An activated sludge plant (CSTR w/ recycle) has the following characteristics: Influent substrate concentration, So = 400 mg/L BODL (all soluble); influent VSS, Xvº = 0; effluent 3 substrate concentration, S = 10 mg/L BODL; flow rate, Q = 1000 m³/day; aeration basin volume, V = 200 m³; reactor MLVSS, Xy = 4,280 mg/L; average, steady-state oxygen uptake rate, Oxygen uptake rate (OUR) = 0.3 mg 02/L-min. The biomass viability (i.e., v = Xa/Xv) was measured using the oxygen uptake rate (OUR) technique and found equal to 0.926. An aliquot of mixed liquor was placed in a small reactor, aerated without any exogenous substrate addition (i.e., starvation conditions) and it's OUR was measured over time resulting in the following data: 0 1 2 3 4 5 6 8 10 Time (days) OUR (mg 02/L-min) 0.3 0.274 0.243 0.222 0.203 0.182 0.165 0.135 0.110 By use of the above data, the microorganism decay coefficient (b, day) can be estimated if you assume that a constant relationship exists between Xa and OUR, i.e., OUR = a Xa, where a = proportionality constant (g O2/g Xa - min). 1. Estimate b (1/d) by using the above data (Use regression). 2. Calculate the solids retention time for this plant. 3. Calculate the net biodegradable fraction of the viable biomass (fd).

Aquaculture Science
3rd Edition
ISBN:9781133558347
Author:Parker
Publisher:Parker
Chapter12: Water Requirements For Aquaculture
Section: Chapter Questions
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An activated sludge plant (CSTR w/ recycle) has the following characteristics: Influent
substrate concentration, So = 400 mg/L BODL (all soluble); influent VSS, Xyº = 0; effluent
3
substrate concentration, S = 10 mg/L BODL; flow rate, Q = 1000 m³/day; aeration basin
3
volume, V = 200 m³; reactor MLVSS, Xv = 4,280 mg/L; average, steady-state oxygen
uptake rate, Oxygen uptake rate (OUR) = 0.3 mg 02/L-min. The biomass viability (i.e., v =
Xa/Xv) was measured using the oxygen uptake rate (OUR) technique and found equal to
0.926. An aliquot of mixed liquor was placed in a small reactor, aerated without any
exogenous substrate addition (i.e., starvation conditions) and it's OUR was measured over
time resulting in the following data:
0 1
2
3
4
5
Time (days)
OUR (mg 02/L-min) 0.3 0.274 0.243| 0.222 0.203 0.182
6
8
10
0.165 0.135 0.110
By use of the above data, the microorganism decay coefficient (b, day can be estimated if
you assume that a constant relationship exists between Xa and OUR, i.e., OUR = a Xa, where
a = proportionality constant (g O2/g Xa - min).
1. Estimate b (1/d) by using the above data (Use regression).
2. Calculate the solids retention time for this plant.
3. Calculate the net biodegradable fraction of the viable biomass (fd).
Transcribed Image Text:An activated sludge plant (CSTR w/ recycle) has the following characteristics: Influent substrate concentration, So = 400 mg/L BODL (all soluble); influent VSS, Xyº = 0; effluent 3 substrate concentration, S = 10 mg/L BODL; flow rate, Q = 1000 m³/day; aeration basin 3 volume, V = 200 m³; reactor MLVSS, Xv = 4,280 mg/L; average, steady-state oxygen uptake rate, Oxygen uptake rate (OUR) = 0.3 mg 02/L-min. The biomass viability (i.e., v = Xa/Xv) was measured using the oxygen uptake rate (OUR) technique and found equal to 0.926. An aliquot of mixed liquor was placed in a small reactor, aerated without any exogenous substrate addition (i.e., starvation conditions) and it's OUR was measured over time resulting in the following data: 0 1 2 3 4 5 Time (days) OUR (mg 02/L-min) 0.3 0.274 0.243| 0.222 0.203 0.182 6 8 10 0.165 0.135 0.110 By use of the above data, the microorganism decay coefficient (b, day can be estimated if you assume that a constant relationship exists between Xa and OUR, i.e., OUR = a Xa, where a = proportionality constant (g O2/g Xa - min). 1. Estimate b (1/d) by using the above data (Use regression). 2. Calculate the solids retention time for this plant. 3. Calculate the net biodegradable fraction of the viable biomass (fd).
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