This thermodynamic modelling with an advanced equation of state and use of molecular dynamics simulations enabled us to simulate different CO2 injection scenarios in a compositional fluid. This type of studies is key to conduct successful CO2 injection processes focused on enhanced recovery (EOR) and CO2 storage in the porous medium in a depleted compositional reservoir in Colombia.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[RESUMEN En la actualidad es necesario reducir las emisiones de CO2 en la atmósfera. La industria petrolera en Colombia puede contribuir mediante procesos de inyección de CO2 en yacimientos depletados. Para ello, es fundamental tener un conocimiento de las interacciones fisicoquímicas del CO2 con fluidos de yacimiento. Para integrar las 3 fases CO2, agua e hidrocarburo se requieren modelos avanzados que capturen Ta fenomenología del equilibrio termodinâmico. La ecuación de estado CPA (cubic-plus-association), es una ecuación que adiciona de un término asociativo para modelar la interacción del agua con fase hidrocarburo y CO2. En este trabajo se modela termodinámicamente el proceso de inyección de CO2 en un caso de estudio de un yacimiento depletado colombiano. Se cuenta con un fluido composicional con un gradiente de propiedades PVT en un relieve vertical de 10000 ft a una condición de depletamiento de 2000 psia @ 15374 ft y un contacto agua-petróleo (OWC) a 17000 ft. Se realizaron inyecciones de CO2 entre el 10 y 80% molar, y a través de ecuación de estado CPA, se evaluaron las condiciones de hinchamiento del crudo, solubilidad del CO2 en el agua de formación y presurización del sistema. Los parámetros asociativos de la ecuación fueron tomados de literatura y estimados a través de simulaciones de dinámica molecular de las interacciones agua-CO2-Hidrocarburo, mediante la descripción simplificada de un crudo vivo con contenido de asfaltenos de 1% y metano de 50% mol a 6500 psia y 255 °F. El esquema 4C_1, en condiciones de inyección de CO2 superiores al 40%, predice valores de solubilidad de CO2 superiores a 2000 scf/ bbl en comparación con los otros esquemas de literatura y los datos experimentales. El esquema 2B_2 presenta inconsistencias en los cálculos de presión de saturación a altos contenidos de inyección de CO2, ya que a 60% reporta un valor de 2800 psia y a 80% un valor de 2600 psia. Este comportamiento es opuesto al reportado en la literatura. Por lo tanto, los esquemas de asociación 4C_1 y 2B_2 presentaron problemas termodinámicos para el cálculo de propiedades como solubilidades y presiones de saturación. Este modelamiento termodinâmico con ecuación de estado avanzada y uso de simulaciones de dinámica molecular, permitió simular diferentes escenarios de inyección de CO2 en un fluido composicional. El desarrollo de este tipo de estudios es clave para llevar a cabo procesos de inyección de CO2 exitosos enfocados en recobro mejorado (EOR) y almacenamiento de CO2 en el medio poroso en un yacimiento composicional depletado colombiano.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[CO2 Injection]]></kwd>
<kwd lng="en"><![CDATA[Depleted Reservoir]]></kwd>
<kwd lng="en"><![CDATA[Compositional Gradient]]></kwd>
<kwd lng="en"><![CDATA[Thermodynamic Equilibrium]]></kwd>
<kwd lng="en"><![CDATA[CPA (Cubic-Plus-Association)]]></kwd>
<kwd lng="en"><![CDATA[Equation of State (EoS)]]></kwd>
<kwd lng="es"><![CDATA[Inyección de CO2]]></kwd>
<kwd lng="es"><![CDATA[Yacimiento Depletado]]></kwd>
<kwd lng="es"><![CDATA[Gradiente Composicional]]></kwd>
<kwd lng="es"><![CDATA[Equilibrio Termodinâmico]]></kwd>
<kwd lng="es"><![CDATA[Ecuación de Estado (EoS) CPA (Cubic-Plus-Association)]]></kwd>
</kwd-group>
</article-meta>
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