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Conventional ASP design, 0.104 m³/s

Short answer

Flow 8985.6 m³/d, aeration tank volume V=Q⋅S₀/(F/M⋅X)=3295 m³. Use liquid depth 4.0 m, provide two tanks each 40 m × 10.5 m × 4.5 m (depth includes 0.5 m freeboard).

Design a conventional activated sludge plant to treat settled domestic sewage with diffused air aeration system for the given data: Sewage discharge = 0.104 m³/s; BOD5 of settled sewage = 220 mg/l; Effluent BOD allowed = 30 mg/l; F/M ratio = 0.2; MLSS = 3000 mg/l.

Data and design basis

Conventional ASP (plug flow, diffused air). The aeration tank volume follows from the food-to-micro-organism ratio:

FM=Q S0V X ⇒ V=Q S0(F/M) X\frac{F}{M}=\frac{Q\,S_0}{V\,X}\ \Rightarrow\ V=\frac{Q\,S_0}{(F/M)\,X}

Data: settled-sewage BOD5=S0=220BOD_5=S_0=220 mg/l, effluent BOD Se=30S_e=30 mg/l, F/M=0.2F/M=0.2 per day, MLSS X=3000X=3000 mg/l. The return sludge ratio is also checked (SVI assumed).

Step 1: Design flow

Q=0.104×86400=8985.6 m3/dayQ = 0.104\times86400 = 8985.6\ \text{m}^3/\text{day}

Step 2: Volume of aeration tank

V=8985.6×2200.2×3000=3294.7 m3V = \frac{8985.6\times 220}{0.2\times 3000} = 3294.7\ \text{m}^3

(units: QQ in m³/day and S0S_0, XX in mg/l = g/m³.)

Step 3: Dimensions

Adopt liquid depth =4.0 m (usual range 3-4.5 m)Plan area A=V4.0=823.7 m2\begin{aligned} \text{Adopt liquid depth } &= 4.0\ \text{m (usual range 3-4.5 m)}\\ \text{Plan area } A &= \frac{V}{4.0} = 823.7\ \text{m}^2 \end{aligned}

Provide 2 tanks (so one can be taken out of service), each with area 411.8411.8 m² and L : B about 4 : 1:

B=411.84=10.15 m (adopt 10.5 m),L=411.810.5=39.2 m (adopt 40 m)B=\sqrt{\frac{411.8}{4}} = 10.15\ \text{m (adopt 10.5 m)},\qquad L=\frac{411.8}{10.5} = 39.2\ \text{m (adopt 40 m)}

Adding 0.5 m free board, the tank depth is 4.5 m. The size of each tank is 40 m×10.5 m×4.5 m40\ \text{m}\times 10.5\ \text{m}\times 4.5\ \text{m}.

Step 4: Checks

Hydraulic retention time=VQ=3294.78985.6×24=8.8 h (slightly above the usual 4-8 h; acceptable)Volumetric loading=Q S0V×1000=0.60 kg BOD/m3/day (usual 0.3-0.6)\begin{aligned} \text{Hydraulic retention time} &= \frac{V}{Q} = \frac{3294.7}{8985.6}\times 24 = 8.8\ \text{h}\ (\text{slightly above the usual 4-8 h; acceptable})\\ \text{Volumetric loading} &= \frac{Q\,S_0}{V\times 1000} = 0.60\ \text{kg BOD/m}^3\text{/day}\ (\text{usual 0.3-0.6}) \end{aligned}

BOD removal efficiency =220−30220×100=86.4%=\dfrac{220-30}{220}\times100=86.4\%, within the usual 85-95% of a conventional ASP.

Return sludge ratio: XR=106SVI=106100=10000 mg/l (SVI assumed 100 ml/g)QRQ=XXR−X=300010000−3000=0.429  (≈43%)Horizontal velocity=Q/NB×H=8986/(86400×2)10.5×4.0=0.0012 m/s (=0.07 m/min)\begin{aligned} \text{Return sludge ratio: } X_R &= \frac{10^6}{SVI} = \frac{10^6}{100} = 10000\ \text{mg/l}\ (SVI\ \text{assumed } 100\ \text{ml/g})\\ \frac{Q_R}{Q} &= \frac{X}{X_R-X} = \frac{3000}{10000-3000} = 0.429\ \ (\approx 43\%)\\ \text{Horizontal velocity} &= \frac{Q/N}{B\times H} = \frac{8986/(86400\times 2)}{10.5\times 4.0} = 0.0012\ \text{m/s}\ (= 0.07\ \text{m/min}) \end{aligned}

Answer: aeration tank volume ≈3295\approx 3295 m³ (detention 8.8 h, depth 4.0 m); provide 2 tanks, each 40 m×10.5 m40\ \text{m}\times 10.5\ \text{m} in plan with liquid depth 4.0 m (tank depth 4.5 m).

✓ Answer checked by Claude Opus 5.5 (high effort)

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