<?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>1900-3803</journal-id>
<journal-title><![CDATA[Entramado]]></journal-title>
<abbrev-journal-title><![CDATA[Entramado]]></abbrev-journal-title>
<issn>1900-3803</issn>
<publisher>
<publisher-name><![CDATA[Universidad Libre de Cali]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1900-38032019000100312</article-id>
<article-id pub-id-type="doi">10.18041/1900-3803/entramado.1.5433</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Revisión del proceso de separación de fases del gas natural a alta presión en la industria Oil&amp;Gas]]></article-title>
<article-title xml:lang="en"><![CDATA[Review of the natural gas phases separation process at high pressure in the Oil&amp;Gas industry]]></article-title>
<article-title xml:lang="pt"><![CDATA[Revisão do processo de separação de fases do gás natural para alta pressão na indústria de Oil&amp;Gas]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Prieto-Jiménez]]></surname>
<given-names><![CDATA[Natalia]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[González-Silva]]></surname>
<given-names><![CDATA[Germán]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Chaves-Guerrero]]></surname>
<given-names><![CDATA[Arlex]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad Industrial de Santander UIS  ]]></institution>
<addr-line><![CDATA[Bucaramanga ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad Industrial de Santander UIS  ]]></institution>
<addr-line><![CDATA[Bucaramanga ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af3">
<institution><![CDATA[,Universidad Industrial de Santander UIS  ]]></institution>
<addr-line><![CDATA[Bucaramanga ]]></addr-line>
<country>Colombia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2019</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2019</year>
</pub-date>
<volume>15</volume>
<numero>1</numero>
<fpage>312</fpage>
<lpage>329</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S1900-38032019000100312&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S1900-38032019000100312&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S1900-38032019000100312&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen La separación física de líquidos y gases es una de las operaciones de producción, procesamiento y tratamiento en la industria petrolera, necesaria para prevenir daños en equipos rotativos, evitar corrosión en tuberías y cumplir con las especificaciones de calidad del gas natural para uso doméstico. Cuando la presión de operación aumenta, la diferencia de densidades entre las fases disminuye, lo cual dificulta el proceso de separación. Se realiza la revisión del estado del arte, desde los años 90 hasta el presente, de las diferentes metodologías para separar las fases líquida y gaseosa del gas natural, así como las variables de diseño con aplicación a sistemas que operan a alta presión; prestando especial énfasis en los avances encontrados utilizando Dinámica de Fluidos Computacional. Los resultados muestran que, aunque los separadores centrífugos y los separadores supersónicos son más compactos y de fácil mantenimiento comparados con los separadores gravitacionales, éstos últimos continúan siendo la estrategia más favorable cuando se combinan alta presión y baja cantidad de líquido (menos del 4% vol), como es el caso del gas natural. Conclusión adjudicada, en parte, a la falta de estudios experimentales/numéricos que involucren al gas natural en equipos alternativos al separador gravitacional]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract The Physical separation of liquids and gases is one of the main operations of production, processing and treatment in the oil industry; it is necessary to prevent damage to rotating equipment, to avoid corrosion in pipes and to achieve with the natural gas quality specifications for domestic use. When the operating pressure increases, the density difference between the phases decreases, which makes the separation process difficult or in some cases impossible. In this work, the state of the art of the different methodologies to separate the liquid and gaseous phases of natural gas is reviewed , as well as the design variables applied to systems that operate at high pressure from the 90's to the present; with special emphasis on the advances found using Computational Fluid Dynamics. The results show that, although both centrifugal and supersonic separators are more compact and easy to maintain compared to gravitational separators, gravitational separators remain the most favorable strategy when combining high pressure and low liquid load (less than 4%vol), as is the case of natural gas. Conclusion awarded, in part, to the lack of experimental/numerical studies involving natural gas in alternative equipment to the gravitational separator]]></p></abstract>
<abstract abstract-type="short" xml:lang="pt"><p><![CDATA[Resumo A separação física de líquidos e gases é uma das principais operações de produção, processamento e tratamento na indústria do petróleo, necessária para evitar danos ao equipamento rotativo, para evitar a corrosão nos tubos e para cumprir as especificações de qualidade do gás natural para uso doméstico. Quando a pressão de operação aumenta, a diferença de densidade entre as fases diminui, o que torna o processo de separação difícil ou, em alguns casos, impossível. Neste trabalho, é realizada a avaliação do estado da arte de diferentes metodologias para separar as fases líquida e gasosa do gás natural e as variáveis de design com aplicação para sistemas que operam a alta pressão a partir dos anos 90 até a data atual; com ênfase especial nos avanços encontrados usando a Dinâmica dos Fluidos Computacional. Os resultados mostram que, embora ambos os separadores centrífugos e supersónicos são mais compactos e de fácil manutenção comparado com separadores gravitacionais, o último continua a ser a estratégia favorecida quando a alta pressão e de baixa quantidade de líquido são combinados (menos de 4% vol), como é o caso do gás natural; Conclusão concedida, em parte, à falta de estudos experimentais/numéricos envolvendo gás natural em equipamentos alternativos ao separador gravitacional]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[Separador trifásico]]></kwd>
<kwd lng="es"><![CDATA[gas natural]]></kwd>
<kwd lng="es"><![CDATA[asentamiento de gota]]></kwd>
<kwd lng="es"><![CDATA[diseño]]></kwd>
<kwd lng="es"><![CDATA[CFD]]></kwd>
<kwd lng="en"><![CDATA[Three-phase separator natural gas]]></kwd>
<kwd lng="en"><![CDATA[settling theory design]]></kwd>
<kwd lng="en"><![CDATA[CFD]]></kwd>
<kwd lng="pt"><![CDATA[Separador trifásico]]></kwd>
