<?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>S0012-73532018000100169</article-id>
<article-id pub-id-type="doi">10.15446/dyna.v85n204.65601</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[CFD simulation of sugarcane bagasse combustion in an industrial grate boiler]]></article-title>
<article-title xml:lang="es"><![CDATA[Simulación en CFD de la combustión de bagazo de caña en una caldera industrial con parrilla]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Diaz-Mateus]]></surname>
<given-names><![CDATA[Fabian Andrey]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Alvarez-Castro]]></surname>
<given-names><![CDATA[Helver Crispiniano]]></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[,AC Ingeniería Virtual  ]]></institution>
<addr-line><![CDATA[Bucaramanga ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad Industrial de Santander  ]]></institution>
<addr-line><![CDATA[Bucaramanga ]]></addr-line>
<country>Colombia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>03</month>
<year>2018</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>03</month>
<year>2018</year>
</pub-date>
<volume>85</volume>
<numero>204</numero>
<fpage>169</fpage>
<lpage>176</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S0012-73532018000100169&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S0012-73532018000100169&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S0012-73532018000100169&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract The simulation of an industrial boiler in CFD (Computational Fluid Dynamics) is usually done by stages due to the extensive size and the different physical phenomena that occur in different locations of the equipment. In this work, the simulation of an industrial grate boiler is done in three stages, one for the primary air circuit, another one for the secondary air circuit and the final one is the furnace. The combustion of sugarcane bagasse is a complex phenomenon that involves moisture vaporization, devolatilization and char combustion, in order to account for those phenomena, bagasse particles were modeled in a Eulerian-Lagrangian approach. The simulations were performed in commercial software ANSYS FLUENT and the devolatilization model were programmed in C language as a User Defined Function (UDF). When the results of the simulations were compared with experimental data, a satisfactory agreement was observed. Simulations were performed with primary and secondary air inlets modifications in order to optimize the boiler performance, the results of those simulations showed significant improvement in the combustion parameters.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen La simulación de una caldera industrial en CFD se realiza, usualmente, por etapas debido al gran tamaño y a los diferentes fenómenos físicos que ocurren dentro del equipo. En este trabajo, la simulación de una caldera industrial de parrilla se realiza en tres etapas, la primera es el circuito de aire primario, la segunda es el circuito de aire secundario y la tercera corresponde a la caldera. La combustión de bagazo de caña es un fenómeno complejo que involucra vaporización de la humedad, devolatilización y combustión del carbón, de forma que para evaluar esos fenómenos las partículas de bagazo fueron modeladas en un marco Euleriano-Lagrangiano. Las simulaciones fueron desarrolladas en el software comercial ANSYS FLUENT y la tasa de devolatilización fue programada en lenguaje C como una función definida por el usuario. Cuando los resultados de las simulaciones se compararon con datos experimentales, se observó una concordancia satisfactoria. Se realizaron simulaciones con modificaciones en las entradas de aire primario y secundario buscando optimizar el funcionamiento de la caldera y los resultados de esas simulaciones presentaron una mejoría significativa en los parámetros de combustión.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[mathematical modeling]]></kwd>
<kwd lng="en"><![CDATA[numerical simulation]]></kwd>
<kwd lng="en"><![CDATA[biomass combustion]]></kwd>
<kwd lng="en"><![CDATA[discrete phase]]></kwd>
<kwd lng="es"><![CDATA[modelamiento matemático]]></kwd>
<kwd lng="es"><![CDATA[simulación numérica]]></kwd>
<kwd lng="es"><![CDATA[combustión de biomasa]]></kwd>
<kwd lng="es"><![CDATA[fase discreta]]></kwd>
</kwd-group>
</article-meta>
</front><back>
<ref-list>
<ref id="B1">
<label>[1]</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Alexandratos]]></surname>
<given-names><![CDATA[N.]]></given-names>
