<?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>2224-6185</journal-id>
<journal-title><![CDATA[Tecnología Química]]></journal-title>
<abbrev-journal-title><![CDATA[RTQ]]></abbrev-journal-title>
<issn>2224-6185</issn>
<publisher>
<publisher-name><![CDATA[Universidad de Oriente]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S2224-61852021000300580</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Estudio preliminar de la pirolisis de bagazo de caña con catálisis in situ]]></article-title>
<article-title xml:lang="en"><![CDATA[Preliminary study of sugarcane bagasse pyrolysis with in situ catalysis]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Guerrero-Haber]]></surname>
<given-names><![CDATA[José Ramón]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Giralt-Ortega]]></surname>
<given-names><![CDATA[Giselle]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Basilé-Maceo]]></surname>
<given-names><![CDATA[Victor Ramón]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Serret-Guasch]]></surname>
<given-names><![CDATA[Nurian]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Penedo-Medina]]></surname>
<given-names><![CDATA[Margarita]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad de Oriente Facultad de Ingeniería Química y Agronomía ]]></institution>
<addr-line><![CDATA[Santiago de Cuba ]]></addr-line>
<country>Cuba</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>12</month>
<year>2021</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>12</month>
<year>2021</year>
</pub-date>
<volume>41</volume>
<numero>3</numero>
<fpage>580</fpage>
<lpage>594</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_arttext&amp;pid=S2224-61852021000300580&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_abstract&amp;pid=S2224-61852021000300580&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_pdf&amp;pid=S2224-61852021000300580&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[RESUMEN Este trabajo muestra los resultados del estudio preliminar de pirolisis de bagazo de caña con catálisis in situ, realizado en una instalación experimental con horno de cama fija. La biomasa fue sometida a análisis granulométrico e inmediato, resultando un contenido de 24,36 % de humedad, 77,03 % de materia volátil, 2,91 % de cenizas y 1,29 % de carbono fijo; el diámetro de partícula promedio fue de 1,2 mm. Se analizó la influencia de la dosis del catalizador C-1, en proporciones de 10 y 20 %, en el rendimiento de los productos de pirolisis. Las condiciones experimentales fueron: masa de la biomasa alimentada al reactor de 18 g, velocidad de calentamiento 30 ºC/min, tiempo de permanencia de la biomasa en el reactor 30 min, temperatura en el reactor 500 ºC; el proceso se desarrolló a una presión absoluta de 81,71 kPa. El mayor rendimiento de líquidos se obtuvo cuando la biomasa se combinó con un 10 % de catalizador C1, siendo el mismo de 41 % (base húmeda). El mayor rendimiento de gases se obtuvo cuando se pirolizó el bagazo sin presencia de catalizador. Por análisis cualitativo se comprobó que los líquidos productos de la pirolisis, con y sin catalizador, evidenciaron la presencia de fenoles y enoles, aldehídos y compuestos carbonilos. La determinación de las propiedades químicas del carbón obtenido mostró que con el uso de catalizador disminuyó el contenido compuestos volátiles, lo cual concuerda con el mayor rendimiento obtenido de productos volátiles en presencia de catalizador.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[ ABSTRACT This work shows the results of the preliminary study of sugarcane bagasse pyrolysis with in situ catalysis, carried out in an experimental installation with a fixed bed oven. The biomass was subjected to granulometric and immediate analysis, resulting in a content of 24,36 % of moisture, 77,03 % of volatile matter, 2,91% of ashes and 1,29% of fixed carbon; the average particle diameter was 1.2 mm. The influence of the dose of catalyst C-1, in proportions of 10 and 20 %, on the yield of the pyrolysis products was analyzed. The experimental conditions were: mass of the biomass fed to the reactor of 18 g, heating rate 30 °C / min, residence time of the biomass in the reactor 30 min, temperature in the reactor 500 °C; the process was developed at an absolute pressure of 81,71 kPa. The highest liquid yield was obtained when the biomass was combined with 10 % of catalyst C1, the same being 41% (wet basis). The highest gas yield was obtained when the bagasse was pyrolyzed without the presence of catalyst. By qualitative analysis it was found that the liquid products of pyrolysis, with and without catalyst, evidenced the presence of phenols and enols, aldehydes and carbonyl compounds. The determination of the chemical properties of the carbon obtained showed that with the use of catalyst the content of volatile compounds decreased, which is consistent with the higher yield obtained from volatile products in the presence of catalyst.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[pirolisis in situ]]></kwd>
<kwd lng="es"><![CDATA[catálisis]]></kwd>
<kwd lng="es"><![CDATA[bagazo de caña]]></kwd>
<kwd lng="en"><![CDATA[in situ pyrolysis]]></kwd>
<kwd lng="en"><![CDATA[catalysis]]></kwd>
<kwd lng="en"><![CDATA[sugarcane bagasse]]></kwd>
</kwd-group>
</article-meta>
</front><back>
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