Your firm has been asked to design the third-stage plug-flow…

Your firm has been asked to design the third-stage plug-flow, nitrification-denitrification reactor for one of your long-term municipal clients. Pertinent design data are as follows: Design flow: 6.25 MGD Temperature 20 °C MLVSS/MLSS: 0.75 2nd stage nitrate (NO3–N) concentration: 30 mg/L Effluent nitrate (NO3–N) concentration: 1.0 mg/L Effluent TSS concentration: 3 mg/L Denitrification cell yield coefficient (Y): 0.85 mg MLVSS/ mg NO3—N removed Endogenous decay constant (ke): 0.04 day-1 Peak nitrate removal rate (): 0.27 mg NO3–N removed/mg MLVSSday Half-saturation constant for denitrification (KD): 0.15 mg NO3–N/L MLSS concentration: 2,800 mg/L Methanol requirement: 3.0 lb methanol/lb nitrate removed Methanol specific weight: 6.60 lb/ft3 Determine the following: (5 pts) “Design” MCRT for denitrification (Days) (5 pts) If the design MCRT for denitrification is calculated to be 5.39 days, determine nitrate removal rate (q)(unit: mg NO3—N removed/ mg MLVSS

The wastewater is to treated by a fixed-bed granular carbon…

The wastewater is to treated by a fixed-bed granular carbon adsorption column. The flow rate of the City of Orlando treatment facility flow rate is 60,000 gpd and the allowable breakthrough concentration, Ca is 20 mg/L. The design column has a unit liquid flowrate of 5 gpm/ft2 and the on-line time is eight (8) days. Your firm has been asked to use the “Kinetic” approach in your design using the following information. Q = 60,000 gpd C0 = 450 mg/L Ca = 20 mg/L Qunit = 5 gpm/ft2 On-line time (t) = 8 days Rate constant (k1) = 55.38 gal/lb