<?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>0012-7353</journal-id>
<journal-title><![CDATA[DYNA]]></journal-title>
<abbrev-journal-title><![CDATA[Dyna rev.fac.nac.minas]]></abbrev-journal-title>
<issn>0012-7353</issn>
<publisher>
<publisher-name><![CDATA[Universidad Nacional de Colombia]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0012-73532020000200085</article-id>
<article-id pub-id-type="doi">10.15446/dyna.v87n213.84413</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Experimental study of phase entrainment in copper solvent extraction]]></article-title>
<article-title xml:lang="es"><![CDATA[Estudio experimental de atrapamiento de fases en extracción por solventes de cobre]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Navarro]]></surname>
<given-names><![CDATA[Patricio]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vargas]]></surname>
<given-names><![CDATA[Cristian]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Castillo]]></surname>
<given-names><![CDATA[Jonathan]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Sepúlveda]]></surname>
<given-names><![CDATA[Rossana]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad de Santiago de Chile Departamento de Ingeniería Metalúrgica Facultad de Ingeniería]]></institution>
<addr-line><![CDATA[Santiago ]]></addr-line>
<country>Chile</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad de Atacama Departamento de Ingeniería en Metalurgia ]]></institution>
<addr-line><![CDATA[Copiapó ]]></addr-line>
<country>Chile</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2020</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2020</year>
</pub-date>
<volume>87</volume>
<numero>213</numero>
<fpage>85</fpage>
<lpage>90</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S0012-73532020000200085&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S0012-73532020000200085&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S0012-73532020000200085&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract The entrainment of the organic phase in the aqueous applied to typical solutions in a copper solvent extraction process was studied. The organic phase used is composed of the commercial extractant LIX 984-N diluted in Shellsol 2046 AR. The aqueous phase contains 6 g/L of Cu2+, at pH 2 and 20 ºC. The variables studied were: mixing speed of 400 to 1000 rpm; mixing time of 3 to 30 minutes; initial pH of the electrolyte 2, 3, and 4; percentage of extractant in the organic phase 10 to 30% v/v; and copper concentration in the aqueous phase 1 to 6 g/L. It was determined that the entrainment of the organic phase in the aqueous is determined by the physical properties of the phases in equilibrium and by the system&#8217;s hydrodynamics, and it is a phenomenon that involves the advancing speed of the interphase (or dispersion band) and the displacement speed of the organic drops.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen Se estudió el atrapamiento de fase orgánica en acuoso aplicado a soluciones típicas de un proceso de extracción por solventes de cobre. La fase orgánica empleada está compuesta por el extractante comercial LIX 984-N diluido en Shellsol 2046 AR. La fase acuosa contiene 6 g/L de Cu2+, pH 2 a 20 ºC. Las variables estudiadas fueron: velocidad de mezclamiento de 400 a 1000 rpm, tiempo de mezclado de 3 a 30 minutos, pH inicial del electrolito de 2, 3 y 4, porcentaje de extractante en fase orgánica de 10 a 30% v/v y concentración de cobre en fase acuosa de 1 a 6 g/L. Se determinó que el atrapamiento de fase orgánica en acuoso está determinado por las propiedades físicas de las fases en equilibrio y por la hidrodinámica del sistema, siendo un fenómeno que involucra a la velocidad de avance de la interfase (o banda de dispersión) y la velocidad de desplazamiento de las gotas de orgánico.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[phase entrainment]]></kwd>
<kwd lng="en"><![CDATA[solvent extraction]]></kwd>
<kwd lng="en"><![CDATA[drop diameter]]></kwd>
<kwd lng="en"><![CDATA[dispersion]]></kwd>
<kwd lng="es"><![CDATA[atrapamiento de fases]]></kwd>
<kwd lng="es"><![CDATA[extracción por solventes]]></kwd>
<kwd lng="es"><![CDATA[diámetro de gotas]]></kwd>
<kwd lng="es"><![CDATA[dispersión]]></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[Asghari]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Safarzadeh]]></surname>
<given-names><![CDATA[M.S.]]></given-names>
