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            <name>Title</name>
            <description>A name given to the resource</description>
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                <text>Agricultura sostenible</text>
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            <name>Description</name>
            <description>An account of the resource</description>
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                <text>Dominio científico: Agricultura sostenible</text>
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    <name>Text</name>
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          <name>Title</name>
          <description>A name given to the resource</description>
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              <text>Estudio de la detoxificación de efluentes cianurados por oxidación con dióxido de azufre, aire y catalizadores de cobre</text>
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          <name>Creator</name>
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              <text>Carolina Liseth Campos, Ernesto De la Torre</text>
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          <name>Description</name>
          <description>An account of the resource</description>
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              <text>Resumen: Se estudió la   detoxificación de efluentes cianurados, mediante oxidación con dióxido de   azufre (SO2), aire y catalizadores de Cu. Se ensayaron diversas   especies de Cu tales como: CuSO4 en solución, carbón activado   granular (CAG) impregnado con CuSO4, CAG impregnado con Cu0 y Cu0 granular. Este proceso es conocido como INCO, el cual oxida   el cianuro WAD a cianato y precipita los metales tales como Cu, Ni, Zn, Cd y   Fe. Se realizaron ensayos a escala de laboratorio con soluciones sintéticas   de 500 mg/L NaCN y efluentes cianurados industriales. Se midió la variación   de CN- con respecto al tiempo por titulación con AgNO3.   Se estudió la influencia del pH, la dosificación de Na2S2O5 (fuente de SO2) y las concentraciones de los diferentes   catalizadores. Los tiempos de oxidación del 98%  de CN- de las soluciones   sintéticas de NaCN, bajo las mejores condiciones de operación del proceso   INCO (pH 10.0; 276 N L/h aire; 400 RPM; y 1000 mg/L Na2S2O5)   fueron 210 min con 50 mg/L Cu2+ (CuSO4), 40 min con 50 g/L de CAG   impregnado con CuSO4, 8 min con 50 g/L de CAG impregnado con Cu0 y 195 min con 10 g/L Cu0 granular. Los efluentes industriales   fueron detoxificados utilizando 5 g/L CAG impregnado con Cu0.   Estos efluentes, con concentraciones iniciales de 432.50 mg/L y 112.50 mg/L de   cianuro total alcanzaron 0.06 mg/L cianuro total en 90 min y 0.05 mg/L   cianuro total en 40 min, respectivamente. El contenido de metales en los   efluentes (Cu, Cd, Zn, Ni y Fe) luego de la precipitación llegaron a los   límites permisibles de descarga a un cuerpo de agua dulce según lo   establecido en el TULAS. El precio del tratamiento de efluentes cianurados   por el método INCO con CAG impregnado con Cu0 es de 6.70 USD/m3. Abstract: It was   studied the detoxification of cyanide effluents by oxidation with sulfur   dioxide (SO2), air and copper catalyzer. The CuSO4 solution, granular activated carbon (GAC) impregnated with CuSO4, GAC   impregnated with Cu0 and granular Cu0 were studied. This   process is called INCO process and it oxidizes WAD cyanide to cyanate and   precipitates metals such as Cu, Ni, Zn, Cd and Fe. Experiments were conducted   at laboratory scale using synthetic solutions of 500 mg/L   NaCN and industrial cyanide effluents. The variation of the CN- concentration   in time was determined titrimetrically with AgNO3 solution. The influence of pH   and the concentrations of Na2S2O5 (SO2 source of process) and Cu catalysts on the rate of the removal of CN- were estudied.   The oxidation times of the 98 % of cyanide removal from the   synthetic solutions of NaCN based on the best   operation conditions (pH   10,0; 276 N L/h air; 400 RPM and 1000 mg/L Na2S2O5) were: 210 min (50 mg/L Cu2+ obtained from CuSO4),   40 min (50 g/L GAC impregnated with CuSO4), 80 min (5 g/L GAC impregnated with Cu0)   and 195 min (10   g/L granular Cu0).   The industrial effluents were detoxified using 5 g/L GAC impregnated with Cu0.   These effluents with initial concentrations of 432.50 mg/L and 112.50 of total   cyanide reached 0.06 mg/L total cyanide in 90 min and  0.05 mg/L total cyanide in 40 min, respectively. Besides, the metal content   (Cu, Cd, Zn, Ni and Fe) of the industrial effluents after precipitation   reached the permissible limits for discharges into a fresh body water   according to TULAS. The price of cyanide wastewater treatment by the INCO   method using GAC impregnated with carbon is 6.70 USD/m3.</text>
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          <name>Date</name>
          <description>A point or period of time associated with an event in the lifecycle of the resource</description>
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              <text>2015</text>
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          <name>Source</name>
          <description>A related resource from which the described resource is derived</description>
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            <elementText elementTextId="167148">
              <text>Revista Politécnica</text>
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          <name>Publisher</name>
          <description>An entity responsible for making the resource available</description>
          <elementTextContainer>
            <elementText elementTextId="167149">
              <text>Escuela Politécnica Nacional (EPN)</text>
            </elementText>
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          <name>Coverage</name>
          <description>The spatial or temporal topic of the resource, the spatial applicability of the resource, or the jurisdiction under which the resource is relevant</description>
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              <text>Science (General), Technology (General)</text>
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          <description>A related resource</description>
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            <elementText elementTextId="167151">
              <text>&lt;a href="https://revistapolitecnica.epn.edu.ec/ojs2/index.php/revista_politecnica2/article/view/578" target="_blank" rel="noreferrer noopener"&gt;https://revistapolitecnica.epn.edu.ec/ojs2/index.php/revista_politecnica2/article/view/578&lt;/a&gt;</text>
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