<?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>0120-100X</journal-id>
<journal-title><![CDATA[Revista ION]]></journal-title>
<abbrev-journal-title><![CDATA[Rev. ion]]></abbrev-journal-title>
<issn>0120-100X</issn>
<publisher>
<publisher-name><![CDATA[Universidad Industrial de Santander]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0120-100X2021000100047</article-id>
<article-id pub-id-type="doi">10.18273/revion.v34n1-2021005</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[Eficiencia de un reactor SBR para la remoción de la materia orgánica presente en el agua residual de una industria de teñido de flores]]></article-title>
<article-title xml:lang="en"><![CDATA[Efficiency of an SBR reactor for the removal of the organic matter present in the wastewater of a flower dyeing industry]]></article-title>
<article-title xml:lang="pt"><![CDATA[Eficiência de um reator SBR para a remoção da matéria orgânica presente na água residual de uma indústria de tinturas de flores]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Restrepo]]></surname>
<given-names><![CDATA[Alfoncina]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[C. Rodríguez]]></surname>
<given-names><![CDATA[Diana]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[A. Peñuela]]></surname>
<given-names><![CDATA[Gustavo]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad de Antioquia Facultad de Ingeniería ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad de Antioquia Facultad de Ingeniería ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af3">
<institution><![CDATA[,Universidad de Antioquia Facultad de Ingeniería ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Colombia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2021</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2021</year>
</pub-date>
<volume>34</volume>
<numero>1</numero>
<fpage>47</fpage>
<lpage>59</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S0120-100X2021000100047&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S0120-100X2021000100047&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S0120-100X2021000100047&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen Se realizó la implementación de un reactor SBR (Sequencing Batch Reactor- por sus siglas en inglés y Reactor Secuencial en Discontinuo - en español) para la remoción de la materia orgánica presente en el agua residual de una empresa de teñido de flores. Se analizaron parámetros fisicoquímicos para evaluar la eficiencia del proceso y seguimiento de la biomasa mediante pruebas de sedimentabilidad y observaciones al microscopio. El sistema SBR fue operado usando una fase de llenado estática durante 2 h, una etapa de reacción durante 8 h (4 h de aireación y 4 h de mezcla) y finalmente una etapa de sedimentación durante 2 h, para un total de 12 horas por ciclo y 2 ciclos al día, y se evaluaron dos colorantes azo (C1 y C2) ampliamente usados en la industria del teñido de flores, variando temporalmente la concentración de la materia orgánica en términos de DQO con valores de 3,0 g /L.d y 7,0 g /L.d. Los resultados experimentales y el análisis estadístico permitió analizar el comportamiento del reactor SBR, concluyendo que ambos colorantes se comportaron estadísticamente iguales en la remoción del carbono orgánico total (COT), con un valor promedio de remoción 92,02% para C1 y 94,60% para C2 con una carga de 3,0 g DQO/L.d y 96,69% para C1 y 98,30% para C2 con una carga de 7,0 g DQO/L.d. La biomasa presentó un IVL bajo, indicando una buena sedimentabilidad tanto para los ensayos llevados a cabo con C1 como C2. Finalmente, los microorganismos identificados en la biomasa permitieron corroborar la eficiencia del sistema de tratamiento, dado que abundaron los rotíferos y ciliados fijos con C1 y ciliados libres con C2, los cuales son indicadores de una buena eficiencia en los procesos de tratamiento y a su vez, indicadores de edades de lodos elevadas, lo que contrasta con la edad de lodos empleada en este estudio (&#952;c = 15 d).]