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Circular sedimentation tank for 58 MLD

Short answer

Provide two circular tanks, each 32.5 m diameter, 3.0 m side water depth (total 4.0 m), detention 2.0 h, surface loading 35.0 m³/m²/day.

Design a circular sedimentation tank for 58 MLD of sewage of a temperature of 20°C. Assume specific gravity of organic matters and inorganic matters are 1.12 and 2.65 respectively.

Assumptions: detention 2 h at the design flow of 58 MLD, side water depth 3 m. Two tanks are provided. The particle sizes are not given, so the sizes removed are only checked at the end (20°C, ν=1.01×10−6\nu=1.01\times 10^{-6} m²/s).

Step 1: Design flow

Q=58×106/1000=58000 m3/dayQ = 58\times 10^6/1000 = 58000\ \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=5800024×2.0=4833.3 m3,A=VH=4833.33.0=1611.1 m2V = Q\,t = \frac{58000}{24}\times 2.0 = 4833.3\ \text{m}^3,\qquad A = \frac{V}{H} = \frac{4833.3}{3.0} = 1611.1\ \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=4×805.6π=32.03 m ⇒ adopt D=32.5 mD = \sqrt{\frac{4A_1}{\pi}} = \sqrt{\frac{4\times 805.6}{\pi}} = 32.03\ \text{m}\ \Rightarrow\ \text{adopt } D = 32.5\ \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=29000829.6=35.0 m3/m2/day (usual 25-40 for primary tanks)Weir loading=Q/NπD=29000π×32.5=284.0 m3/m/day (should be below about 300)Actual detention=(πD2/4)HQ/N×24=2.06 h\begin{aligned} \text{Surface loading} &= \frac{Q/N}{\pi D^2/4} = \frac{29000}{829.6} = 35.0\ \text{m}^3/\text{m}^2\text{/day}\ (\text{usual 25-40 for primary tanks})\\ \text{Weir loading} &= \frac{Q/N}{\pi D} = \frac{29000}{\pi\times 32.5} = 284.0\ \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 = 2.06\ \text{h} \end{aligned}

Size of particles removed: the tank removes all particles whose settling velocity is ≥\ge the overflow rate v0=35.0/86400=4.05×10−4v_0 = 35.0/86400 = 4.05\times 10^{-4} m/s. From Stokes' law, d=18νv0/(g(G−1))d=\sqrt{18\nu v_0/(g(G-1))}:

  • inorganic particles (G=2.65G=2.65): d=0.021d = 0.021 mm
  • organic particles (G=1.12G=1.12): d=0.079d = 0.079 mm

Particles larger than these are fully removed (Stokes' law is valid, since Re<1Re<1).

   Section (circular, radial flow)
      inlet well        weir/launder
   ->  |__|~~~~~~~~~~~~~~~~~~~~~|_
       |  \                  /  | H = 3.0 m
       |   \______    ______/   | + sludge zone
       +----------\__/----------+
                  sludge hopper -> sludge pipe
        <---------- D = 32.5 m ---------->

Answer: 2 circular sedimentation tanks, each of diameter 32.5 m, side water depth 3.0 m (total depth about 4.0 m), detention 2.0 h, surface loading 35.0 m³/m²/day.

✓ Answer checked by Claude Opus 5.5 (high effort)

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