</name>
<name>
<surname><![CDATA[Asghari]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Moradkham]]></surname>
<given-names><![CDATA[D]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The effect of impurities on the extraction of copper from sulfate medium using LIX®984N in kerosene]]></article-title>
<source><![CDATA[Russian Journal of Non-Ferrous Metals]]></source>
<year>2009</year>
<volume>50</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>89-96</page-range></nlm-citation>
</ref>
<ref id="B2">
<label>[2]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Donegan]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Direct solvent extraction of nickel at Bulong operations]]></article-title>
<source><![CDATA[Minerals Engineering]]></source>
<year>2006</year>
<volume>19</volume>
<numero>12</numero>
<issue>12</issue>
<page-range>1234-45</page-range></nlm-citation>
</ref>
<ref id="B3">
<label>[3]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Araneda]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Basualto]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Sapag]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Tapia]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Cotorás]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
<name>
<surname><![CDATA[Valenzuela]]></surname>
<given-names><![CDATA[F]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Uptake of copper (II) ions from acidic aqueous solutions using a continuous column packed with microcapsules containing a &#946;-hydroxyoximic compound]]></article-title>
<source><![CDATA[Chemical Engineering Research and Design]]></source>
<year>2011</year>
<volume>89</volume>
<numero>12</numero>
<issue>12</issue>
<page-range>2761-9</page-range></nlm-citation>
</ref>
<ref id="B4">
<label>[4]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Da Silveira]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
<name>
<surname><![CDATA[Gutierrez]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Rodrigues de Lemos]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Barbosa]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Dias]]></surname>
<given-names><![CDATA[G]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Hydrometallurgical separation of copper and cobalt from lithium-ion batteries using aqueous two-phase systems]]></article-title>
<source><![CDATA[Hydrometallurgy]]></source>
<year>2017</year>
<volume>169</volume>
<page-range>245-52</page-range></nlm-citation>
</ref>
<ref id="B5">
<label>[5]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Huang]]></surname>
<given-names><![CDATA[T.]]></given-names>
</name>
<name>
<surname><![CDATA[Wang]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Hu]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Hu]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Luo]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Liu]]></surname>
<given-names><![CDATA[S]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Phase separation in solvent extraction of cobalt from acidic sulfate solution using synergistic mixture containing dinonylnaphthalene sulfonic acid and 2-ethylhexyl 4-pyridinecarboxylate ester]]></article-title>
<source><![CDATA[Trans. Nonferrous Met. Soc. China]]></source>
<year>2019</year>
<volume>29</volume>
<page-range>1107-16</page-range></nlm-citation>
</ref>
<ref id="B6">
<label>[6]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Barnard]]></surname>
<given-names><![CDATA[K.R.]]></given-names>
</name>
<name>
<surname><![CDATA[Turner]]></surname>
<given-names><![CDATA[N.L]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The effect of temperature on hydroxyoxime stability in the LIX 63 - Versatic 10 - tributyl phosphate synergistic solvent extraction system under synthetic nickel laterite conditions]]></article-title>
<source><![CDATA[Hydrometallurgy]]></source>
<year>2011</year>
<volume>109</volume>
<numero>3-4</numero>
<issue>3-4</issue>
<page-range>245-51</page-range></nlm-citation>
</ref>
<ref id="B7">
<label>[7]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ning]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Cao]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Zhang]]></surname>
<given-names><![CDATA[Y]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Stability of the interfacial crud produced during the extraction of vanadium and chromium]]></article-title>
