<?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>0035-001X</journal-id>
<journal-title><![CDATA[Revista mexicana de física]]></journal-title>
<abbrev-journal-title><![CDATA[Rev. mex. fis.]]></abbrev-journal-title>
<issn>0035-001X</issn>
<publisher>
<publisher-name><![CDATA[Sociedad Mexicana de Física]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0035-001X2020000500656</article-id>
<article-id pub-id-type="doi">10.31349/revmexfis.66.656</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Equation of state to predict the solid-liquid-vapor phase coexistences of pure substances]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Marín-García]]></surname>
<given-names><![CDATA[J. M.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
<xref ref-type="aff" rid="Aaf"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Romero-Martínez]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
<xref ref-type="aff" rid="Aaf"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Guevara-Rodríguez]]></surname>
<given-names><![CDATA[F. de J.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
<xref ref-type="aff" rid="Aaf"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Instituto Mexicano del Petróleo Programa Académico de Posgrado Dirección de Desarrollo de Talento]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
</aff>
<aff id="Af2">
<institution><![CDATA[,Instituto Mexicano del Petróleo Gerencia de Herramientas y Sistemas para Pozos e Instalaciones Dirección de Investigación en Exploración y Producción]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
</aff>
<aff id="Af3">
<institution><![CDATA[,Instituto Mexicano del Petróleo Gerencia de Desarrollo de Materiales y Productos Químicos Dirección de Investigación en Transformación de Hidrocarburos]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
</aff>
<aff id="Af4">
<institution><![CDATA[,Instituto Mexicano del Petróleo  ]]></institution>
<addr-line><![CDATA[Ciudad de México ]]></addr-line>
<country>Mexico</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>10</month>
<year>2020</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>10</month>
<year>2020</year>
</pub-date>
<volume>66</volume>
<numero>5</numero>
<fpage>656</fpage>
<lpage>670</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S0035-001X2020000500656&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S0035-001X2020000500656&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S0035-001X2020000500656&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract A non-cubic equation of state is used to predict the solid-liquid, solid-vapor and liquid-vapor coexistences of pure substances. The equation of state is obtained using as input data the critical point, the boiling temperature, the triple point temperature and the acentric factor of the substance. In this work, some examples of phase diagrams predicted with the equation of state are reported in order to show its capabilities. Finally, a database with the parameters for different pure substances is presented.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[Phase coexistence]]></kwd>
<kwd lng="en"><![CDATA[solid]]></kwd>
<kwd lng="en"><![CDATA[liquid]]></kwd>
<kwd lng="en"><![CDATA[vapor]]></kwd>
<kwd lng="en"><![CDATA[pure substances]]></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[Guevara-Rodríguez]]></surname>
<given-names><![CDATA[F. de J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Ecuación de estado cúbica para substancia pura usando los datos del segundo coeficiente del virial]]></article-title>
<source><![CDATA[Rev. Mex. Fis. E]]></source>
<year>2015</year>
<volume>61</volume>
</nlm-citation>
</ref>
<ref id="B2">
<label>2</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Peng]]></surname>
<given-names><![CDATA[D.-Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Robinson]]></surname>
<given-names><![CDATA[D. B.]]></given-names>
</name>
<name>
<surname><![CDATA[Chao]]></surname>
<given-names><![CDATA[K. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Robinson]]></surname>
<given-names><![CDATA[R. L.]]></given-names>
</name>
</person-group>
<source><![CDATA[Equations of State in Engineering and Research]]></source>
<year>1979</year>
<page-range>185-95</page-range><publisher-loc><![CDATA[New York ]]></publisher-loc>
<publisher-name><![CDATA[American Chemical Society]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B3">
<label>3</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Lang]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<name>
<surname><![CDATA[Wenzel]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Extension of a cubic equation of state to solids]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>1989</year>
<volume>51</volume>
</nlm-citation>
</ref>
<ref id="B4">
<label>4</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Secuianu]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Feroiu]]></surname>
<given-names><![CDATA[V.]]></given-names>
</name>
<name>
<surname><![CDATA[Geana]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Phase behavior for carbon dioxide + ethanol system: Experimental measurements and modeling with a cubic equation of state]]></article-title>
<source><![CDATA[J. Supercrit. Fluid.]]></source>
<year>2008</year>
<volume>47</volume>
</nlm-citation>
</ref>
<ref id="B5">
<label>5</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Wenzel]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Schmidt]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A modified van der Waals equation of state for the representation of phase equilibria between solids, liquids and gases]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>1980</year>
<volume>5</volume>
</nlm-citation>
</ref>
<ref id="B6">
<label>6</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Yokozeki]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Analytical Equation of State for Solid-Liquid-Vapor Phases]]></article-title>