<kwd lng="pt"><![CDATA[gás natural]]></kwd>
<kwd lng="pt"><![CDATA[assentamento de gotas]]></kwd>
<kwd lng="pt"><![CDATA[design]]></kwd>
<kwd lng="pt"><![CDATA[CFD]]></kwd>
</kwd-group>
</article-meta>
</front><back>
<ref-list>
<ref id="B1">
<label>1</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[ABERNATHY]]></surname>
<given-names><![CDATA[W. J]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Chapter Gravity Settlers, Design]]></article-title>
<source><![CDATA[Unit Operation Handbook]]></source>
<year>1993</year>
</nlm-citation>
</ref>
<ref id="B2">
<label>2</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[ARNOLD]]></surname>
<given-names><![CDATA[Ken]]></given-names>
</name>
<name>
<surname><![CDATA[STEWART]]></surname>
<given-names><![CDATA[Maurice]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Surface Production Operations-Design of Oil Handling Systems and Facilities]]></article-title>
<source><![CDATA[Volume 1: Gulf Professional Publishing]]></source>
<year>2008</year>
</nlm-citation>
</ref>
<ref id="B3">
<label>3</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[AUSTRHEIM]]></surname>
<given-names><![CDATA[Trond]]></given-names>
</name>
<name>
<surname><![CDATA[GJERTSEN]]></surname>
<given-names><![CDATA[Lars H]]></given-names>
</name>
<name>
<surname><![CDATA[HOFFMANN]]></surname>
<given-names><![CDATA[Alex C]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Experimental investigation of the performance of a large-scale scrubber operating at elevated pressure on live natural gas]]></article-title>
<source><![CDATA[Fuel]]></source>
<year>2008</year>
<volume>87</volume>
<numero>7</numero>
<issue>7</issue>
<page-range>1281-8</page-range></nlm-citation>
</ref>
<ref id="B4">
<label>4</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[BAHADORI]]></surname>
<given-names><![CDATA[Alireza]]></given-names>
</name>
</person-group>
<source><![CDATA[Natural gas processing: technology and engineering design: Gulf Professional Publishing]]></source>
<year>2014</year>
</nlm-citation>
</ref>
<ref id="B5">
<label>5</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[BLEZARD]]></surname>
<given-names><![CDATA[R. G.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[chapter Production Engineering]]></article-title>
<source><![CDATA[Modern Petroleum Technology: Institution of Petroleum]]></source>
<year>2000</year>
</nlm-citation>
</ref>
<ref id="B6">
<label>6</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[BOTHAMLEY]]></surname>
<given-names><![CDATA[Mark]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Gas/liquids separators-Quantifying separation performance-part 2]]></article-title>
<source><![CDATA[Oil and Gas Facilities]]></source>
<year>2013</year>
<volume>2</volume>
<numero>05</numero>
<issue>05</issue>
<page-range>35-47</page-range></nlm-citation>
</ref>
<ref id="B7">
<label>7</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[BRIGADEAU]]></surname>
<given-names><![CDATA[Alexandre H. M]]></given-names>
</name>
</person-group>
<source><![CDATA[Modeling and Numerical Investigation of High Pressure Gas-Liquid Separation: Fakultet for ingeniørvitenskap og teknologi]]></source>
<year>2007</year>
</nlm-citation>
</ref>
<ref id="B8">
<label>8</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[BURKHOLZ]]></surname>
<given-names><![CDATA[Armin]]></given-names>
</name>
</person-group>
<source><![CDATA[Droplet Separation]]></source>
<year>1989</year>
<publisher-loc><![CDATA[Weinheim (Federal Republic of Germany): New York, NY (USA) ]]></publisher-loc>
<publisher-name><![CDATA[Vch Pub]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B9">
<label>9</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[BYMASTER]]></surname>
<given-names><![CDATA[Adam]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[High pressure gas-liquid separation: an experimental study on separator performance of natural gas streams at elevated pressures.]]></article-title>
<source><![CDATA[Offshore Technology Conference]]></source>
<year>2011</year>
</nlm-citation>
</ref>
<ref id="B10">
<label>10</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[CAO]]></surname>
<given-names><![CDATA[Xuewen]]></given-names>
</name>
<name>
<surname><![CDATA[BIAN]]></surname>
<given-names><![CDATA[Jiang]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Supersonic separation technology for natural gas processing: A review]]></article-title>
<source><![CDATA[Chemical Engineering and Processing-Process Intensification]]></source>
<year>2019</year>
</nlm-citation>
</ref>
<ref id="B11">
<label>11</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[CHEN]]></surname>
<given-names><![CDATA[Bin]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Simulating vapor-liquid nucleation of n-alkanes]]></article-title>
<source><![CDATA[The Journal of chemical physics]]></source>
<year>2002</year>
<volume>116</volume>
<numero>10</numero>
<issue>10</issue>
<page-range>4317-29</page-range></nlm-citation>
</ref>
<ref id="B12">
<label>12</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[CHIN]]></surname>
<given-names><![CDATA[R. W.]]></given-names>
</name>
<name>
<surname><![CDATA[STANBRIDGE]]></surname>
<given-names><![CDATA[D. I.]]></given-names>
</name>
<name>
<surname><![CDATA[SCHOOK]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
</person-group>
<source><![CDATA[Increasing separation capacity with new and proven technologies]]></source>
<year>2002</year>
</nlm-citation>
</ref>
<ref id="B13">
<label>13</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[CHIN]]></surname>
<given-names><![CDATA[RW]]></given-names>
</name>
<name>
<surname><![CDATA[STANBRIDGE]]></surname>
<given-names><![CDATA[DI]]></given-names>
</name>
<name>
<surname><![CDATA[SCHOOK]]></surname>
<given-names><![CDATA[R]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Increasing separation capacity with new and proven technologies]]></article-title>
<source><![CDATA[SPE Annual Technical Conference And Exhibition]]></source>
<year>2002</year>
</nlm-citation>
</ref>
<ref id="B14">
<label>14</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[CRONQUIST]]></surname>
<given-names><![CDATA[C]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Evaluating and producing volatile oil-reservoirs]]></article-title>
<source><![CDATA[World Oil]]></source>
<year>1979</year>
<volume>188</volume>
<numero>5</numero>
<issue>5</issue>
<page-range>159</page-range></nlm-citation>
</ref>
<ref id="B15">
<label>15</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[ELSAYED]]></surname>
<given-names><![CDATA[Khairy]]></given-names>
</name>
<name>
<surname><![CDATA[LACOR]]></surname>
