<?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>2223-4861</journal-id>
<journal-title><![CDATA[Centro Azúcar]]></journal-title>
<abbrev-journal-title><![CDATA[cen. az.]]></abbrev-journal-title>
<issn>2223-4861</issn>
<publisher>
<publisher-name><![CDATA[Editorial Feijóo]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S2223-48612019000200089</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[INFLUENCIA DE LOS PROCESOS OXIDATIVOS AVANZADOS EN LA DIGESTIÓN ANAEROBIA DE AGUAS RESIDUALES DE LA INDUSTRIA DEL CAFÉ]]></article-title>
<article-title xml:lang="en"><![CDATA[INFLUENCE OF ADVANCED OXIDATIVE PROCESSES IN ANAEROBIA DIGESTION OF WASTEWATER IN COFFEE INDUSTRY]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Córdova Mosquera]]></surname>
<given-names><![CDATA[Alexandra]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Gómez-Salcedo]]></surname>
<given-names><![CDATA[Yunet]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Riera]]></surname>
<given-names><![CDATA[María Antonieta]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Rodríguez-Díaz]]></surname>
<given-names><![CDATA[Joan Manuel]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Pereda-Reyes]]></surname>
<given-names><![CDATA[Ileana]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad Técnica de Manabí Facultad de Ciencias Matemáticas Físicas y Químicas ]]></institution>
<addr-line><![CDATA[ Portoviejo]]></addr-line>
<country>Ecuador</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad Técnica de Manabí Instituto de Investigación Laboratorio de Análisis Químicos y Biotecnológicos ]]></institution>
<addr-line><![CDATA[ Portoviejo]]></addr-line>
<country>Ecuador</country>
</aff>
<aff id="Af3">
<institution><![CDATA[,Universidad Tecnológica de La Habana José Antonio Echeverría, CUJAE Centro de Estudios de Ingeniería de Procesos (CIPRO) ]]></institution>
<addr-line><![CDATA[Marianao La Habana]]></addr-line>
<country>Cuba</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2019</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2019</year>
</pub-date>
<volume>46</volume>
<numero>2</numero>
<fpage>89</fpage>
<lpage>100</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_arttext&amp;pid=S2223-48612019000200089&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_abstract&amp;pid=S2223-48612019000200089&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_pdf&amp;pid=S2223-48612019000200089&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[RESUMEN La producción de café soluble genera un gran volumen de aguas residuales, cuyo tratamiento mediante digestión anaerobia (DA) se dificulta debido a que presentan en su composición sustancias recalcitrantes como polifenoles y taninos. Algunos estudios proponen tratamientos para estos efluentes, pero no apuntan a la eliminación de estos compuestos recalcitrantes. La aplicación de procesos oxidativos avanzados (POA), puede tener influencia en la reducción de la demanda química de oxígeno (DQO) y del carbono orgánico total. También puede reducir o eliminar compuestos tóxicos, inhibitorios o refractarios. Esta investigación tiene como objetivo determinar la incidencia de la fotocatálisis homogénea con H2O2 y radiación ultravioleta, como pretratamiento a la digestión anaerobia para la reducción de taninos presentes en aguas sintéticas de la industria del café soluble. Para evaluar el efecto POA se determinó el potencial bioquímico de metano (BMP) del residual, se caracterizó el inóculo empleado en función de los sólidos suspendidos volátiles (SSV) y su incidencia en el rendimiento de metano. Los ensayos se efectuaron a temperaturas mesofílica (35ºC ± 2ºC) y termofílica (55ºC ± 2ºC), con cargas orgánicas de 0,2 y 0,35 gDQO/gSSV. Se constató que el pretratamiento no afectó el valor de la DQO del agua sintética, sin embargo, se alcanza un porcentaje de reducción de taninos del 70,53 %. Al comparar los rendimientos de metano y reducción de la DQO obtenidos en el BMP con y sin POA, evaluados con iguales cargas orgánicas y régimen de temperatura, se constató que no se producen mejoras significativas en el proceso.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[ABSTRACT The production of soluble coffee generates a large volume of wastewater, whose treatment by anaerobic digestion (AD) is difficult because they have recalcitrant substances in their composition such as polyphenols and tannins. Some studies propose treatments for these effluents, but they do not point to the elimination of these recalcitrant compounds. The application of advanced oxidative processes (POA) can influence the reduction of chemical oxygen demand (COD) and total organic carbon. It can also reduce or eliminate toxic, inhibitory or refractory compounds. The objective of this research is to determine the incidence of homogeneous photocatalysis with H2O2 and ultraviolet radiation, as a pretreatment to anaerobic digestion for the reduction of tannins present in synthetic waters of the soluble coffee industry. To evaluate the POA effect, the biochemical potential of methane (BMP) was determined, the inoculum used as a function of volatile suspended solids (SSV) was characterized and its incidence on methane yield. The tests were carried out at mesophilic (35ºC ± 2ºC) and thermophilic (55ºC ± 2ºC) temperatures, with organic loads of 0.2 and 0.35 gDQO/gSSV. It was found that the pretreatment did not affect the COD value of the synthetic water, however a percentage of tannin reduction of 70.53% was reached. When comparing the methane yields and COD reduction obtained in the BMP with and without POA, evaluated with the same organic loads and temperature regime, it was found that there are no significant improvements in the process.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[aguas residuales]]></kwd>
<kwd lng="es"><![CDATA[café instantáneo]]></kwd>
<kwd lng="es"><![CDATA[inhibición]]></kwd>
<kwd lng="es"><![CDATA[potencial bioquímico de metano]]></kwd>
<kwd lng="es"><![CDATA[procesos oxidativos avanzados]]></kwd>
<kwd lng="en"><![CDATA[wastewater]]></kwd>
<kwd lng="en"><![CDATA[instant coffee]]></kwd>
<kwd lng="en"><![CDATA[inhibition]]></kwd>
<kwd lng="en"><![CDATA[biochemical methane potential]]></kwd>
<kwd lng="en"><![CDATA[advanced oxidative processes]]></kwd>
</kwd-group>
</article-meta>
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