</name>
<name>
<surname><![CDATA[Bruinsma]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
</person-group>
<source><![CDATA[World agriculture towards 2030/2050: The 2012 revision]]></source>
<year>2012</year>
<publisher-name><![CDATA[FAO Agricultural Development Economics Division]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B2">
<label>[2]</label><nlm-citation citation-type="">
<source><![CDATA[Global Ethanol Production]]></source>
<year>2017</year>
</nlm-citation>
</ref>
<ref id="B3">
<label>[3]</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Kaewpradap]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Yoksenakul]]></surname>
<given-names><![CDATA[W.]]></given-names>
</name>
<name>
<surname><![CDATA[Jugjai]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<source><![CDATA[Effects of moisture content in simulated bagasse by equilibrium analysis]]></source>
<year></year>
<conf-name><![CDATA[ 4thTSME International Conference on Mechanical Engineering]]></conf-name>
<conf-date>October, 2013</conf-date>
<conf-loc> </conf-loc>
</nlm-citation>
</ref>
<ref id="B4">
<label>[4]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Shrivastav]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Hussain]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Design of bagasse dryer to recover energy of water tube boiler in a sugar factory]]></article-title>
<source><![CDATA[International Journal of Science and Research]]></source>
<year>2013</year>
<volume>2</volume>
<numero>8</numero>
<issue>8</issue>
<page-range>356-8</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[Centeno-Gonzáleza]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Silva-Lora]]></surname>
<given-names><![CDATA[E.D.]]></given-names>
</name>
<name>
<surname><![CDATA[Villa-Nova]]></surname>
<given-names><![CDATA[H.F.]]></given-names>
</name>
<name>
<surname><![CDATA[Mendes Neto]]></surname>
<given-names><![CDATA[L.J.]]></given-names>
</name>
<name>
<surname><![CDATA[Martínez-Reyes]]></surname>
<given-names><![CDATA[A.M.]]></given-names>
</name>
<name>
<surname><![CDATA[Ratner]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Ghamari]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[CFD modeling of combustion of sugarcane bagasse in an industrial boiler]]></article-title>
<source><![CDATA[Fuel]]></source>
<year>2017</year>
<numero>193</numero>
<issue>193</issue>
<page-range>31-8</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[Demirbas]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Potential applications of renewable energy sources, biomass combustion problems in boiler power systems and combustion related environmental issues]]></article-title>
<source><![CDATA[Prog. Energy Combust. Sci.]]></source>
<year>2005</year>
<numero>31</numero>
<issue>31</issue>
<page-range>171-92</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[Ferreira]]></surname>
<given-names><![CDATA[D.J.O.]]></given-names>
</name>
<name>
<surname><![CDATA[Sosa-Arnao]]></surname>
<given-names><![CDATA[J.H.]]></given-names>
</name>
<name>
<surname><![CDATA[Moreira]]></surname>
<given-names><![CDATA[B.C.]]></given-names>
</name>
<name>
<surname><![CDATA[Paes-Rangel]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Park]]></surname>
<given-names><![CDATA[S.W.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A comprehensive CFD model for sugar-cane bagasse heterogeneous combustion in a grate boiler system]]></article-title>
<source><![CDATA[International Journal of Chemical, Molecular, Nuclear, Materials and Metallurgical Engineering]]></source>
<year>2015</year>
<volume>9</volume>
<numero>5</numero>
<issue>5</issue>
<page-range>593-600</page-range></nlm-citation>
</ref>
<ref id="B8">
<label>[8]</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zahirovic]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Scharler]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Obernberger]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
</person-group>
<source><![CDATA[Advanced CFD modelling of pulverised biomass combustion]]></source>
<year>2006</year>
<conf-name><![CDATA[ Internat. Conf. Science in Thermal and Chemical Biomass Conversion]]></conf-name>
<conf-loc> </conf-loc>
<page-range>267-83</page-range></nlm-citation>
</ref>
<ref id="B9">
<label>[9]</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Jin]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Yan]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Higgins]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Liu]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
