<?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>1993-8012</journal-id>
<journal-title><![CDATA[Minería y Geología]]></journal-title>
<abbrev-journal-title><![CDATA[Min. Geol.]]></abbrev-journal-title>
<issn>1993-8012</issn>
<publisher>
<publisher-name><![CDATA[EDUM. Universidad de Moa]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1993-80122022000400346</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Modelación matemática del secado de menas lateríticas de Ni en un horno cilíndrico rotatorio a escala semindustrial]]></article-title>
<article-title xml:lang="en"><![CDATA[Mathematical modeling of Ni-lateritic ore drying in a rotary cylindrical kiln on a semi-industrial scale]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Zalazar-Oliva]]></surname>
<given-names><![CDATA[Carlos]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Góngora-Leyva]]></surname>
<given-names><![CDATA[Ever]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Legrá-Lobaina]]></surname>
<given-names><![CDATA[Arístides A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[León-Segovia]]></surname>
<given-names><![CDATA[Marco A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[León-Segovia]]></surname>
<given-names><![CDATA[Manuel A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Laurencio-Alfonso]]></surname>
<given-names><![CDATA[Héctor L.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad de Moa  ]]></institution>
<addr-line><![CDATA[ Holguín]]></addr-line>
<country>Cuba</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Bindura University of Science and Education  ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Zimbabwe</country>
</aff>
<aff id="Af3">
<institution><![CDATA[,Universidad Técnica de Cotopaxi  ]]></institution>
<addr-line><![CDATA[ Latacunga]]></addr-line>
<country>Ecuador</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>12</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>12</month>
<year>2022</year>
</pub-date>
<volume>38</volume>
<numero>4</numero>
<fpage>346</fpage>
<lpage>362</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_arttext&amp;pid=S1993-80122022000400346&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_abstract&amp;pid=S1993-80122022000400346&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_pdf&amp;pid=S1993-80122022000400346&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[RESUMEN El desconocimiento de la relación existente entre las variables que caracterizan el proceso de secado térmico impide alcanzar los valores requeridos de humedad en la mena laterítica de Ni a la salida del cilindro horizontal rotatorio, a escala semindustrial, con el menor consumo de combustible posible y el menor impacto sobre el medioambiente. Por tal motivo, se estableció un modelo fenomenológico en estado estacionario, constituido por: un sistema de ecuaciones diferenciales y ecuaciones ordinarias obtenidas a partir de los balances de masa y de energía en la mena, en el gas y en la pared del secador; las ecuaciones de enlace que permiten obtener las propiedades termofísicas de la mena y de los gases; así como los coeficientes de transferencia de calor y masa que intervienen en el proceso, resuelto a través del método numérico Runger-Kutta de cuarto orden. El modelo permite establecer el comportamiento de la distribución de la temperatura del gas, de la mena y la variación de la humedad de esta última en toda la longitud del cilindro.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[ABSTRACT The lack of knowledge about the relationship between variables that characterize the thermal drying process prevents reaching the required moisture values in the Ni-lateritic ore at the exit of the rotating horizontal cylinder on a semi-industrial scale, with lowest possible fuel consumption and least impact on environment. For this reason, a steady state phenomenological model was established. This model consists of a system of differential equations and ordinary equations obtained from the mass and energy balances in the Ni-laterites ore, in the gas and in the wall of the dryer. Besides, from the bond equations that allow obtaining the thermophysical properties of the Ni-ore laterites and gases and the heat and mass transfer coefficients involved in the process, solved by using the fourth order Runger-Kutta numerical method. This model allows establishing the distribution temperature behavior of the gas, the Ni-laterites ore and the variation of moisture of the last one along the entire cylinder length.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[modelación matemática]]></kwd>
<kwd lng="es"><![CDATA[secado térmico]]></kwd>
