CAPÍTULO UNO

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TRADICIÓN E INNOVACIÓN S.A. de C.V. BALANCE GENERAL Q1= Q2 + Q3 + Q4 Q3 = 5,519 L/d - 4.09 L/d - 109.9 L/d BALANCE PARA SST: SST3 = 409,812 mg/d - 204,906 mg/d Q3 = 5,405 L/d SST3 = 204,906 mg/d La remoción de DBO tomada fue el 85% lo cual entra en el intervalo teórico 70-95%. DBO1 = 38.29 mg/L DBO2 = 32.54 mg/L BALANCE GENERAL DBO3= DBO1 – DBO2 = 38.29 mg/L - 32.54 mg/L DQO1 = 44.2 mg/L DQO2 = 37.57 mg/L DBO3= 5.79 mg/L DQO3= DQO1 – DQO2 = 44.2 mg/L - 37.57 mg/L DQO3= 6.7 mg/L 361
TRADICIÓN E INNOVACIÓN S.A. de C.V. 4.3.2.3 Filtro percolador de baja tasa Q1 = 5,405 L/d SST1 = 204,906 mg/d DBO1= 5.79 mg/L DQO1= 6.7 mg/L Flujo SST1 = 204,906 mg/d Q1 Q3 Q2 Para calcular el flujo de SST en Q2 (purga de lodos), se sabe que la eficiencia de estos es: SST2 = (204,906 mg/d) * (0.6) = 122,943 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. Flujo volumétrico para la purga de lodos es: BALANCE GENERAL Q1= Q2 + Q3 Q3 = Q1 - Q2= 5,405 L/d - 6.14 L/d Q2 = 122,943 mg/d 20,000 mg/L Q2 =6.14 L/d Q3 = 5,264L/d 362
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CAPÍTULO UNO

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