<given-names><![CDATA[Chris]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modeling and Pareto optimization of gas cyclone separator performance using RBF type artificial neural networks and genetic algorithms]]></article-title>
<source><![CDATA[Powder Technology]]></source>
<year>2012</year>
<volume>217</volume>
<page-range>84-99</page-range></nlm-citation>
</ref>
<ref id="B16">
<label>16</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[ERDAL]]></surname>
<given-names><![CDATA[Ferhat M]]></given-names>
</name>
<name>
<surname><![CDATA[SHIRAZI]]></surname>
<given-names><![CDATA[Siamack A]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Local velocity measurements and computational fluid dynamics (CFD) simulations of swirling flow in a cylindrical cyclone separator]]></article-title>
<source><![CDATA[Journal of energy resources technology]]></source>
<year>2004</year>
<volume>126</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>326-33</page-range></nlm-citation>
</ref>
<ref id="B17">
<label>17</label><nlm-citation citation-type="journal">
<collab>EXXONMOBIL</collab>
<article-title xml:lang=""><![CDATA[Chapter 5. Drums: Vapor-Liquid Separators]]></article-title>
<source><![CDATA[ExxonMobil Design Practices: ExxonMobil Research and Engineering Company]]></source>
<year>1999</year>
</nlm-citation>
</ref>
<ref id="B18">
<label>18</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[FEWEL JR]]></surname>
<given-names><![CDATA[KJ]]></given-names>
</name>
<name>
<surname><![CDATA[KEAN]]></surname>
<given-names><![CDATA[James A]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Computer modeling aids separator retrofit]]></article-title>
<source><![CDATA[Oil and Gas Journal]]></source>
<year>1992</year>
<volume>90</volume>
<numero>27</numero>
<issue>27</issue>
</nlm-citation>
</ref>
<ref id="B19">
<label>19</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[FORD]]></surname>
<given-names><![CDATA[IJ]]></given-names>
</name>
<name>
<surname><![CDATA[LAAKSONEN]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[KULMALA]]></surname>
<given-names><![CDATA[M]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modification of the Dillmann-Meier theory of homogeneous nucleation]]></article-title>
<source><![CDATA[The Journal of chemical physics.]]></source>
<year>1993</year>
<volume>99</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>764-5</page-range></nlm-citation>
</ref>
<ref id="B20">
<label>20</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[FRANKIEWICZ]]></surname>
<given-names><![CDATA[Ted]]></given-names>
</name>
<name>
<surname><![CDATA[BROWNE]]></surname>
<given-names><![CDATA[Michael M]]></given-names>
</name>
<name>
<surname><![CDATA[LEE]]></surname>
<given-names><![CDATA[Chang-Ming]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Reducing separation train sizes and increasing capacity by application of emerging technologies]]></article-title>
<source><![CDATA[Offshore Technology Conference]]></source>
<year>2001</year>
</nlm-citation>
</ref>
<ref id="B21">
<label>21</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[FRANKIEWICZ]]></surname>
<given-names><![CDATA[Ted]]></given-names>
</name>
<name>
<surname><![CDATA[LEE]]></surname>
<given-names><![CDATA[Chang-Ming]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Using computational fluid dynamics (CFD) simulation to model fluid motion in process vessels on fixed and floating platforms]]></article-title>
<source><![CDATA[SPE Annual Technical Conference And Exhibition]]></source>
<year>2002</year>
</nlm-citation>
</ref>
<ref id="B22">
<label>22</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[FRENKEL]]></surname>
<given-names><![CDATA[Daan]]></given-names>
</name>
<name>
<surname><![CDATA[SMIT]]></surname>
<given-names><![CDATA[Berend]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Understanding molecular simulation: From algorithms to applications]]></article-title>
<source><![CDATA[Computational sciences series]]></source>
<year>2002</year>
<volume>1</volume>
<page-range>1-638</page-range></nlm-citation>
</ref>
<ref id="B23">
<label>23</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GHARIBSHAHI]]></surname>
<given-names><![CDATA[Reza]]></given-names>
</name>
<name>
<surname><![CDATA[JAFARI]]></surname>
<given-names><![CDATA[Arezou]]></given-names>
</name>
<name>
<surname><![CDATA[AHMADI]]></surname>
<given-names><![CDATA[Hamid]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[CFD investigation of enhanced extra-heavy oil recovery using metallic nanoparticles/steam injection in a micromodel with random pore distribution]]></article-title>
<source><![CDATA[Journal of Petroleum Science and Engineering]]></source>
<year>2019</year>
<volume>174</volume>
<page-range>374-83</page-range></nlm-citation>
</ref>
<ref id="B24">
<label>24</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GIBBS]]></surname>
<given-names><![CDATA[Josiah Willard]]></given-names>
</name>
</person-group>
<source><![CDATA[Elementary Principles in Statistical Mechanics, developed with special reference to the rational foundation of thermodynamics: New Haven]]></source>
<year>1914</year>
</nlm-citation>
</ref>
<ref id="B25">
<label>25</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GIRSHICK]]></surname>
<given-names><![CDATA[Steven L]]></given-names>
</name>
<name>
<surname><![CDATA[CHIU]]></surname>
<given-names><![CDATA[Chia-Pin]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Kinetic nucleation theory: A new expression for the rate of homogeneous nucleation from an ideal supersaturated vapor]]></article-title>
<source><![CDATA[The journal of chemical physics]]></source>
<year>1990</year>
<volume>93</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>1273-7</page-range></nlm-citation>
</ref>
<ref id="B26">
<label>26</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GOMEZ]]></surname>
<given-names><![CDATA[LE]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Enhanced mechanistic model and field-application design of gas/liquid cylindrical cyclone separators]]></article-title>
<source><![CDATA[Spe Journal,]]></source>
<year>2000</year>
<volume>5</volume>
<numero>02</numero>
<issue>02</issue>
<page-range>190-8</page-range></nlm-citation>
</ref>
<ref id="B27">
<label>27</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GONZÁLEZ-SILVA]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The importance of 3D mesh generation for large eddy simulation of gas-solid turbulent flows in a fluidized beds]]></article-title>
<source><![CDATA[Int. J. Chem. Mol. Nucl. Mater. Metall. Eng]]></source>
<year>2012</year>
<volume>6</volume>
<numero>8</numero>
<issue>8</issue>
<page-range>770-7</page-range></nlm-citation>