</person-group>
<source><![CDATA[CFD Modeling of biomass combustion for conversion application]]></source>
<year></year>
<conf-name><![CDATA[ NALCO Mobotec Clearwater Coal Conference]]></conf-name>
<conf-date>2011</conf-date>
<conf-loc> </conf-loc>
</nlm-citation>
</ref>
<ref id="B10">
<label>[10]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Aboyadea]]></surname>
<given-names><![CDATA[A.O.]]></given-names>
</name>
<name>
<surname><![CDATA[Hugo]]></surname>
<given-names><![CDATA[T.J.]]></given-names>
</name>
<name>
<surname><![CDATA[Carriera]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Meyer]]></surname>
<given-names><![CDATA[E.L.]]></given-names>
</name>
<name>
<surname><![CDATA[Stahl]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Knoetzea]]></surname>
<given-names><![CDATA[J.H.]]></given-names>
</name>
<name>
<surname><![CDATA[Görgens]]></surname>
<given-names><![CDATA[J.F.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Non-isothermal kinetic analysis of the devolatilization of corn cobs and sugarcane bagasse in an inert atmosphere]]></article-title>
<source><![CDATA[Thermochimica Acta]]></source>
<year>2011</year>
<numero>517</numero>
<issue>517</issue>
<page-range>81-9</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[Sánchez-Castro]]></surname>
<given-names><![CDATA[Z.]]></given-names>
</name>
<name>
<surname><![CDATA[Mendieta-Menjura]]></surname>
<given-names><![CDATA[O.A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber]]></article-title>
<source><![CDATA[Corpoica Cienc. Tecnol. Agropecu.]]></source>
<year>2014</year>
<volume>15</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>133-51</page-range></nlm-citation>
</ref>
<ref id="B12">
<label>[12]</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Smith]]></surname>
<given-names><![CDATA[J.D.]]></given-names>
</name>
</person-group>
<collab>Dept of Chemical Engineering</collab>
<source><![CDATA[Foundations of a three-dimensional model for predicting coal combustion characteristics in industrial power generation plants]]></source>
<year>1990</year>
<publisher-loc><![CDATA[Utah ]]></publisher-loc>
<publisher-name><![CDATA[Brigham Young University]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B13">
<label>[13]</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Yin]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Kaer]]></surname>
<given-names><![CDATA[S.K.]]></given-names>
</name>
<name>
<surname><![CDATA[Rosendahl]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Hvid]]></surname>
<given-names><![CDATA[S.L.]]></given-names>
</name>
</person-group>
<source><![CDATA[Modeling of pulverized coal and biomass co-firing in a 150 KW swirling stabilized burner and experimental validation]]></source>
<year></year>
<conf-name><![CDATA[ international conference on powder engineering-09. (ICOPE-09)]]></conf-name>
<conf-date>2009</conf-date>
<conf-loc>Kobe, Japan </conf-loc>
</nlm-citation>
</ref>
<ref id="B14">
<label>[14]</label><nlm-citation citation-type="book">
<source><![CDATA[ANSYS FLUENT User Manual]]></source>
<year></year>
<publisher-name><![CDATA[ANSYS Inc.]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B15">
<label>[15]</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Torresi]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Saponaro]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Camporeale]]></surname>
<given-names><![CDATA[S.M.]]></given-names>
</name>
<name>
<surname><![CDATA[Fortunato]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
</person-group>
<source><![CDATA[CFD analysis of the flow through tube banks of HRSG]]></source>
<year></year>
<conf-name><![CDATA[ ASME Turbo Expo 2008: Power for Land, Sea and Air]]></conf-name>
<conf-date>2008</conf-date>
<conf-loc> </conf-loc>
</nlm-citation>
</ref>
<ref id="B16">
<label>[16]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ergun]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Fluid flow through packed columns]]></article-title>
<source><![CDATA[Chem. Eng. Prog.]]></source>
<year>1952</year>
<volume>48</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>89-94</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[Tabet]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Gökalp]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Review on CFD based models for co-firing coal and biomass]]></article-title>
<source><![CDATA[Renewable and Sustainable Energy Reviews]]></source>
<year>2015</year>
<numero>51</numero>
