An activated sludge system is to be used for secondary treatment of 10,000 m³/d of municipal wastewater. After primary clarification, the BOD is 150 mg/L, and it is desired to have not more than 5 mg/L of soluble BOD in the effluent. A completely mixed reactor is to be used, and pilot-plant analysis has established the following kinetic values: Y = 0.5 kg/kg, kg = 0.05 d-¹. Assuming an MLSS concentration of 3000 mg/L and an underflow concentration of 10,000 mg/L from the secondary clarifier (MLVSS=0.8MLSS) determine (1) the volume of the reactor, (2) the mass and volume of solids that must be wasted each day, and (3) the recycle ratio. d
An activated sludge system is to be used for secondary treatment of 10,000 m³/d of municipal wastewater. After primary clarification, the BOD is 150 mg/L, and it is desired to have not more than 5 mg/L of soluble BOD in the effluent. A completely mixed reactor is to be used, and pilot-plant analysis has established the following kinetic values: Y = 0.5 kg/kg, kg = 0.05 d-¹. Assuming an MLSS concentration of 3000 mg/L and an underflow concentration of 10,000 mg/L from the secondary clarifier (MLVSS=0.8MLSS) determine (1) the volume of the reactor, (2) the mass and volume of solids that must be wasted each day, and (3) the recycle ratio. d
Chapter2: Loads On Structures
Section: Chapter Questions
Problem 1P
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An activated sludge system is to be used for secondary
treatment of 10,000 m³/d of municipal wastewater. After
primary clarification, the BOD is 150 mg/L, and it is
desired to have not more than 5 mg/L of soluble BOD in
the effluent. A completely mixed reactor is to be used,
and pilot-plant analysis has established the following
kinetic values: Y = 0.5 kg/kg, k, = 0.05 d-¹. Assuming an
MLSS concentration of 3000 mg/L and an underflow
concentration of 10,000 mg/L from the secondary clarifier
(MLVSS=0.8MLSS) determine (1) the volume of the
reactor, (2) the mass and volume of solids that must be
wasted each day, and (3) the recycle ratio.
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