</ref>
<ref id="B28">
<label>28</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GONZÁLEZ]]></surname>
<given-names><![CDATA[Germán]]></given-names>
</name>
<name>
<surname><![CDATA[JIMÉNEZ]]></surname>
<given-names><![CDATA[Natalia Prieto]]></given-names>
</name>
<name>
<surname><![CDATA[SALAZAR]]></surname>
<given-names><![CDATA[Oscar Fabio]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Fluid Dynamics of Gas-Solid Fluidized Beds]]></article-title>
<source><![CDATA[Advanced Fluid Dynamics: InTech]]></source>
<year>2012</year>
</nlm-citation>
</ref>
<ref id="B29">
<label>29</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GONZALEZ]]></surname>
<given-names><![CDATA[S.G]]></given-names>
</name>
</person-group>
<source><![CDATA[Modeling and simulation of cocurrent downflow reactor (Downer). 2008.]]></source>
<year>2008</year>
<publisher-loc><![CDATA[Campinas, Brazil ]]></publisher-loc>
<publisher-name><![CDATA[State University of Campinas]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B30">
<label>30</label><nlm-citation citation-type="book">
<collab>GPSA</collab>
<source><![CDATA[GPSA Engineering Data Book]]></source>
<year></year>
<volume>1</volume>
<edition>11</edition>
<publisher-name><![CDATA[GPSA publisher]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B31">
<label>31</label><nlm-citation citation-type="">
<collab>CREG</collab>
<source><![CDATA[Sector Gas Natural en Colombia - Transporte de Gas. 2016]]></source>
<year>2016</year>
<page-range>41</page-range><publisher-loc><![CDATA[Cartagena. Anais... Cartagena ]]></publisher-loc>
</nlm-citation>
</ref>
<ref id="B32">
<label>32</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GRØDAL]]></surname>
<given-names><![CDATA[Evert O]]></given-names>
</name>
<name>
<surname><![CDATA[REALFF]]></surname>
<given-names><![CDATA[Matthew J]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Optimal design of two-and three-phase separators: A mathematical programming formulation]]></article-title>
<source><![CDATA[SPE ANNUAL TECHNICAL CONFERENCE AND EXHIBITION]]></source>
<year>1999</year>
</nlm-citation>
</ref>
<ref id="B33">
<label>33</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GUO]]></surname>
<given-names><![CDATA[Boyan]]></given-names>
</name>
<name>
<surname><![CDATA[GHALAMBOR]]></surname>
<given-names><![CDATA[Ali]]></given-names>
</name>
</person-group>
<source><![CDATA[Natural gas engineering handbook: Elsevier]]></source>
<year>2014</year>
</nlm-citation>
</ref>
<ref id="B34">
<label>34</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[GYARMATHY]]></surname>
<given-names><![CDATA[George]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The spherical droplet in gaseous carrier streams: review and synthesis]]></article-title>
<source><![CDATA[Multiphase science and technology]]></source>
<year>1982</year>
<volume>1</volume>
<numero>1-4</numero>
<issue>1-4</issue>
</nlm-citation>
</ref>
<ref id="B35">
<label>35</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HALLANGER]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[SOENSTABOE]]></surname>
<given-names><![CDATA[F]]></given-names>
</name>
<name>
<surname><![CDATA[KNUTSEN]]></surname>
<given-names><![CDATA[T.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A simulation model for three-phase gravity separators]]></article-title>
<source><![CDATA[SPE Annual Technical Conference And Exhibition]]></source>
<year>1996</year>
</nlm-citation>
</ref>
<ref id="B36">
<label>36</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HAN]]></surname>
<given-names><![CDATA[Qing]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The effect of geometry and operation conditions on the performance of a gas-liquid cylindrical cyclone separator with new structure]]></article-title>
<source><![CDATA[AIP Conference Proceedings]]></source>
<year>2013</year>
</nlm-citation>
</ref>
<ref id="B37">
<label>37</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HANSEN]]></surname>
<given-names><![CDATA[Ernst WM]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Phenomenological Modelling and Simulation of Fluid Flow and Separation Behavior in Offshore Gravity Separators]]></article-title>
<source><![CDATA[ASME-PUBLICATIONS-PVP]]></source>
<year>2001</year>
<volume>431</volume>
<page-range>23-30</page-range></nlm-citation>
</ref>
<ref id="B38">
<label>38</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HANSEN]]></surname>
<given-names><![CDATA[Ernst WM]]></given-names>
</name>
<name>
<surname><![CDATA[CELIUS]]></surname>
<given-names><![CDATA[Harald K]]></given-names>
</name>
<name>
<surname><![CDATA[HAFSKJOLD]]></surname>
<given-names><![CDATA[Bjørn]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Fluid flow and separation mechanisms in offshore separation equipment]]></article-title>
<source><![CDATA[International Symposium On Two-Phase Flow Modelling And Experimentation]]></source>
<year>1995</year>
<page-range>16</page-range></nlm-citation>
</ref>
<ref id="B39">
<label>39</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HANSEN]]></surname>
<given-names><![CDATA[Ernst WM]]></given-names>
</name>
<name>
<surname><![CDATA[RORTVEIT]]></surname>
<given-names><![CDATA[GJ]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Numerical simulation of fluid mechanisms and separation behavior in offshore gravity separators]]></article-title>
<source><![CDATA[Surfactant science series]]></source>
<year>2006</year>
<volume>132</volume>
<page-range>593</page-range></nlm-citation>
</ref>
<ref id="B40">
<label>40</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HANSEN]]></surname>
<given-names><![CDATA[EWM]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Fluid flow modelling of gravity separators]]></article-title>
<source><![CDATA[PROC]]></source>
<year>1991</year>
<page-range>364-80</page-range></nlm-citation>
</ref>
<ref id="B41">
<label>41</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HANSEN]]></surname>
<given-names><![CDATA[EWM]]></given-names>
</name>
</person-group>
<source><![CDATA[Numerical Simulation of Fluid Flow Behavior Inside, and Redesign of a Field Separator. In: PROC]]></source>
<year>1993</year>
<conf-name><![CDATA[ 6thInternational Conference on Multiphase Production]]></conf-name>
<conf-loc>Cannes, Francia </conf-loc>
<page-range>117-29</page-range></nlm-citation>
</ref>
<ref id="B42">
<label>42</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HOFFMANN]]></surname>
<given-names><![CDATA[Alex C.]]></given-names>
</name>
<name>
<surname><![CDATA[STEIN]]></surname>
<given-names><![CDATA[Louis E]]></given-names>
</name>
</person-group>
<source><![CDATA[Gas Cyclones and Swirl Tubes: Principles, Design, and Operation]]></source>
