<?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>1815-5944</journal-id>
<journal-title><![CDATA[Ingeniería Mecánica]]></journal-title>
<abbrev-journal-title><![CDATA[Ingeniería Mecánica]]></abbrev-journal-title>
<issn>1815-5944</issn>
<publisher>
<publisher-name><![CDATA[Facultad de Ingeniería Mecánica. Instituto Superior Politécnico "José Antonio Echeverría"]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1815-59442019000200108</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Organización en capa de partículas de biomasa capilaroporosa durante el movimiento en espiral ascendente]]></article-title>
<article-title xml:lang="en"><![CDATA[Organization in layer form of porous biomass particles during ascending swirling movement]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Bombino-Matos]]></surname>
<given-names><![CDATA[Eugenio F.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Imbert-González]]></surname>
<given-names><![CDATA[Josué]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Arteaga-Linzán]]></surname>
<given-names><![CDATA[Ángel Rafael]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Cantos-Macías]]></surname>
<given-names><![CDATA[Manuel A.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Silva-Lora]]></surname>
<given-names><![CDATA[Electo E.]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad de Oriente Facultad de Ingeniería Mecánica e Industrial ]]></institution>
<addr-line><![CDATA[ Santiago de Cuba]]></addr-line>
<country>Cuba</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad Técnica de Manabí  ]]></institution>
<addr-line><![CDATA[Portoviejo ]]></addr-line>
<country>Ecuador</country>
</aff>
<aff id="Af3">
<institution><![CDATA[,Universidad Federal de Itajubá  ]]></institution>
<addr-line><![CDATA[ Minas Gerais]]></addr-line>
<country>Brazil</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>08</month>
<year>2019</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>08</month>
<year>2019</year>
</pub-date>
<volume>22</volume>
<numero>2</numero>
<fpage>108</fpage>
<lpage>114</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_arttext&amp;pid=S1815-59442019000200108&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_abstract&amp;pid=S1815-59442019000200108&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_pdf&amp;pid=S1815-59442019000200108&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen Durante el movimiento de biomasa capilaroporosa, dentro de una llamada Columna para Movimiento en Espiral Ascendente, las partículas se organizaron en forma de una capa debido a la acción de la fuerza centrífuga. El objetivo fue determinar el espesor de la capa de material, que se visualiza, a través de una llamada zona activa de flujo. Los valores de velocidad del aire y caídas de presión se obtuvieron experimentalmente y a través de imágenes, procesadas mediante el programa Particle Image Velocimetry for MATLAB (PIV) se determinó la velocidad de las partículas. Posteriormente, mediante comparaciones con resultados de simulaciones, se determinaron la porosidad y el espesor correspondientes de la capa de partículas formada en cada caso yse dedujo, analíticamente, la ecuación general para determinar el espesor de la capa de partículas formada durante este tipo de movimiento.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract During the movement of capillary biomass, within a called Column for Upward Spiral Movement, the particles pile up in the form of a layer due to the action of the centrifugal force. The objective was to determine the thickness of material layer that was visualized, through a called active flow Zone. The air speed and pressure drop values were experimentally obtained, and trough images, processing by Particle Image Velocimetry for MATLAB (PIV) program, was determined the particles velocity. Subsequently, by comparison with simulations values, were determined the porosity and thickness corresponding to each formed particles layer and was analytically deduced the general equation to determine the thickness of the particles layer formed during this kind of movement.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[movimiento en espiral ascendente]]></kwd>
<kwd lng="es"><![CDATA[cámara rotatoria fluidizada]]></kwd>
<kwd lng="es"><![CDATA[unidad de vórtice gas-sólido]]></kwd>
<kwd lng="en"><![CDATA[ascending swirling movement]]></kwd>
<kwd lng="en"><![CDATA[rotating fluidized bed]]></kwd>
<kwd lng="en"><![CDATA[gas-solid vortex unit]]></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[Abdel-Aziz]]></surname>
<given-names><![CDATA[MH]]></given-names>
</name>
<name>
<surname><![CDATA[El-Abd]]></surname>
<given-names><![CDATA[MZ]]></given-names>
</name>
<name>
<surname><![CDATA[Bassyouni]]></surname>
<given-names><![CDATA[M]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Heat and mass transfer in three phases fluidized bed containing high density particles at high gas velocities]]></article-title>
<source><![CDATA[International Journal of Thermal Sciences]]></source>
<year>2016</year>
<numero>102</numero>
<issue>102</issue>
<page-range>145-53</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[Agbor]]></surname>
<given-names><![CDATA[E]]></given-names>
</name>
<name>
<surname><![CDATA[Zhang]]></surname>
<given-names><![CDATA[X]]></given-names>
</name>
<name>
<surname><![CDATA[Kumar]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A review of biomass co-firing in North America]]></article-title>
<source><![CDATA[Renewable and Sustainable Energy Reviews]]></source>
<year>2014</year>
<numero>40</numero>
<issue>40</issue>
