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TRADICIÓN E INNOVACIÓN S.A. de C.V. 4.1.2.3 Filtro percolador de baja tasa Q1= 5,519 L/d DQO1 = 44.2 mg/L SST1 = 409,812 mg/d DBO1 = 38.3 mg/L Q2 = Lodos Q3 = Efluente Q1 Q3 Q2 Para poder calcular el flujo de lodos Q2 tomamos en cuenta principalmente la remoción de los SST la cual tiene una remoción de 60% (MARK J. HAMMER). SST2= (409,812 mg/L)*(0.60) SST2 = 245,887 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. El flujo volumétrico para la purga de lodos es: BALANCE GENERAL Q1= Q2 + Q3 Q3 = Q1 – Q2 = 5,519 L/d - 12.29 L/d Q2= (245,887 mg/d) 20,000 mg/L Q2= 12.29 L/d Q3 = 5,507 L/d SST3= Q1SST1 – Q2SST2 SST3= (5,519 L/d)* (409,812 mg/d) – (12.29 L/d)*(245,887 mg/d) 345
TRADICIÓN E INNOVACIÓN S.A. de C.V. SST3= 164,818 mg/d La tasa de remoción de DBO para los filtros percoladores de baja tasa están dentro de los intervalos de 80-90% (MORGAN SAGUSTUME), nosotros tomamos una eficiencia de remoción de DBO de 85%. DBO1 = 38.3 mg/L DBO2 = 32.5 mg/L BALANCE GENERAL DBO3 = DBO1 - DBO2 DQO1=44.2 mg/L DQO2= 37.5 mg/L 4.1.2.4 Sedimentador secundario DBO3 = 5.8 mg/L DQO3 = 6.7 mg/L Q1 Q3 Q2 Q1 = 5,507 L/d = Afluente (agua que proviene del filtro percolador) DBO1 = 5.8 mg/L DQO1 = 6.7 mg/L SST1= 164,818 mg/d Q2 = Lodos Q3 = Efluente para calcular el flujo de Q2 tomamos en cuenta principalmente la remoción de los sólidos suspendidos totales, para caudales industriales en 346
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CAPÍTULO UNO

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