<year>2008</year>
<edition>2</edition>
<publisher-loc><![CDATA[Berlin Heidelberg ]]></publisher-loc>
<publisher-name><![CDATA[Springer-Verlag]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B43">
<label>43</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HREIZ]]></surname>
<given-names><![CDATA[Rainier]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Hydrodynamics and velocity measurements in gas-liquid swirling flows in cylindrical cyclones]]></article-title>
<source><![CDATA[Chemical engineering research and design]]></source>
<year>2014</year>
<volume>92</volume>
<numero>11</numero>
<issue>11</issue>
<page-range>2231-46</page-range></nlm-citation>
</ref>
<ref id="B44">
<label>44</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[HREIZ]]></surname>
<given-names><![CDATA[Rainier]]></given-names>
</name>
<name>
<surname><![CDATA[GENTRIC]]></surname>
<given-names><![CDATA[Caroline]]></given-names>
</name>
<name>
<surname><![CDATA[MIDOUX]]></surname>
<given-names><![CDATA[Noël]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Numerical investigation of swirling flow in cylindrical cyclones]]></article-title>
<source><![CDATA[Chemical engineering research and design]]></source>
<year>2011</year>
<volume>89</volume>
<numero>12</numero>
<issue>12</issue>
<page-range>2521-39</page-range></nlm-citation>
</ref>
<ref id="B45">
<label>45</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[JEONG]]></surname>
<given-names><![CDATA[Woowon]]></given-names>
</name>
<name>
<surname><![CDATA[SEONG]]></surname>
<given-names><![CDATA[Jaehoon]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Comparison of effects on technical variances of computational fluid dynamics (CFD) software based on finite element and finite volume methods]]></article-title>
<source><![CDATA[International Journal of Mechanical Sciences]]></source>
<year>2014</year>
<volume>78</volume>
<page-range>19-26</page-range></nlm-citation>
</ref>
<ref id="B46">
<label>46</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[KALIKMANOV]]></surname>
<given-names><![CDATA[VI]]></given-names>
</name>
<name>
<surname><![CDATA[WÖLK]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[KRASKA]]></surname>
<given-names><![CDATA[T]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Argon nucleation: Bringing together theory, simulations, and experiment.]]></article-title>
<source><![CDATA[The Journal of chemical physics]]></source>
<year>2008</year>
<volume>128</volume>
<numero>12</numero>
<issue>12</issue>
<page-range>124506</page-range></nlm-citation>
</ref>
<ref id="B47">
<label>47</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[KALIKMANOV]]></surname>
<given-names><![CDATA[Vitaly]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[New developments in nucleation theory and their impact on natural gas separation]]></article-title>
<source><![CDATA[SPE Annual Technical Conference And Exhibition]]></source>
<year>2007</year>
</nlm-citation>
</ref>
<ref id="B48">
<label>48</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[KALIKMANOV]]></surname>
<given-names><![CDATA[Vitaly I]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Classical nucleation theory]]></article-title>
<source><![CDATA[Nucleation theory: Springer]]></source>
<year>2013</year>
<page-range>17-41</page-range></nlm-citation>
</ref>
<ref id="B49">
<label>49</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[KATZ]]></surname>
<given-names><![CDATA[Joseph L]]></given-names>
</name>
<name>
<surname><![CDATA[WIEDERSICH]]></surname>
<given-names><![CDATA[H]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Nucleation theory without Maxwell demons]]></article-title>
<source><![CDATA[Journal of colloid and interface science]]></source>
<year>1977</year>
<volume>61</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>351-5</page-range></nlm-citation>
</ref>
<ref id="B50">
<label>50</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[KHAROUA]]></surname>
<given-names><![CDATA[N.]]></given-names>
</name>
<name>
<surname><![CDATA[KHEZZAR]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[SAADAWI]]></surname>
<given-names><![CDATA[H]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[CFD Modelling of a Horizontal Three-Phase Separator: A Population Balance Approach]]></article-title>
<source><![CDATA[American Journal of Fluid Dynamics]]></source>
<year>2013</year>
<volume>3</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>101-18</page-range></nlm-citation>
</ref>
<ref id="B51">
<label>51</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[LALEH]]></surname>
<given-names><![CDATA[Ali Pourahmadi]]></given-names>
</name>
<name>
<surname><![CDATA[SVRCEK]]></surname>
<given-names><![CDATA[William Y.]]></given-names>
</name>
<name>
<surname><![CDATA[MONNERY]]></surname>
<given-names><![CDATA[Wayne D]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Design and CFD studies of multiphase separators-a review]]></article-title>
<source><![CDATA[The Canadian Journal of Chemical Engineering]]></source>
<year>2012</year>
<volume>90</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>1547-61</page-range></nlm-citation>
</ref>
<ref id="B52">
<label>52</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[LEBON]]></surname>
<given-names><![CDATA[Georgy]]></given-names>
</name>
<name>
<surname><![CDATA[JOU]]></surname>
<given-names><![CDATA[David]]></given-names>
</name>
<name>
<surname><![CDATA[CASAS-VÁZQUEZ]]></surname>
<given-names><![CDATA[José]]></given-names>
</name>
</person-group>
<source><![CDATA[Understanding non-equilibrium thermodynamics: Springer]]></source>
<year>2008</year>
<volume>295</volume>
</nlm-citation>
</ref>
<ref id="B53">
<label>53</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[LEE]]></surname>
<given-names><![CDATA[Chang-Ming]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Field confirmation of CFD design for FPSO- mounted separator]]></article-title>
<source><![CDATA[Offshore Technology Conference]]></source>
<year>2004</year>
</nlm-citation>
</ref>
<ref id="B54">
<label>54</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[LEE]]></surname>
<given-names><![CDATA[Joseph M]]></given-names>
</name>
<name>
<surname><![CDATA[KHAN]]></surname>
<given-names><![CDATA[Rafiqul I]]></given-names>
</name>
<name>
<surname><![CDATA[PHELPS]]></surname>
<given-names><![CDATA[Daniel W]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Debottlenecking and Computational-Fluid-Dynamics Studies of High-and Low-Pressure Production Separators]]></article-title>
<source><![CDATA[SPE Projects, Facilities &amp; Construction]]></source>
<year>2009</year>
<volume>4</volume>
