<?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>1692-3561</journal-id>
<journal-title><![CDATA[Biotecnología en el Sector Agropecuario y Agroindustrial]]></journal-title>
<abbrev-journal-title><![CDATA[Rev.Bio.Agro]]></abbrev-journal-title>
<issn>1692-3561</issn>
<publisher>
<publisher-name><![CDATA[Taller Editorial Universidad del Cauca]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1692-35612018000100062</article-id>
<article-id pub-id-type="doi">10.18684/bsaa.v16n1.625</article-id>
<title-group>
<article-title xml:lang="es"><![CDATA[CONDICIONES ÓPTIMAS DE LA ETAPA DE LIXIVIACIÓN EN LA EXTRACCIÓN DE ALMIDÓN DE YUCA]]></article-title>
<article-title xml:lang="en"><![CDATA[OPTIMUM CONDITIONS FOR THE LEACHING STEP IN THE EXTRACTION OF CASSAVA STARCH]]></article-title>
<article-title xml:lang="pt"><![CDATA[CONDIÇÕES IDEAIS DE LA FASE DE LIXIVIAÇÃO EM EXTRAÇÃO DE AMIDO DE MANDIOCA]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[GARCÍA-MOGOLLÓN]]></surname>
<given-names><![CDATA[CARLOS]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[SALCEDO-MENDOZA]]></surname>
<given-names><![CDATA[JAIRO]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[ALVIS-BERMUDEZ]]></surname>
<given-names><![CDATA[ARMANDO]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad de Sucre Facultad de Ingenierías, Grupo PADES ]]></institution>
<addr-line><![CDATA[Montería ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad de Córdoba Facultad de Ingenierías Grupo de Investigación Procesos y Agroindustria de Vegetales]]></institution>
<addr-line><![CDATA[Montería ]]></addr-line>
<country>Colombia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>06</month>
<year>2018</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>06</month>
<year>2018</year>
</pub-date>
<volume>16</volume>
<numero>1</numero>
<fpage>62</fpage>
<lpage>67</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S1692-35612018000100062&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S1692-35612018000100062&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S1692-35612018000100062&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="es"><p><![CDATA[RESUMEN La operación de lixiviación consiste en poner en contacto suficiente agua con yuca molida para extraer el almidón y separarlo de la fibra y otros componentes. Con el objetivo de determinar las condiciones óptimas de consumo de agua en la etapa de lixiviación de almidón de yuca se obtuvo una curva de equilibrio pulpa de yuca-agua de extracción. El uso excesivo de agua no garantiza la mayor extracción de almidón en este proceso e incrementa el costo de este. Se utilizaron relaciones agua-yuca molida, se mezclaron durante un tiempo de residencia de 5 s a 37°C y se separaron a través de una malla de 120 mesh; para después calcular la composición en agua, almidón e inertes. Los resultados obtenidos permiten establecer una relación óptima de 450 kg a 740 kg de agua por 1 kg de pulpa de yuca con un porcentaje entre el 18 y el 20% de almidón extraíble. Con la optimización fue posible reducir el consumo de 3 a 4 kg de agua por 1 kg de yuca al molino.]]></p></abstract>
<abstract abstract-type="short" xml:lang="en"><p><![CDATA[ABSTRACT The leaching operation is to put in contact enough water with ground manioc to extract the starch and separate it from the fiber and other components. With the objective of determining the optimal conditions of water consumption in the stage of leaching of cassava was obtained a starch extraction (cassava pulp - water) equilibrium curve. The excessive use of water does not warrant the extraction of starch in this process and increases the cost of this. Quantities of pulp-water were mixed for a residence time of 5 s at 37°C, and refining through a mesh of 120 mesh; to then calculate the composition in water, starch and inert. The results obtained allow optimum relationship of 450 kg to 740 kg of water per 1 kg of cassava pulp with a percentage between the 18 and 20% of removable starch. With the optimization it was possible to reduce the consumption of 3 to 4 kg of water per 1 kg of cassava pulp.]]></p></abstract>
<abstract abstract-type="short" xml:lang="pt"><p><![CDATA[RESUMO A operação de lixiviação é em colocar em contato suficiente água com chão de yucca para extrair o amido e separá-lo de fibra e outros componentes. A fim de determinar as condições ideais de consumo de água na fase de lixiviação de amido de mandioca obteve-se uma polpa de yuca-agua de extração de curva de equilíbrio. O uso excessivo de água não garante a extração de amido neste processo e aumenta o custo disto. Quantidades de polpa-água foram misturadas para um tempo de residência de 5 s a 37°C e separados através de uma malha 120 malha; para em seguida calcular a composição em água, amido e inerte. Os resultados obtidos permitem estabelecer uma melhor relação de 450 kg para 740 kg de água por 1 kg de polpa da mandioca com uma percentagem entre os 18 e os 20% de amido removível. Com a otimização foi possível reduzir o consumo de 3 a 4 kg de água de 1 kg de mandioca para o moinho.]]></p></abstract>
<kwd-group>
<kwd lng="es"><![CDATA[Manihot esculenta Crantz]]></kwd>
<kwd lng="es"><![CDATA[Curva de equilibrio]]></kwd>
<kwd lng="es"><![CDATA[Lixiviación]]></kwd>
<kwd lng="es"><![CDATA[Agua]]></kwd>
<kwd lng="es"><![CDATA[Fibra]]></kwd>
<kwd lng="en"><![CDATA[Manihot esculenta Crantz]]></kwd>
<kwd lng="en"><![CDATA[Equilibrium curve]]></kwd>
<kwd lng="en"><![CDATA[Leaching]]></kwd>
<kwd lng="en"><![CDATA[Water]]></kwd>
<kwd lng="en"><![CDATA[Fiber]]></kwd>
<kwd lng="pt"><![CDATA[Manihot esculenta Crantz]]></kwd>
<kwd lng="pt"><![CDATA[Curva de equilíbrio]]></kwd>
<kwd lng="pt"><![CDATA[Lixiviação]]></kwd>
<kwd lng="pt"><![CDATA[Água]]></kwd>
<kwd lng="pt"><![CDATA[Fibra]]></kwd>
</kwd-group>
</article-meta>
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