<issue>51</issue>
<page-range>1101-14</page-range></nlm-citation>
</ref>
<ref id="B18">
<label>[18]</label><nlm-citation citation-type="confpro">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Magnussen]]></surname>
<given-names><![CDATA[B.F.]]></given-names>
</name>
<name>
<surname><![CDATA[Hjertager]]></surname>
<given-names><![CDATA[B.H.]]></given-names>
</name>
</person-group>
<source><![CDATA[On mathematical models of turbulent combustion with special emphasis on soot formation and combustion]]></source>
<year></year>
<conf-name><![CDATA[ 16thSymp. (Int&#8217;l.) on Combustion]]></conf-name>
<conf-date>1976</conf-date>
<conf-loc> </conf-loc>
</nlm-citation>
</ref>
<ref id="B19">
<label>[19]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Scharler]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Fleckl]]></surname>
<given-names><![CDATA[T.]]></given-names>
</name>
<name>
<surname><![CDATA[Obernberger]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Modification of a magnussen constant of the Eddy dissipation model for biomass grate furnaces by means of hot gas in-situ FT-IR absorption spectroscopy]]></article-title>
<source><![CDATA[Progress in Computational Fluid Dynamics]]></source>
<year>2003</year>
<volume>3</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>102-11</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[Miller]]></surname>
<given-names><![CDATA[R.S.]]></given-names>
</name>
<name>
<surname><![CDATA[Harstad]]></surname>
<given-names><![CDATA[K.]]></given-names>
</name>
<name>
<surname><![CDATA[Bellan]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Evaluation of equilibrium and non-equilibrium evaporation models for many droplet gas-liquid flow simulations]]></article-title>
<source><![CDATA[International Journal of Multiphase Flow]]></source>
<year>1998</year>
<volume>24</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>1025-55</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[Sazhin]]></surname>
<given-names><![CDATA[S.S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Advanced models of fuel droplet heating and evaporation]]></article-title>
<source><![CDATA[Progress in Energy and Combustion Science]]></source>
<year>2006</year>
<numero>32</numero>
<issue>32</issue>
<page-range>162-214</page-range><publisher-name><![CDATA[Elsevier Science]]></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[Baum]]></surname>
<given-names><![CDATA[M.M.]]></given-names>
</name>
<name>
<surname><![CDATA[Street]]></surname>
<given-names><![CDATA[P.J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Predicting the combustion behaviour of coal particles]]></article-title>
<source><![CDATA[Combust Sci Technol.]]></source>
<year>1971</year>
<numero>3</numero>
<issue>3</issue>
<page-range>231-43</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[Field]]></surname>
<given-names><![CDATA[M.A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Rate of combustion of size-graded fractions of char from a low-rank coal between 1200 K and 2000 K]]></article-title>
<source><![CDATA[Combust Flame]]></source>
<year>1969</year>
<numero>13</numero>
<issue>13</issue>
<page-range>237-52</page-range></nlm-citation>
</ref>
<ref id="B24">
<label>[24]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Luo]]></surname>
<given-names><![CDATA[M]]></given-names>
</name>
<name>
<surname><![CDATA[Stanmore]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The combustion characteristics of char from pulverized bagasse]]></article-title>
<source><![CDATA[Fuel]]></source>
<year>1992</year>
<volume>71</volume>
<numero>9</numero>
<issue>9</issue>
<page-range>1074-6</page-range></nlm-citation>
</ref>
<ref id="B25">
<label>[25]</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Li]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Paul]]></surname>
<given-names><![CDATA[M.C.]]></given-names>
</name>
<name>
<surname><![CDATA[Younger]]></surname>
<given-names><![CDATA[P.L.]]></given-names>
</name>
<name>
<surname><![CDATA[Watson]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
<name>
<surname><![CDATA[Hossain]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Welch]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Characterization of biomass combustion at high temperatures based on an upgraded single particle model]]></article-title>
<source><![CDATA[Applied Energy]]></source>
<year>2015</year>
<numero>156</numero>
<issue>156</issue>
<page-range>749-55</page-range></nlm-citation>
</ref>
</ref-list>
</back>
</article>
