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Conventional ASP design, population 126000

Short answer

Design flow 20160 m³/d, aeration tank volume 6720 m³ (detention 8.0 h). Provide three tanks each 47 m × 12.0 m × 4.5 m. Checks: HRT 8.0 h, volumetric loading 0.60 kg BOD/m³/d, return sludge ratio 43%, horizontal velocity 0.10 m/min.

Design a conventional activated sludge treatment plant in your Municipality to treat the domestic sewage with diffused air aeration with the following data. Population = 1,26,000; Per capita sewage flow = 160 lpcd; Settled sewage BOD5 = 200 mg/L; Effluent BOD5 required = 15 mg/L; Take F/M: 0.2 and MLSS = 3000 mg/L. Also check HRT, Volumetric Loading, Return Sludge ratio, Horizontal Velocity.

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=200BOD_5=S_0=200 mg/l; effluent BOD5=15BOD_5=15 mg/l (efficiency 200−15200=92.5%\dfrac{200-15}{200}=92.5\%); F/M=0.2F/M=0.2/day; MLSS =3000=3000 mg/l. Assumed: SVI =100=100 ml/g for the return sludge ratio.

Step 1: Design flow

Q=126000×160/1000=20160.0 m3/dayQ = 126000\times160/1000 = 20160.0\ \text{m}^3/\text{day}

Step 2: Volume of aeration tank

V=20160.0×2000.2×3000=6720.0 m3V = \frac{20160.0\times 200}{0.2\times 3000} = 6720.0\ \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=1680.0 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} = 1680.0\ \text{m}^2 \end{aligned}

Provide 3 tanks (so one can be taken out of service), each with area 560.0560.0 m² and L : B about 4 : 1:

B=560.04=11.83 m (adopt 12.0 m),L=560.012.0=46.7 m (adopt 47 m)B=\sqrt{\frac{560.0}{4}} = 11.83\ \text{m (adopt 12.0 m)},\qquad L=\frac{560.0}{12.0} = 46.7\ \text{m (adopt 47 m)}

Adding 0.5 m free board, the tank depth is 4.5 m. The size of each tank is 47 m×12.0 m×4.5 m47\ \text{m}\times 12.0\ \text{m}\times 4.5\ \text{m}.

Step 4: Checks

Hydraulic retention time=VQ=6720.020160.0×24=8.0 h (usual 4-8 h; accepted)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{6720.0}{20160.0}\times 24 = 8.0\ \text{h}\ (\text{usual 4-8 h; accepted})\\ \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} 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=20160/(86400×3)12.0×4.0=0.0016 m/s (=0.10 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{20160/(86400\times 3)}{12.0\times 4.0} = 0.0016\ \text{m/s}\ (= 0.10\ \text{m/min}) \end{aligned}

Answer: aeration tank volume ≈6720\approx 6720 m³ (detention 8.0 h, depth 4.0 m); provide 3 tanks, each 47 m×12.0 m47\ \text{m}\times 12.0\ \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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