<source><![CDATA[Int. J. Thermophys.]]></source>
<year>2003</year>
<volume>24</volume>
</nlm-citation>
</ref>
<ref id="B7">
<label>7</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Yokozeki]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A simple theoretical model for condensed-phase equilibria based on a hard-sphere equation-of-state and its applications]]></article-title>
<source><![CDATA[Appl. Energy]]></source>
<year>2005</year>
<volume>81</volume>
</nlm-citation>
</ref>
<ref id="B8">
<label>8</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Guevara-Rodríguez]]></surname>
<given-names><![CDATA[F. de J.]]></given-names>
</name>
<name>
<surname><![CDATA[Romero-Martínez]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[An empirical extension for a generalized cubic equation of state, applied to a pure substance with small molecules]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>2013</year>
<volume>347</volume>
</nlm-citation>
</ref>
<ref id="B9">
<label>9</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Schmidt]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Wenzel]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A modified van der Waals type equation of state]]></article-title>
<source><![CDATA[Chem. Eng. Sci.]]></source>
<year>1980</year>
<volume>35</volume>
</nlm-citation>
</ref>
<ref id="B10">
<label>10</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Lee]]></surname>
<given-names><![CDATA[J. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Yoo]]></surname>
<given-names><![CDATA[K.-P.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Comments on &#8220;Analytic Equation of State for Solid-Liquid-Vapor Phases&#8221;]]></article-title>
<source><![CDATA[Int. J. Thermophys.]]></source>
<year>2003</year>
<volume>24</volume>
</nlm-citation>
</ref>
<ref id="B11">
<label>11</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Guevara-Rodríguez]]></surname>
<given-names><![CDATA[F. de J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A methodology to define the Cubic Equation of State of a simple fluid]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>2011</year>
<volume>307</volume>
</nlm-citation>
</ref>
<ref id="B12">
<label>12</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Guennec]]></surname>
<given-names><![CDATA[Y. Le]]></given-names>
</name>
<name>
<surname><![CDATA[Privat]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Lasala]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Jaubert]]></surname>
<given-names><![CDATA[J. N.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[On the imperative need to use a consistent ®-function for the prediction of pure-compound supercritical properties with a cubic equation of state]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>2017</year>
</nlm-citation>
</ref>
<ref id="B13">
<label>13</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Guennec]]></surname>
<given-names><![CDATA[Y. Le]]></given-names>
</name>
<name>
<surname><![CDATA[Lasala]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Privat]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Jaubert]]></surname>
<given-names><![CDATA[J. N.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A consistency test for ®-functions of cubic equations of state]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>2016</year>
<volume>427</volume>
</nlm-citation>
</ref>
<ref id="B14">
<label>14</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Gil-Villegas]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Río]]></surname>
<given-names><![CDATA[F. del]]></given-names>
</name>
<name>
<surname><![CDATA[Benavides]]></surname>
<given-names><![CDATA[A. L.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Deviations from corresponding-states behavior in the vaporliquid equilibrium of the square-well fluid]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>1996</year>
<volume>119</volume>
</nlm-citation>
</ref>
<ref id="B15">
<label>15</label><nlm-citation citation-type="">
<collab>NIST</collab>
<source><![CDATA[Chemisty WebBook]]></source>
<year></year>
</nlm-citation>
</ref>
<ref id="B16">
<label>16</label><nlm-citation citation-type="">
<collab>Design Institute for Physical Properties</collab>
<source><![CDATA[Sample Database]]></source>
<year></year>
</nlm-citation>
</ref>
<ref id="B17">
<label>17</label><nlm-citation citation-type="">
<source><![CDATA[Dortmund Data Bank]]></source>
<year></year>
</nlm-citation>
</ref>
<ref id="B18">
<label>18</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Poling]]></surname>
<given-names><![CDATA[B. E.]]></given-names>
</name>
<name>
<surname><![CDATA[Prausnitz]]></surname>
<given-names><![CDATA[J. M.]]></given-names>
</name>
<name>
<surname><![CDATA[O&#8217;Connell]]></surname>
<given-names><![CDATA[J. P.]]></given-names>
</name>
</person-group>
<source><![CDATA[The properties of gases and liquids]]></source>
<year>2001</year>
<edition>5</edition>
<page-range>A5-A19</page-range><publisher-loc><![CDATA[New York ]]></publisher-loc>
<publisher-name><![CDATA[McGraw-Hill]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B19">
<label>19</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sedunov]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Brondz]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The Zigzag Progression of Melting and Triple Point Properties of n-Alkanes, n-Alcohols, n-Alkanoic Amines and n-Alkanoic Acids]]></article-title>
<source><![CDATA[Voice Publ.]]></source>
<year>2017</year>
<volume>3</volume>
</nlm-citation>
</ref>
<ref id="B20">
<label>20</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Velasco]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Santos]]></surname>
<given-names><![CDATA[M. J.]]></given-names>
</name>
<name>
<surname><![CDATA[White]]></surname>
