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Circular sedimentation tank, population 80000

Short answer

Two circular tanks, each 19.5 m diameter, 3.0 m side water depth (total 4.0 m), detention 2.0 h, surface loading 35.3 m³/m²/day.

What will be the circular sewage sedimentation tank dimension for an industrial area having population of 80,000? The average water demand is 135 lpcd. Assume that 78% water reaches at treatment plant and maximum demand is 2.5 times average demand. Dimension of the suspended silica particles available in influent water more than 0.12 mm.

Assumptions: sewage reaching the plant =0.78×135=105.3=0.78\times135 = 105.3 lpcd, designed for the maximum rate (2.5×2.5\times average): Qavg=80000×105.3/1000=8424.0Q_{avg}=80000\times 105.3/1000 = 8424.0 m³/day. Detention 2 h and depth 3 m are adopted; two tanks are provided. Silica d=0.12d=0.12 mm (G=2.65G=2.65) at 20°C.

Step 1: Design flow

Q=80000×135×0.78×2.5/1000=21060 m3/dayQ = 80000\times 135\times 0.78\times 2.5/1000 = 21060\ \text{m}^3/\text{day}

Step 2: Capacity

Adopt detention period t=2.0t = 2.0 h and side water depth H=3.0H = 3.0 m (typical for plain sedimentation: 2-3 h, 2.5-4 m).

V=Q t=2106024×2.0=1755.0 m3,A=VH=1755.03.0=585.0 m2V = Q\,t = \frac{21060}{24}\times 2.0 = 1755.0\ \text{m}^3,\qquad A = \frac{V}{H} = \frac{1755.0}{3.0} = 585.0\ \text{m}^2

Step 3: Diameter

Provide 2 circular tanks, each with area A1=A/2A_1 = A/2 (one tank can then be shut down for cleaning).

D=4A1π=4×292.5π=19.30 m ⇒ adopt D=19.5 mD = \sqrt{\frac{4A_1}{\pi}} = \sqrt{\frac{4\times 292.5}{\pi}} = 19.30\ \text{m}\ \Rightarrow\ \text{adopt } D = 19.5\ \text{m}

Adopt a total depth of H+0.5 (free board)+0.5 (sludge zone)=4.0H + 0.5\ (\text{free board}) + 0.5\ (\text{sludge zone}) = 4.0 m, with a central inlet well and a peripheral weir.

Step 4: Checks

Surface loading=Q/NπD2/4=10530298.6=35.3 m3/m2/day (usual 25-40 for primary tanks)Weir loading=Q/NπD=10530π×19.5=171.9 m3/m/day (should be below about 300)Actual detention=(πD2/4)HQ/N×24=2.04 h\begin{aligned} \text{Surface loading} &= \frac{Q/N}{\pi D^2/4} = \frac{10530}{298.6} = 35.3\ \text{m}^3/\text{m}^2\text{/day}\ (\text{usual 25-40 for primary tanks})\\ \text{Weir loading} &= \frac{Q/N}{\pi D} = \frac{10530}{\pi\times 19.5} = 171.9\ \text{m}^3/\text{m/day}\ (\text{should be below about 300})\\ \text{Actual detention} &= \frac{(\pi D^2/4)H}{Q/N}\times 24 = 2.04\ \text{h} \end{aligned}

Check: for 0.1<d<10.1<d<1 mm, Hazen's transition formula at 20°C gives vs=60.6×1.65×0.12×1.3=15.6v_s = 60.6\times1.65\times0.12\times1.3 = 15.6 mm/s ≈1348\approx 1348 m/day (dd in mm). This is far greater than the overflow rate of the tank, so silica of 0.12 mm and larger is removed.

   Section (circular, radial flow)
      inlet well        weir/launder
   ->  |__|~~~~~~~~~~~~~~~~~~~~~|_
       |  \                  /  | H = 3.0 m
       |   \______    ______/   | + sludge zone
       +----------\__/----------+
                  sludge hopper -> sludge pipe
        <---------- D = 19.5 m ---------->

Answer: 2 circular sedimentation tanks, each of diameter 19.5 m, side water depth 3.0 m (total depth about 4.0 m), detention 2.0 h, surface loading 35.3 m³/m²/day.

✓ Answer checked by Claude Opus 5.5 (high effort)

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