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TRADICIÓN E INNOVACIÓN S.A. de C.V. Flujo volumétrico para la purga de lodos es: BALANCE GENERAL Q1= Q2 + Q3 Q3 = Q1 – Q2 = 5,550 L/d - 30.7 L/d Q2 = 614,718 mg/d 20,000 mg/L Q2 = 30.7 L/d Q3 =5,519 L/d SST3 = SST1 – SST2 = 1´024,530 mg/d - 30.7 L/d SST3 = 409,812 mg/d La tasa de remoción de DBO esta dentro de un intervalo de 40-70%: tomamos el 60% DBO1 = 95.72 mg/L DBO2 = 57.43 mg/L BALANCE GENERAL DBO3= DBO1 – DBO2 = 95.72 mg/L - 57.43 mg/L DQO1 = 110.5 mg/L DQO2 = 66.3 mg/L DBO3=38.29 mg/L DQO3= DQO1 – DQO2 = 110.5 mg/L - 66.3 mg/L DQO3= 44.2 mg/L 359
TRADICIÓN E INNOVACIÓN S.A. de C.V. 4.3.2.2 Reactor UASB Q4 Q1 Q3 Q2 Q1 = 5,519 L/d = Afluente (agua que proviene del sedimentador primario) Q2 = Lodos Q3 = Efluentes Q4 = Biogás Flujo SST1 = 409,812 mg/d Para calcular el flujo de SST en Q2 (purga de lodos), se sabe que la eficiencia de estos es: SST2 = (409,812 mg/d) * (0.5) = 204,906 mg/d Se considera que la purga de lodos no debe ser mayor del 5% ( p /V), por lo tanto: Q2 =204,906 mg/d 50,000 mg/L Q2 =4.09 L/d Para el valor del biogás este depende del diseño, temperatura de operación, tipo de residuo, etc, aunque típicamente este valor es de alrededor de 0.18-0.2 m 3 de biogás/kg DQO removido. Se tomo un valor entre el intervalo de 0.19. Q4 = 109.9 L/d 360
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CAPÍTULO UNO

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