<numero>04</numero>
<issue>04</issue>
<page-range>124-31</page-range></nlm-citation>
</ref>
<ref id="B55">
<label>55</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[LU]]></surname>
<given-names><![CDATA[Yaojun]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Effect of Internal Baffles on Volumetric Utilization of an FWKO--A CFD Evaluation]]></article-title>
<source><![CDATA[SPE Annual Technical Conference And Exhibition]]></source>
<year>2007</year>
</nlm-citation>
</ref>
<ref id="B56">
<label>56</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[LUIJTEN]]></surname>
<given-names><![CDATA[Carlo Cornelis Maria]]></given-names>
</name>
</person-group>
<source><![CDATA[Nucleation and droplet growth at high pressure: Eindhoven University of Technology]]></source>
<year>1998</year>
<publisher-loc><![CDATA[The Netherlands ]]></publisher-loc>
</nlm-citation>
</ref>
<ref id="B57">
<label>57</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MACKENZIE]]></surname>
<given-names><![CDATA[Alasdair]]></given-names>
</name>
</person-group>
<source><![CDATA[A comparison of CFD software packages&#8217; ability to model a submerged jet. The 11th International Conference on CFD in the Minerals and Process Industries]]></source>
<year>2015</year>
<page-range>1-4</page-range><publisher-loc><![CDATA[Dickson, Australia ]]></publisher-loc>
<publisher-name><![CDATA[Commonwealth Scientific and Industrial Research Organisation (CSIRO)]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B58">
<label>58</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MALISKA]]></surname>
<given-names><![CDATA[Clovis Raimundo]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Transferência de calor e mecânica dos fluidos computacional]]></article-title>
<source><![CDATA[Grupo Gen-LTC]]></source>
<year>2017</year>
</nlm-citation>
</ref>
<ref id="B59">
<label>59</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MERIKANTO]]></surname>
<given-names><![CDATA[Joonas]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Monte Carlo simulations of molecular clusters in nucleation]]></article-title>
<source><![CDATA[Finnish Assosiation for Aerosol Research]]></source>
<year>2007</year>
<month>b</month>
</nlm-citation>
</ref>
<ref id="B60">
<label>60</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MERIKANTO]]></surname>
<given-names><![CDATA[Joonas]]></given-names>
</name>
</person-group>
<source><![CDATA[Monte Carlo simulations of molecular clusters in nucleation]]></source>
<year>2007</year>
<publisher-name><![CDATA[University of Helsinki, Department of Physics]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B61">
<label>61</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MOKHATAB]]></surname>
<given-names><![CDATA[Saeid]]></given-names>
</name>
<name>
<surname><![CDATA[POE]]></surname>
<given-names><![CDATA[William A.]]></given-names>
</name>
<name>
<surname><![CDATA[MAK]]></surname>
<given-names><![CDATA[John Y]]></given-names>
</name>
</person-group>
<source><![CDATA[Chapter 3 - Basic Concepts of Natural Gas Processing. Handbook of Natural GasTransmission and Processing]]></source>
<year>2015</year>
<edition>Third</edition>
<page-range>123-35</page-range><publisher-loc><![CDATA[Boston ]]></publisher-loc>
<publisher-name><![CDATA[Gulf Professional Publishing]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B62">
<label>62</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MONNERY]]></surname>
<given-names><![CDATA[WD]]></given-names>
</name>
<name>
<surname><![CDATA[SVRCEK]]></surname>
<given-names><![CDATA[WY]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Analytical study of liquid/vapor separation efficiency]]></article-title>
<source><![CDATA[study developed for Petroleum Technology Alliance Canada]]></source>
<year>2000</year>
</nlm-citation>
</ref>
<ref id="B63">
<label>63</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MORROW]]></surname>
<given-names><![CDATA[T. B. EW. M]]></given-names>
</name>
<name>
<surname><![CDATA[Hansen]]></surname>
<given-names><![CDATA[H]]></given-names>
</name>
<name>
<surname><![CDATA[Heitrnann]]></surname>
<given-names><![CDATA[B]]></given-names>
</name>
<name>
<surname><![CDATA[Laksa]]></surname>
<given-names><![CDATA[AEllingsen]]></given-names>
</name>
</person-group>
<source><![CDATA[Fluid Flow Modelling of Gravity Separators]]></source>
<year>1991</year>
<conf-name><![CDATA[ 5International Conference on MultiPhase Production]]></conf-name>
<conf-loc>Cannes, France </conf-loc>
<page-range>364&#8722;380</page-range></nlm-citation>
</ref>
<ref id="B64">
<label>64</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[MOVAFAGHIAN]]></surname>
<given-names><![CDATA[S]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The effects of geometry, fluid properties and pressure on the hydrodynamics of gas-liquid cylindrical cyclone separators]]></article-title>
<source><![CDATA[International Journal of Multiphase Flow]]></source>
<year>2000</year>
<volume>26</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>999-1018</page-range></nlm-citation>
</ref>
<ref id="B65">
<label>65</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[NAPARI]]></surname>
<given-names><![CDATA[Ismo]]></given-names>
</name>
</person-group>
<source><![CDATA[Density functional theory of nucleation and phase behavior in binary fluid systems]]></source>
<year>2000</year>
<publisher-name><![CDATA[University of Helsinki, Department of Physics, Theoretical Physics Division, Faculty of Science]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B66">
<label>66</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[NEWTON]]></surname>
<given-names><![CDATA[Timothy]]></given-names>
</name>
<name>
<surname><![CDATA[CONNOLLY]]></surname>
<given-names><![CDATA[David]]></given-names>
</name>
<name>
<surname><![CDATA[MOKHATAB]]></surname>
<given-names><![CDATA[Saeid]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Tools to model multiphase separation]]></article-title>
<source><![CDATA[Chemical engineering progress]]></source>
<year>2007</year>
<volume>103</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>26-31</page-range></nlm-citation>
</ref>
<ref id="B67">
<label>67</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[NIEUWSTADT]]></surname>
<given-names><![CDATA[Frans T. M.]]></given-names>
</name>
<name>
<surname><![CDATA[DIRKZWAGER]]></surname>
<given-names><![CDATA[Maarten]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A Fluid Mechanics Model for an Axial Cyclone Separator]]></article-title>
<source><![CDATA[Industrial &amp; Engineering Chemistry Research,]]></source>
<year>1995</year>
<volume>34</volume>
<numero>10</numero>