<source><![CDATA[Hydrometallurgy]]></source>
<year>2013</year>
<volume>133</volume>
<page-range>156-60</page-range></nlm-citation>
</ref>
<ref id="B8">
<label>[8]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zagorodnyaya]]></surname>
<given-names><![CDATA[A.N.]]></given-names>
</name>
<name>
<surname><![CDATA[Abisheva]]></surname>
<given-names><![CDATA[Z.S.]]></given-names>
</name>
<name>
<surname><![CDATA[Sadykanova]]></surname>
<given-names><![CDATA[S.E.]]></given-names>
</name>
<name>
<surname><![CDATA[Bobrova]]></surname>
<given-names><![CDATA[V.V.]]></given-names>
</name>
<name>
<surname><![CDATA[Sharipova]]></surname>
<given-names><![CDATA[A.S]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The characterization and origins of interphase substances (cruds) in the rhenium solvent extraction circuit of a copper smelter]]></article-title>
<source><![CDATA[Hydrometallurgy]]></source>
<year>2010</year>
<volume>104</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>308-12</page-range></nlm-citation>
</ref>
<ref id="B9">
<label>[9]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Liu]]></surname>
<given-names><![CDATA[X.]]></given-names>
</name>
<name>
<surname><![CDATA[Qiu]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Hu]]></surname>
<given-names><![CDATA[Y]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Degradation of Lix 984N and its effect on interfacial emulsion]]></article-title>
<source><![CDATA[J. Cent. South Univ. Technol]]></source>
<year>2006</year>
<volume>13</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>668-72</page-range></nlm-citation>
</ref>
<ref id="B10">
<label>[10]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Benavente]]></surname>
<given-names><![CDATA[O.]]></given-names>
</name>
<name>
<surname><![CDATA[Hernández]]></surname>
<given-names><![CDATA[M.C.]]></given-names>
</name>
<name>
<surname><![CDATA[Sagredo]]></surname>
<given-names><![CDATA[F]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Estimation and modeling of organic entrainment in aqueous solution (O/A) in laboratory tests of copper solvent extraction (SX) plant]]></article-title>
<source><![CDATA[Revista de Metalurgia]]></source>
<year>2013</year>
<volume>49</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>92-9</page-range></nlm-citation>
</ref>
<ref id="B11">
<label>[11]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Castillo]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Biela]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Navarro]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Study of phase separation in liquid-liquid systems using LIX984N in organic phase]]></article-title>
<source><![CDATA[Revista de Metalurgia]]></source>
<year>2012</year>
<volume>48</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>107-17</page-range></nlm-citation>
</ref>
<ref id="B12">
<label>[12]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Morgan]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Cashwell]]></surname>
<given-names><![CDATA[W.]]></given-names>
</name>
<name>
<surname><![CDATA[Doole]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Steeples]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Entrainment reduction at Freeport-McMoRan Copper &amp; Gold Morenci Operations]]></article-title>
<source><![CDATA[Solvent Extraction and Ion Exchange]]></source>
<year>2011</year>
<volume>29</volume>
<numero>5-6</numero>
<issue>5-6</issue>
<page-range>854-67</page-range></nlm-citation>
</ref>
<ref id="B13">
<label>[13]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Lovick]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Angeli]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Droplet size and velocity profiles in liquid-liquid horizontal flows]]></article-title>
<source><![CDATA[Chemical Engineering Science]]></source>
<year>2004</year>
<volume>59</volume>
<numero>15</numero>
<issue>15</issue>
<page-range>3105-15</page-range></nlm-citation>
</ref>
<ref id="B14">
<label>[14]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Miller]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Readett]]></surname>
<given-names><![CDATA[D]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Solvent extraction entrainment control needs and strategies]]></article-title>
<source><![CDATA[Proceedings of ALTA SX/IX]]></source>
<year>2003</year>
<page-range>1-24</page-range></nlm-citation>
</ref>
<ref id="B15">
