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TRADICIÓN E INNOVACIÓN S.A. de C.V. un sedimentador primario que esta dentro de un intervalo del 50-70%. Por el parámetro de remoción de SST en un sedimentador secundario tomamos el 60% por lo tanto: Flujo SST2 = (164,818 mg/d) * (0.60) SST2= 98,890 mg/d La purga de lodos en un sedimentador o cualquier equipo que necesite de ello no debe ser mayor al 5% (MARK J. HAMMER), por lo que nosotros tomamos el 2% ( P /V) que nos quiere decir que hay 20,000 mg/L. BALANCE GENERAL Calculando SST3: Q2 = 98,890 mg/d 20,000 mg/L Q2 = 5 L/d Q1= Q2 + Q3 Q3 = Q1 – Q2 = 5,507 L/d - 5 L/d Q3 = 5,502 L/d SST3 = Q1 SST1 – Q2 SST2 = 164,818 mg/d –98,890 mg/d Q3 SST3 = (65,928 mg/d)* (1/5,502L/d) SST3 = 11.98 mg/L La tasa de remoción de DBO para aguas industriales esta dentro de un intervalo de DBO de 40-70% (MARK J. HAMMER) DBO1 = 5.8 mg/L DBO2 = 3.48 mg/L BALANCE GENERAL: DBO3 = DBO1 - DBO2 = 5.8 mg/L - 3.48 mg/L DBO3 = 2.32 mg/L 347
TRADICIÓN E INNOVACIÓN S.A. de C.V. 4.2 Tecnología 2 φ Entrada de agua residual φ Cribado φ Cárcamo φ Sedimentador primario φ Disco rotatorio biológico φ Sedimentador secundario φ Cloración ENTRADA DE AGUA RESIDUAL DE PROCESO Y DE SERVICIOS CRIBADO TANQUE DE CLORACIÓN CISTERNA TECNOLOGÍA 2 CÁRCAMO SEDIMENTADOR SECUNDARIO COMPOSTEO 348 SEDIMENTADOR PRIMARIO DISCO ROTATORIO BIOLÓGICO
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CAPÍTULO UNO

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