<kwd lng="es"><![CDATA[mena laterítica de Ni]]></kwd>
<kwd lng="es"><![CDATA[cilindro horizontal rotatorio]]></kwd>
<kwd lng="es"><![CDATA[balance de energía]]></kwd>
<kwd lng="en"><![CDATA[mathematical modeling]]></kwd>
<kwd lng="en"><![CDATA[thermal drying]]></kwd>
<kwd lng="en"><![CDATA[lateritic Ni-ore]]></kwd>
<kwd lng="en"><![CDATA[rotating horizontal cylinder]]></kwd>
<kwd lng="en"><![CDATA[energy balance]]></kwd>
</kwd-group>
</article-meta>
</front><back>
<ref-list>
<ref id="B1">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Abbasfard]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Rafsanjani]]></surname>
<given-names><![CDATA[H. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Ghader]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Ghanbari]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Mathematical modeling and simulation of an industrial rotary dryer: a case study of ammonium nitrate plant]]></article-title>
<source><![CDATA[Powder technology]]></source>
<year>2013</year>
<volume>239</volume>
<page-range>499-505</page-range></nlm-citation>
</ref>
<ref id="B2">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Agustini]]></surname>
<given-names><![CDATA[S. S.]]></given-names>
</name>
</person-group>
<source><![CDATA[Regenerative action of the wall on the heat transfer for directly and indirectly heated rotary kilns]]></source>
<year>2006</year>
<publisher-name><![CDATA[Universität Magdeburg]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B3">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Arruda]]></surname>
<given-names><![CDATA[E. B.]]></given-names>
</name>
</person-group>
<source><![CDATA[Comparison of the performance of the roto-fluidized dryer and conventional rotary dryer]]></source>
<year>2008</year>
<publisher-name><![CDATA[Federal University of Uberlândia]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B4">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Cao]]></surname>
<given-names><![CDATA[W. F.]]></given-names>
</name>
<name>
<surname><![CDATA[Langrish]]></surname>
<given-names><![CDATA[T. A. G.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The development and validation of a system model for a countercurrent cascading rotary dryer]]></article-title>
<source><![CDATA[Drying Technology]]></source>
<year>2000</year>
<volume>18</volume>
<numero>1-2</numero>
<issue>1-2</issue>
<page-range>99-115</page-range></nlm-citation>
</ref>
<ref id="B5">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Castaño]]></surname>
<given-names><![CDATA[L. F.]]></given-names>
</name>
<name>
<surname><![CDATA[Rubio]]></surname>
<given-names><![CDATA[F. R.]]></given-names>
</name>
<name>
<surname><![CDATA[Ortega]]></surname>
<given-names><![CDATA[M. G.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modelado de secaderos rotatorios en isocorriente]]></article-title>
<source><![CDATA[Revista Iberoamericana de automática e informática industrial]]></source>
<year>2009</year>
<volume>6</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>32-43</page-range></nlm-citation>
</ref>
<ref id="B6">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Douglas]]></surname>
<given-names><![CDATA[P. L.]]></given-names>
</name>
<name>
<surname><![CDATA[Kwade]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Lee]]></surname>
<given-names><![CDATA[P. L.]]></given-names>
</name>
<name>
<surname><![CDATA[Mallick]]></surname>
<given-names><![CDATA[S. K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Simulation of a rotary dryer for sugar crystalline]]></article-title>
<source><![CDATA[Drying Technology]]></source>
<year>1993</year>
<volume>11</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>129-55</page-range></nlm-citation>
</ref>
<ref id="B7">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Echeeri]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Maalmi]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Performance evaluation of a rotary dryer in both co-current and counter-current configurations]]></article-title>
<source><![CDATA[Journal of Thermal Engineering]]></source>
<year>2021</year>
<volume>7</volume>
<numero>14</numero>
<issue>14</issue>
<page-range>1945-57</page-range></nlm-citation>
</ref>
<ref id="B8">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Froment]]></surname>
<given-names><![CDATA[G. F.]]></given-names>
</name>
<name>
<surname><![CDATA[Bischoff]]></surname>
<given-names><![CDATA[K. B.]]></given-names>
</name>
</person-group>
<source><![CDATA[Chemical Reactor Analysis and Design]]></source>
<year>1990</year>
<publisher-loc><![CDATA[New York ]]></publisher-loc>