<label>[15]</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Szymanowski]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
</person-group>
<source><![CDATA[Hydroxyoximes and copper hydrometallurgy]]></source>
<year>1993</year>
<publisher-name><![CDATA[CRC Press]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B16">
<label>[16]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Dopson]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Sundkvist]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Börje-Lindström]]></surname>
<given-names><![CDATA[E]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Toxicity of metal extraction and flotation chemicals to Sulfolobus metallicus and chalcopyrite bioleaching]]></article-title>
<source><![CDATA[Hydrometallurgy]]></source>
<year>2006</year>
<volume>81</volume>
<numero>3-4</numero>
<issue>3-4</issue>
<page-range>205-13</page-range></nlm-citation>
</ref>
<ref id="B17">
<label>[17]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Miller]]></surname>
<given-names><![CDATA[G.M.]]></given-names>
</name>
<name>
<surname><![CDATA[Readett]]></surname>
<given-names><![CDATA[D.J.]]></given-names>
</name>
<name>
<surname><![CDATA[Hutchinson]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Experience in operating the girilambone copper SX-EW plant in changing chemical environments]]></article-title>
<source><![CDATA[Minerals Engineering]]></source>
<year>1997</year>
<volume>10</volume>
<numero>5</numero>
<issue>5</issue>
<page-range>467-81</page-range></nlm-citation>
</ref>
<ref id="B18">
<label>[18]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Neira]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[O'Keefe]]></surname>
<given-names><![CDATA[T.J.]]></given-names>
</name>
<name>
<surname><![CDATA[Watson]]></surname>
<given-names><![CDATA[J.L]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Solvent extraction reagent entrainment effects on zinc electrowinning from waste oxide leach solutions]]></article-title>
<source><![CDATA[Minerals Engineering]]></source>
<year>1992</year>
<volume>5</volume>
<numero>3-5</numero>
<issue>3-5</issue>
<page-range>521-34</page-range></nlm-citation>
</ref>
<ref id="B19">
<label>[19]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sole]]></surname>
<given-names><![CDATA[K.C.]]></given-names>
</name>
<name>
<surname><![CDATA[Stewart]]></surname>
<given-names><![CDATA[R.J.]]></given-names>
</name>
<name>
<surname><![CDATA[Maluleke]]></surname>
<given-names><![CDATA[R.F.]]></given-names>
</name>
<name>
<surname><![CDATA[Rampersad]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Edward-Mavhungu]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Removal of entrained organic phase from zinc electrolyte: pilot plant comparison of CoMatrix and carbon filtration]]></article-title>
<source><![CDATA[Hydrometallurgy]]></source>
<year>2007</year>
<volume>89</volume>
<numero>1-2</numero>
<issue>1-2</issue>
<page-range>11-20</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[Bacon]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Mihaylov]]></surname>
<given-names><![CDATA[I]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Solvent extraction as an enabling technology in the nickel industry]]></article-title>
<source><![CDATA[The Journal of The South African Institute of Mining and Metallurgy]]></source>
<year>2002</year>
<volume>102</volume>
<numero>8</numero>
<issue>8</issue>
<page-range>435-43</page-range></nlm-citation>
</ref>
<ref id="B21">
<label>[21]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Burkhardt]]></surname>
<given-names><![CDATA[D.J]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Understanding wash efficiency and chloride transfer in copper solvent extraction]]></article-title>
<source><![CDATA[JOM]]></source>
<year>2003</year>
<volume>55</volume>
<numero>7</numero>
<issue>7</issue>
<page-range>34-7</page-range></nlm-citation>
</ref>
<ref id="B22">
<label>[22]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Kumar]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Hartland]]></surname>
<given-names><![CDATA[S]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Gravity settling in liquid/liquid dispersions]]></article-title>
<source><![CDATA[The Canadian Journal of Chemical Engineering]]></source>
<year>1985</year>
<volume>63</volume>
<numero>3</numero>
<issue>3</issue>
<page-range>368-76</page-range></nlm-citation>
</ref>
</ref-list>
</back>
</article>