<page-range>930-43</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[De Wilde]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Gas-solid fluidized beds in vortex chambers]]></article-title>
<source><![CDATA[Chemical Engineering and Processing]]></source>
<year>2014</year>
<numero>85</numero>
<issue>85</issue>
<page-range>256-90</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[De Wilde]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[Richards]]></surname>
<given-names><![CDATA[G]]></given-names>
</name>
<name>
<surname><![CDATA[Benyahia]]></surname>
<given-names><![CDATA[S]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Qualitative numerical study of simultaneous high-G-intensified gas-solids contact, separation and segregation in a bi-disperse rotating fluidized bed in a vortex chamber]]></article-title>
<source><![CDATA[Advanced Powder Technology]]></source>
<year>2016</year>
<numero>27</numero>
<issue>27</issue>
<page-range>1453-63</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[Chokphoemphun]]></surname>
<given-names><![CDATA[S]]></given-names>
</name>
<name>
<surname><![CDATA[Chokphoemphun]]></surname>
<given-names><![CDATA[S]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Moisture content prediction of paddy drying in a fluidized-bed dryer with a vortex flow generator using an artificial neural network]]></article-title>
<source><![CDATA[Applied Thermal Engineering]]></source>
<year>2018</year>
<numero>145</numero>
<issue>145</issue>
<page-range>630-6</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[Eliaers]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
<name>
<surname><![CDATA[Broqueville]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[Poortinga]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[High-G, low-temperature coating of cohesive particles in a vortex chamber]]></article-title>
<source><![CDATA[Powder technology]]></source>
<year>2014</year>
<numero>258</numero>
<issue>258</issue>
<page-range>242-51</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[Dening]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[Océane]]></surname>
<given-names><![CDATA[C]]></given-names>
</name>
<name>
<surname><![CDATA[Jianghong]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Fluidization and drying of biomass particles in a vibrating fluidized bed with pulsed gas flow]]></article-title>
<source><![CDATA[Fuel Processing Technology]]></source>
<year>2015</year>
<numero>138</numero>
<issue>138</issue>
<page-range>471-82</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[Dening]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[Xiaotao]]></surname>
<given-names><![CDATA[B]]></given-names>
</name>
<name>
<surname><![CDATA[Jim]]></surname>
<given-names><![CDATA[LC]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Biomass drying in a pulsed fluidized bed without inert bed particles]]></article-title>
<source><![CDATA[Fuel]]></source>
<year>2016</year>
<numero>186</numero>
<issue>186</issue>
<page-range>270-84</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[Weber]]></surname>
<given-names><![CDATA[JM]]></given-names>
</name>
<name>
<surname><![CDATA[Stehle]]></surname>
<given-names><![CDATA[RC]]></given-names>
</name>
<name>
<surname><![CDATA[Breault]]></surname>
<given-names><![CDATA[RW]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Experimental study of the application of rotating fluidized beds to particle separation]]></article-title>
<source><![CDATA[Powder Technology]]></source>
<year>2017</year>
<numero>316</numero>
<issue>316</issue>
<page-range>123-30</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[Ibrahim]]></surname>
<given-names><![CDATA[KA]]></given-names>
</name>
<name>
<surname><![CDATA[Mofreh]]></surname>
<given-names><![CDATA[H]]></given-names>
</name>
<name>
<surname><![CDATA[Hamed]]></surname>
<given-names><![CDATA[WA]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Swirling gas-solid flow through pneumatic conveying dryer]]></article-title>
<source><![CDATA[Powder Technol]]></source>
<year>2013</year>
<numero>235</numero>
<issue>235</issue>
<page-range>500-15</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[Bombino]]></surname>
<given-names><![CDATA[EF]]></given-names>
</name>
<name>
<surname><![CDATA[Pineda]]></surname>
<given-names><![CDATA[RE]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Simulación del secado neumático de biomasa con movimiento en espiral ascendente]]></article-title>
<source><![CDATA[Ingeniería Mecánica]]></source>
<year>2017</year>
<volume>20</volume>
<numero>3</numero>
<issue>3</issue>
<page-range>107-14</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[Friedle]]></surname>
<given-names><![CDATA[M]]></given-names>
</name>
<name>
<surname><![CDATA[Niyogi]]></surname>
<given-names><![CDATA[K]]></given-names>
</name>
<name>
<surname><![CDATA[Torregrosa]]></surname>
<given-names><![CDATA[MM]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A drag model for the gas-solid vortex unit]]></article-title>
<source><![CDATA[Powder Technology]]></source>
<year>2017</year>
<numero>312</numero>
<issue>312</issue>
<page-range>210-21</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[Friedle]]></surname>
<given-names><![CDATA[M]]></given-names>
</name>
<name>
<surname><![CDATA[Marin]]></surname>
<given-names><![CDATA[GB]]></given-names>
</name>
<name>
<surname><![CDATA[Heynderickx]]></surname>
<given-names><![CDATA[GJ]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Operational range of a Gas-Solid Vortex Unit]]></article-title>
<source><![CDATA[Powder Technology]]></source>
<year>2018</year>
<numero>338</numero>
<issue>338</issue>
<page-range>702-15</page-range></nlm-citation>
</ref>
</ref-list>
</back>
</article>