<publisher-name><![CDATA[John Wiley &amp; Sons]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B9">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Gorog]]></surname>
<given-names><![CDATA[J. P.]]></given-names>
</name>
<name>
<surname><![CDATA[Adams]]></surname>
<given-names><![CDATA[T. N.]]></given-names>
</name>
<name>
<surname><![CDATA[Brimacombe]]></surname>
<given-names><![CDATA[J. K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Regenerative heat transfer in rotary kilns]]></article-title>
<source><![CDATA[Metallurgical transactions B]]></source>
<year>1982</year>
<volume>13</volume>
<page-range>153-63</page-range></nlm-citation>
</ref>
<ref id="B10">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Goyal]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Bushra]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modelling and Simulation of Rotary Dryer for Wheat drying]]></article-title>
<source><![CDATA[Journal of Postharvest Technology]]></source>
<year>2018</year>
<volume>6</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>63-8</page-range></nlm-citation>
</ref>
<ref id="B11">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Harriot]]></surname>
<given-names><![CDATA[W. L. M. J. C. S. P.]]></given-names>
</name>
</person-group>
<source><![CDATA[Operaciones unitarias en ingeniería química]]></source>
<year>2007</year>
<edition>7ma</edition>
<publisher-loc><![CDATA[México D. F. ]]></publisher-loc>
<publisher-name><![CDATA[Mcgraw-Hill/Interamericana]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B12">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Mujumdar]]></surname>
<given-names><![CDATA[K. S.]]></given-names>
</name>
<name>
<surname><![CDATA[Ganesh]]></surname>
<given-names><![CDATA[K. V.]]></given-names>
</name>
<name>
<surname><![CDATA[Kulkarni]]></surname>
<given-names><![CDATA[S. B.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Rotary Cement Kiln Simulator (RoCKS): Integrated Modeling of Pre-Heater, Calciner, Kiln and Clinker Cooler]]></article-title>
<source><![CDATA[Chemical Engineering Science]]></source>
<year>2007</year>
<volume>62</volume>
<numero>9</numero>
<issue>9</issue>
<page-range>2590-607</page-range></nlm-citation>
</ref>
<ref id="B13">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Myklestad]]></surname>
<given-names><![CDATA[O.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Heat and Mass Transfer in Rotary Dryers]]></article-title>
<source><![CDATA[Chemical Engineering Progress Symposium Series]]></source>
<year>1963</year>
<volume>59</volume>
<numero>41</numero>
<issue>41</issue>
<page-range>129-37</page-range></nlm-citation>
</ref>
<ref id="B14">
<nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Nonhebel]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Moss]]></surname>
<given-names><![CDATA[A. A. H.]]></given-names>
</name>
</person-group>
<source><![CDATA[Drying of Solids in the Chemical Industry]]></source>
<year>1971</year>
<publisher-loc><![CDATA[London ]]></publisher-loc>
</nlm-citation>
</ref>
<ref id="B15">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Parra-Rosero]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
</person-group>
<source><![CDATA[Modelación de un proceso de secado de cacao utilizando una cámara rotatoria cilíndrica y flujo de aire caliente]]></source>
<year>2017</year>
<publisher-loc><![CDATA[Perú ]]></publisher-loc>
<publisher-name><![CDATA[Universidad de Piura]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B16">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Perazzini]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Perazzini]]></surname>
<given-names><![CDATA[M. T.]]></given-names>
</name>
<name>
<surname><![CDATA[Freire]]></surname>
<given-names><![CDATA[F. B.]]></given-names>
</name>
<name>
<surname><![CDATA[Freire]]></surname>
<given-names><![CDATA[F. B.]]></given-names>
</name>
<name>
<surname><![CDATA[Freire]]></surname>
<given-names><![CDATA[J. T.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modeling and cost analysis of drying of citrus residues as biomass in rotary dryer for bioenergy]]></article-title>
<source><![CDATA[Renewable Energy]]></source>
<year>2021</year>
<volume>175</volume>
<page-range>167-78</page-range></nlm-citation>
</ref>
<ref id="B17">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ponce De La Cruz]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Royo]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[García]]></surname>
<given-names><![CDATA[A. C.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modelo matemático de un secadero rotatorio: secado de biomasa sólida lignocelulósica]]></article-title>