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract The implementation of an SBR reactor (Sequencing Batch Reactor- for its acronym in English and Sequential Reactor in Discontinuous- in Spanish) was carried out for the removal of organic matter present in the wastewater of a flower dyeing company. Physicochemical parameters were analyzed to evaluate the efficiency of the process and biomass monitoring through sedimentation tests and microscopic observations. The SBR system was operated using a static filling phase for 2 h, a reaction step for 8 h (4 h of aeration and 4 h of mixing) and finally a sedimentation step for 2 h, for a total of 12 hours per cycle and 2 cycles per day and two azo dyes (C1 and C2) widely used in the flower dyeing industry were evaluated, temporarily varying the concentration of organic matter in terms of COD with values of 3.0 g/L.d and 7.0 g/L.d The experimental results and statistical analysis allowed to analyze the behavior of the SBR reactor, concluding that both colorants behaved statistically the same in the removal of total organic carbon (TOC), with an average removal value of 92.02% for C1 and 94.60% for C2 with a loading of 3.0 g COD/L.d and 96.69% for C1 and 98.30% for C2 with a loading of 7.0 g COD/L.d The biomass presented a low SVI, indicating a good sedimentability for both the tests carried out with C1 and C2. Finally, the microorganisms identified in the biomass allowed to corroborate the efficiency of the treatment system, since rotifers and fixed ciliates with C1 and free ciliates with C2 abounded, which are indicators of good efficiency in the treatment processes and, in turn, high sludge age indicators, which contrasts with the sludge age used in this study (&#952;c = 15 d).]]></p></abstract>
<abstract abstract-type="short" xml:lang="pt"><p><![CDATA[Resumo Foi realizada a implantação de um reator SBR (Sequencing Batch Reactor- por sua sigla em inglês e Sequential Reactor em Discontinuous- em espanhol) para a remoção de matéria orgânica presente no efluente de uma empresa de tinturaria de flores. Parâmetros físico-químicos foram analisados para avaliação da eficiência do processo e monitoramento da biomassa por meio de testes de sedimentação e observações microscópicas. O sistema SBR foi operado usando uma fase de enchimento estático por 2 h, uma etapa de reação por 8 h (4 h de aeração e 4 h de mistura) e finalmente uma etapa de sedimentação por 2 h, para um total de 12 horas por ciclo e 2 Foram avaliados ciclos diários e dois corantes azo (C1 e C2) amplamente utilizados na indústria de tingimento de flores, variando temporariamente a concentração de matéria orgânica em termos de DQO com valores de 3,0 g/L.d e 7,0 g/L.d Os resultados experimentais e estatísticos a análise permitiu analisar o comportamento do reator SBR, concluindo que ambos os corantes se comportaram estatisticamente da mesma forma na remoção de carbono orgânico total (COT), com valor médio de remoção de 92,02% para C1 e 94,60% para C2 com carregamento de 3,0 g DQO/L.d e 96,69% para C1 e 98,30% para C2 com carregamento de 7,0 g DQO/L.d. A biomassa apresentou baixo SVI, indicando boa sedimentabilidade para ambos os testes realizados com C1 e C2. Por fim, os microrganismos identificados na biomassa permitiram corroborar a eficiência do sistema de tratamento, uma vez que abundaram rotíferos e ciliados fixos com C1 e ciliados livres com C2, que são indicadores de boa eficiência nos processos de tratamento e, por sua vez, elevada idade do lodo. indicadores, o que contrasta com a idade do lodo utilizado neste estudo (&#952;c = 15 d).]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[Colorantes]]></kwd>
<kwd lng="es"><![CDATA[Materia orgánica]]></kwd>
<kwd lng="es"><![CDATA[Procesos biológicos]]></kwd>
<kwd lng="es"><![CDATA[Reactor aerobio]]></kwd>
<kwd lng="es"><![CDATA[Reactor anaerobio]]></kwd>
<kwd lng="en"><![CDATA[Dyes]]></kwd>
<kwd lng="en"><![CDATA[Organic material]]></kwd>
<kwd lng="en"><![CDATA[Biological processes]]></kwd>
<kwd lng="en"><![CDATA[Aerobic reactor]]></kwd>
<kwd lng="en"><![CDATA[Anaerobic reactor]]></kwd>
<kwd lng="pt"><![CDATA[Corantes]]></kwd>
<kwd lng="pt"><![CDATA[Matéria orgânica]]></kwd>
<kwd lng="pt"><![CDATA[Processos biológicos]]></kwd>
<kwd lng="pt"><![CDATA[Reator aeróbico]]></kwd>
<kwd lng="pt"><![CDATA[Reator anaeróbico]]></kwd>
</kwd-group>
</article-meta>
</front><back>
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