<issue>10</issue>
<page-range>3399-404</page-range></nlm-citation>
</ref>
<ref id="B68">
<label>68</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[OXTOBY]]></surname>
<given-names><![CDATA[David W]]></given-names>
</name>
<name>
<surname><![CDATA[KASHCHIEV]]></surname>
<given-names><![CDATA[Dimo]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A general relation between the nucleation work and the size of the nucleus in multicomponent nucleation]]></article-title>
<source><![CDATA[The Journal of chemical physics]]></source>
<year>1994</year>
<volume>100</volume>
<numero>10</numero>
<issue>10</issue>
<page-range>7665-71</page-range></nlm-citation>
</ref>
<ref id="B69">
<label>69</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[PATHAK]]></surname>
<given-names><![CDATA[Harshad Narayan]]></given-names>
</name>
</person-group>
<source><![CDATA[Nucleation and Droplet Growth During Co-condensation of Nonane and D 2 O in a Supersonic Nozzle]]></source>
<year>2013</year>
<publisher-name><![CDATA[The Ohio State University]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B70">
<label>70</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[PINILLA]]></surname>
<given-names><![CDATA[Laura Isabel Díaz]]></given-names>
</name>
<name>
<surname><![CDATA[MENESES-PRADO]]></surname>
<given-names><![CDATA[Leidy Paola]]></given-names>
</name>
<name>
<surname><![CDATA[GONZÁLEZ-SILVA]]></surname>
<given-names><![CDATA[Germán]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Dinámica de fluidos computacional en el análisis de intercambiadores de calor de coraza y tubos]]></article-title>
<source><![CDATA[Revista UIS Ingenierías]]></source>
<year>2019</year>
<volume>18</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>237-44</page-range></nlm-citation>
</ref>
<ref id="B71">
<label>71</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[POURAHMADI LALEH]]></surname>
<given-names><![CDATA[Ali]]></given-names>
</name>
<name>
<surname><![CDATA[SVRCEK]]></surname>
<given-names><![CDATA[William Y.]]></given-names>
</name>
<name>
<surname><![CDATA[MONNERY]]></surname>
<given-names><![CDATA[Wayne]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Computational Fluid Dynamics-Based Study of an Oilfield Separator-Part I: A Realistic Simulation]]></article-title>
<source><![CDATA[Oil and Gas Facilities]]></source>
<year>2012</year>
<volume>1</volume>
<numero>06</numero>
<issue>06</issue>
<page-range>57-68</page-range></nlm-citation>
</ref>
<ref id="B72">
<label>72</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[CHAVES GUERRERO]]></surname>
<given-names><![CDATA[Arlex]]></given-names>
</name>
<name>
<surname><![CDATA[PRIETO JIMÉNEZ]]></surname>
<given-names><![CDATA[Natalia]]></given-names>
</name>
<name>
<surname><![CDATA[GONZÁLEZ SILVA]]></surname>
<given-names><![CDATA[Germán]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Comparative Study of Equations of State for the Dew Curves Calculation in High Pressure Natural Gas Mixtures]]></article-title>
<source><![CDATA[Revista Logos Ciencia &amp; Tecnología]]></source>
<year>2018</year>
<volume>11</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>13</page-range></nlm-citation>
</ref>
<ref id="B73">
<label>73</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[REZENDE]]></surname>
<given-names><![CDATA[Ricardo Vicente de Paula]]></given-names>
</name>
</person-group>
<source><![CDATA[Modelagem matemática e desenvolvimento de metodologia computacional para a simulação numérica do escoamento bifásico de ar e ferro-gusa em canal de corrida de alto-forno]]></source>
<year>2013</year>
<publisher-loc><![CDATA[Florianópolis ]]></publisher-loc>
<publisher-name><![CDATA[Universidade Federal de Santa Catarina, Centro Tecnológico]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B74">
<label>74</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[ROSIN]]></surname>
<given-names><![CDATA[PAUL]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The laws governing the fineness of powdered coal]]></article-title>
<source><![CDATA[J. Inst. Fuel.]]></source>
<year>1933</year>
<volume>7</volume>
<page-range>. 29-36</page-range></nlm-citation>
</ref>
<ref id="B75">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[SETEKLEIV]]></surname>
<given-names><![CDATA[A Eddie]]></given-names>
</name>
</person-group>
<source><![CDATA[Experimental characterization of scrubber internals at low and elevated pressures]]></source>
<year>2012</year>
<publisher-name><![CDATA[Norwegian University of Science and Technology (NTNU)]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B76">
<label>76</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[SILVA]]></surname>
<given-names><![CDATA[Germán González]]></given-names>
</name>
<name>
<surname><![CDATA[PRIETO]]></surname>
<given-names><![CDATA[Natalia]]></given-names>
</name>
<name>
<surname><![CDATA[MERCADO]]></surname>
<given-names><![CDATA[Iván]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Large Eddy Simulation (LES) Aplicado a un lecho fluidizado gas-sólido. Parte I: Reactor a escala de laboratorio]]></article-title>
<source><![CDATA[Revista UIS Ingenierías]]></source>
<year>2018</year>
<volume>17</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>93-104</page-range></nlm-citation>
</ref>
<ref id="B77">
<label>77</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[SOUDERS]]></surname>
<given-names><![CDATA[Mott]]></given-names>
</name>
<name>
<surname><![CDATA[BROWN]]></surname>
<given-names><![CDATA[George Granger]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Design of fractionating columns I. Entrainment and capacity]]></article-title>
<source><![CDATA[Industrial &amp; Engineering Chemistry]]></source>
<year>1934</year>
<volume>26</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>98-103</page-range></nlm-citation>
</ref>
<ref id="B78">
<label>78</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[STANLEY]]></surname>
<given-names><![CDATA[WALAS]]></given-names>
</name>
</person-group>
<collab>WALAS, Ed</collab>
<article-title xml:lang=""><![CDATA[Chemical process equipment-selection and design]]></article-title>
<source><![CDATA[Butterman-Heinemam Series]]></source>
<year>1990</year>
</nlm-citation>
</ref>
<ref id="B79">
<label>79</label><nlm-citation citation-type="">
<collab>SULZER</collab>
<source><![CDATA[Brochure Gas/Liquid Separation Technology]]></source>
<year></year>
</nlm-citation>
</ref>
<ref id="B80">
<label>80</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[SVRCEK]]></surname>
<given-names><![CDATA[WY]]></given-names>
</name>
<name>
<surname><![CDATA[MONNERY]]></surname>