<source><![CDATA[Revista Ingeniería Mecánica Tecnología y Desarrollo]]></source>
<year>2018</year>
<volume>6</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>031-43</page-range></nlm-citation>
</ref>
<ref id="B18">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Reay]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Theory in the Desing of Dryers]]></article-title>
<source><![CDATA[Chem. Eng.]]></source>
<year>1979</year>
<volume>5</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>501-6</page-range></nlm-citation>
</ref>
<ref id="B19">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sharples]]></surname>
<given-names><![CDATA[K.]]></given-names>
</name>
<name>
<surname><![CDATA[Glikin]]></surname>
<given-names><![CDATA[P. G.]]></given-names>
</name>
<name>
<surname><![CDATA[Warne]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Computer simulation of rotary dryers]]></article-title>
<source><![CDATA[Transactions of the Institute of Chemical Engineers]]></source>
<year>1964</year>
<volume>42</volume>
<page-range>275-84</page-range></nlm-citation>
</ref>
<ref id="B20">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Souza]]></surname>
<given-names><![CDATA[G. F. M. V.]]></given-names>
</name>
<name>
<surname><![CDATA[Avendaño]]></surname>
<given-names><![CDATA[P. S.]]></given-names>
</name>
<name>
<surname><![CDATA[Francisquetti]]></surname>
<given-names><![CDATA[M. C. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Ferreira]]></surname>
<given-names><![CDATA[F. R. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Duarte]]></surname>
<given-names><![CDATA[C. R.]]></given-names>
</name>
<name>
<surname><![CDATA[Barrozo]]></surname>
<given-names><![CDATA[M. A. S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modeling of heat and mass transfer in a non-conventional rotary dryer]]></article-title>
<source><![CDATA[Applied Thermal Engineering]]></source>
<year>2021</year>
<volume>182</volume>
<page-range>116-8</page-range></nlm-citation>
</ref>
<ref id="B21">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Yi]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Li]]></surname>
<given-names><![CDATA[X.]]></given-names>
</name>
<name>
<surname><![CDATA[He]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Duan]]></surname>
<given-names><![CDATA[X.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Drying efficiency and product quality of biomass drying: a review]]></article-title>
<source><![CDATA[Drying Technology]]></source>
<year>2020</year>
<volume>38</volume>
<numero>15</numero>
<issue>15</issue>
<page-range>2039-54</page-range></nlm-citation>
</ref>
<ref id="B22">
<nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zalazar-Oliva]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
</person-group>
<source><![CDATA[Modelación matemática del proceso de secado de mineral laterítico en secadores rotatorios]]></source>
<year>2021</year>
<publisher-loc><![CDATA[Cuba ]]></publisher-loc>
<publisher-name><![CDATA[Universidad de Moa]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B23">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zalazar-Oliva]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Góngora-Leyva]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<name>
<surname><![CDATA[Legrá-Lobaina]]></surname>
<given-names><![CDATA[A. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Retirado-Mediaceja]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Caneghem]]></surname>
<given-names><![CDATA[J. V.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Determinación del calor específico del mineral laterítico mediante el método de calorimetría diferencial de barrido]]></article-title>
<source><![CDATA[Minería y Geología]]></source>
<year>2021</year>
<volume>37</volume>
<numero>3</numero>
<issue>3</issue>
<page-range>318-32</page-range></nlm-citation>
</ref>
<ref id="B24">
<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zalazar-Oliva]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Góngora-Leyva]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<name>
<surname><![CDATA[Retirado-Mediaceja]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Sánchez-Escalona]]></surname>
<given-names><![CDATA[A. A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Determinación de la conductividad térmica de menas lateríticas a partir del método de Hot-Ball]]></article-title>
<source><![CDATA[Minería y Geología]]></source>
<year>2019</year>
<volume>35</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>419-29</page-range></nlm-citation>
</ref>
</ref-list>
</back>
</article>
