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TRADICIÓN E INNOVACIÓN S.A. de C.V. 4.2.2.4 Sedimentador secundario Q1 Q2, E=65% Para el parámetro de remoción de SST en un sedimentador primario lo tomamos el 65% por tanto el flujo de SST en la purga seria 355 Q3 SSTi = 40974.5mg/d * 0.65 = 26425mg/d La purga de lodos en un sedimentador o cualquier equipo de ella no debe ser mayor al 5% (Mark, J Hammer). Por lo que nosotros tomamos el 2% (P/V) que nos quiere decir 2g-100ml, convirtiendo las unidades a mg/L = 20000mg/l Balance General: Ahora SST3 SEDIMENTADOR SECUNDARIO Por lo tanto Q2 = 1.333 l/d Q3 = Q1 +Q2 Q3 = 5517.66 l/d SST3 = 2.599mg/l
TRADICIÓN E INNOVACIÓN S.A. de C.V. La remoción de DBO para aguas industriales esta dentro de un intervalo de DBO de 40-70% 4.3 Tecnología 3 ENTRADA DE AGUA RESIDUAL CRIBADO CLORACIÓN DBO = 3.43 ,mg/d *.65 DBO2 = 2.22mg/d DBO3 = 3.73-2.22 DBO3 = 1.24 mg/d φ Entrada de agua residual φ Cribado φ Sedimentador primario φ UASB φ Filtro percolador de baja tasa φ Sedimentador secundario φ Cloración TECNOLOGÍA 3 SEDIMENTADOR PRIMARIO SEDIMENTADOR SECUNDARIO 356 UASB FILTRO PERCOLADOR
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CAPÍTULO UNO

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