<given-names><![CDATA[WD]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Design two-phase separators within the right limits]]></article-title>
<source><![CDATA[Chemical engineering progress]]></source>
<year>1993</year>
<volume>89</volume>
<numero>10</numero>
<issue>10</issue>
<page-range>53-60</page-range></nlm-citation>
</ref>
<ref id="B81">
<label>81</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[SWANBORN]]></surname>
<given-names><![CDATA[R. A]]></given-names>
</name>
</person-group>
<source><![CDATA[A new approach to the design of gas-liquid separators for the oil industr]]></source>
<year>1988</year>
<publisher-name><![CDATA[Delft University of Technology]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B82">
<label>82</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[SWARTZENDRUBER]]></surname>
<given-names><![CDATA[Jason]]></given-names>
</name>
<name>
<surname><![CDATA[FADDA]]></surname>
<given-names><![CDATA[Dani]]></given-names>
</name>
<name>
<surname><![CDATA[TAYLOR]]></surname>
<given-names><![CDATA[David]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Accommodating Last Minute Changes: Two Phase Separation Performance Validated by CFD]]></article-title>
<source><![CDATA[ASME 2005 Fluids Engineering Division Summer Meeting, 2005]]></source>
<year>2005</year>
<page-range>713-5</page-range><publisher-name><![CDATA[American Society of Mechanical Engineers]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B83">
<label>83</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[VERLAAN]]></surname>
<given-names><![CDATA[C. C. J]]></given-names>
</name>
</person-group>
<source><![CDATA[Performance of novel mist eliminators]]></source>
<year>1991</year>
<publisher-name><![CDATA[Delft University of Technology]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B84">
<label>84</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[WALLIS]]></surname>
<given-names><![CDATA[Graham B]]></given-names>
</name>
</person-group>
<source><![CDATA[One-dimensional two-phase flow]]></source>
<year>1969</year>
<publisher-loc><![CDATA[New York ]]></publisher-loc>
<publisher-name><![CDATA[McGraw Hill Higher Education]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B85">
<label>85</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[WANG]]></surname>
<given-names><![CDATA[Shoubo]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Gas-Liquid Cylindrical Cyclone (GLCC©) Compact Separators For Wet Gas Applications]]></article-title>
<source><![CDATA[Journal of energy resources technology]]></source>
<year>2003</year>
<volume>125</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>43-50</page-range></nlm-citation>
</ref>
<ref id="B86">
<label>86</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[WANG]]></surname>
<given-names><![CDATA[Shuyan]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Effect of the inlet angle on the performance of a cyclone separator using CFD-DEM]]></article-title>
<source><![CDATA[Advanced Powder Technology]]></source>
<year>2019</year>
<volume>30</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>227-39</page-range></nlm-citation>
</ref>
<ref id="B87">
<label>87</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[WASILEWSKI]]></surname>
<given-names><![CDATA[Marek]]></given-names>
</name>
<name>
<surname><![CDATA[BRAR]]></surname>
<given-names><![CDATA[Lakhbir Singh]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Effect of the inlet duct angle on the performance of cyclone separators]]></article-title>
<source><![CDATA[Separation and Purification Technology]]></source>
<year>2019</year>
<volume>213</volume>
<page-range>19-33</page-range></nlm-citation>
</ref>
<ref id="B88">
<label>88</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[WILEMSKI]]></surname>
<given-names><![CDATA[Gerald]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The Kelvin equation and self-consistent nucleation theory]]></article-title>
<source><![CDATA[The Journal of chemical physics]]></source>
<year>1995</year>
<volume>103</volume>
<numero>3</numero>
<issue>3</issue>
<page-range>1119-26</page-range></nlm-citation>
</ref>
<ref id="B89">
<label>89</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[WILKINSON]]></surname>
<given-names><![CDATA[D]]></given-names>
</name>
<name>
<surname><![CDATA[WALDIE]]></surname>
<given-names><![CDATA[B]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[CFD and experimental studies of fluid and particle flow in horizontal primary separators]]></article-title>
<source><![CDATA[Chemical engineering research &amp; design]]></source>
<year>1994</year>
<volume>72</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>189-96</page-range></nlm-citation>
</ref>
<ref id="B90">
<label>90</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[WILKINSON]]></surname>
<given-names><![CDATA[Derek]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Baffle plate configurations to enhance separation in horizontal primary separators.]]></article-title>
<source><![CDATA[Chemical Engineering Journal,]]></source>
<year>2000</year>
<volume>77</volume>
<numero>3</numero>
<issue>3</issue>
<page-range>221-6</page-range></nlm-citation>
</ref>
<ref id="B91">
<label>91</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[XU]]></surname>
<given-names><![CDATA[Weiwei]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Performance evaluat on of a new cyclone separator-Part II simulation results]]></article-title>
<source><![CDATA[Separation and Purification Technology]]></source>
<year>2016</year>
<volume>160</volume>
<page-range>112-6</page-range></nlm-citation>
</ref>
<ref id="B92">
<label>92</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[YOUNG]]></surname>
<given-names><![CDATA[JB]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The condensation and evaporation of liquid droplets in a pure vapour at arbitrary Knudsen number]]></article-title>
<source><![CDATA[International journal of heat and mass transfer]]></source>
<year>1991</year>
<volume>34</volume>
<numero>7</numero>
<issue>7</issue>
<page-range>1649-61</page-range></nlm-citation>
</ref>
<ref id="B93">
<label>93</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[YU]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
</person-group>
<source><![CDATA[Oil, water and gas three-phase cyclone separator]]></source>
<year>2013</year>
</nlm-citation>
</ref>
<ref id="B94">
<label>94</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[ZHANG]]></surname>
<given-names><![CDATA[X. D.]]></given-names>
</name>
</person-group>
<source><![CDATA[Embedded-type inverted double-cone oil-gas water triphase cyclone separator]]></source>
<year>2014</year>
</nlm-citation>
</ref>
</ref-list>
</back>
</article>