<given-names><![CDATA[J. A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Extended corresponding states expressions for the changes in enthalpy, compressibility factor and constant-volume heat capacity at vaporization]]></article-title>
<source><![CDATA[J. Chem. Therm.]]></source>
<year>2015</year>
<volume>85</volume>
</nlm-citation>
</ref>
<ref id="B21">
<label>21</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Gallant]]></surname>
<given-names><![CDATA[R.W.]]></given-names>
</name>
<name>
<surname><![CDATA[Railey]]></surname>
<given-names><![CDATA[J. M.]]></given-names>
</name>
<name>
<surname><![CDATA[Yaws]]></surname>
<given-names><![CDATA[C. L.]]></given-names>
</name>
</person-group>
<source><![CDATA[Physical properties of hydrocarbons]]></source>
<year>1984</year>
<edition>2</edition>
<publisher-loc><![CDATA[Houston ]]></publisher-loc>
<publisher-name><![CDATA[Gulf Publishing]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B22">
<label>22</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Nicola]]></surname>
<given-names><![CDATA[G. Di]]></given-names>
</name>
<name>
<surname><![CDATA[Brandoni]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Nicola]]></surname>
<given-names><![CDATA[C. Di]]></given-names>
</name>
<name>
<surname><![CDATA[Giuliani]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Triple point measurements for alternative refrigerants]]></article-title>
<source><![CDATA[J. Therm. Anal. Calorim.]]></source>
<year>2012</year>
<volume>108</volume>
</nlm-citation>
</ref>
<ref id="B23">
<label>23</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Colonna]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Nannan]]></surname>
<given-names><![CDATA[N. R.]]></given-names>
</name>
<name>
<surname><![CDATA[Guardone]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Lemmon]]></surname>
<given-names><![CDATA[E. W.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Multiparameter equations of state for selected siloxanes]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>2006</year>
<volume>244</volume>
</nlm-citation>
</ref>
<ref id="B24">
<label>24</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Colonna]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Nannan]]></surname>
<given-names><![CDATA[N. R.]]></given-names>
</name>
<name>
<surname><![CDATA[Guardone]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Multiparameter equations of state for siloxanes]]></article-title>
<source><![CDATA[Fluid Ph. Equilibria]]></source>
<year>2008</year>
<volume>263</volume>
</nlm-citation>
</ref>
<ref id="B25">
<label>25</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Yaws]]></surname>
<given-names><![CDATA[C. L.]]></given-names>
</name>
</person-group>
<source><![CDATA[Thermophysical properties of chemicals and hydrocarbons]]></source>
<year>2008</year>
<page-range>4-95</page-range><publisher-loc><![CDATA[Norwich ]]></publisher-loc>
<publisher-name><![CDATA[William Andrew]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B26">
<label>26</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Cheng]]></surname>
<given-names><![CDATA[V. M.]]></given-names>
</name>
<name>
<surname><![CDATA[Daniels]]></surname>
<given-names><![CDATA[W. B.]]></given-names>
</name>
<name>
<surname><![CDATA[Crawford]]></surname>
<given-names><![CDATA[R. K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Melting parameters of methane and nitrogen from 0 to 10 kbar]]></article-title>
<source><![CDATA[Phys. Rev. B]]></source>
<year>1975</year>
<volume>11</volume>
</nlm-citation>
</ref>
<ref id="B27">
<label>27</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Jensen]]></surname>
<given-names><![CDATA[J. E.]]></given-names>
</name>
<name>
<surname><![CDATA[Tuttle]]></surname>
<given-names><![CDATA[W. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Stewart]]></surname>
<given-names><![CDATA[R. B.]]></given-names>
</name>
<name>
<surname><![CDATA[Brechna]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Prodell]]></surname>
<given-names><![CDATA[A. G.]]></given-names>
</name>
</person-group>
<source><![CDATA[Brookhaven National Laboratory Report No. BNL10200-R]]></source>
<year>1980</year>
</nlm-citation>
</ref>
<ref id="B28">
<label>28</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ninet]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Datchi]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[High pressure-high temperature phase diagram for ammonia]]></article-title>
<source><![CDATA[J. Chem. Phys.]]></source>
<year>2008</year>
<volume>128</volume>
</nlm-citation>
</ref>
<ref id="B29">
<label>29</label><nlm-citation citation-type="book">
<collab>International Institute of Ammonia Refrigeration</collab>
<source><![CDATA[Ammonia Data Book]]></source>
<year>2008</year>
<edition>2</edition>
<page-range>A32-5</page-range><publisher-loc><![CDATA[Virginia ]]></publisher-loc>
<publisher-name><![CDATA[IIAR]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B30">
<label>30</label><nlm-citation citation-type="">
<source><![CDATA[International Association for the Properties of Water and Steam]]></source>
<year>2011</year>
</nlm-citation>
</ref>
<ref id="B31">
<label>31</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Keenan]]></surname>
<given-names><![CDATA[J. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Keyes]]></surname>
<given-names><![CDATA[F. G.]]></given-names>
</name>
<name>
<surname><![CDATA[Hill]]></surname>
<given-names><![CDATA[P. G.]]></given-names>
</name>
<name>
<surname><![CDATA[Moore]]></surname>
<given-names><![CDATA[J. G.]]></given-names>
</name>
</person-group>
<source><![CDATA[Steam tables: Thermodynamic properties of water including vapor, liquid, and solid phases]]></source>
<year>1992</year>
<publisher-loc><![CDATA[Malabar ]]></publisher-loc>
<publisher-name><![CDATA[Krieger Publishing]]></publisher-name>
</nlm-citation>
</ref>
</ref-list>
</back>
</article>
