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Question

Look at the following information for a completely mixed biological reactor: tank volume = 200 m3; flow rate = 50 m3/day ; incoming substrate concentration = 95 mg BOD5/L. Calculate effluent BOD5 ( Given Ks = 60 mg BOD5 /L ; kd = 0.06/day; μm = 3 /day )

The correct answer is

6.92 mg/L

Understanding the Biological Reactor Problem

This problem asks us to calculate the effluent BOD5 concentration from a completely mixed biological reactor. We are given the reactor's tank volume, the flow rate, the incoming substrate concentration (BOD5), and kinetic parameters like half-saturation constant ($K_s$), decay coefficient ($k_d$), and maximum specific growth rate ($\mu_{max}$).

Calculating Key Reactor Parameters

First, we need to determine the Hydraulic Retention Time ($\theta$) for the reactor. This represents the average time water spends in the reactor.

The formula for hydraulic retention time is:

$$ \theta = \frac{V}{Q} $$

Where:

  • $V$ = Tank Volume = 200 m³
  • $Q$ = Flow Rate = 50 m³/day

Plugging in the values:

$$ \theta = \frac{200 \text{ m}^3}{50 \text{ m}^3/\text{day}} = 4 \text{ days} $$

The dilution rate ($D$) is the reciprocal of the hydraulic retention time:

$$ D = \frac{1}{\theta} = \frac{1}{4 \text{ days}} = 0.25 \text{ day}^{-1} $$

Applying Monod Kinetics for Effluent Calculation

For a completely mixed biological reactor operating at steady state, the effluent substrate concentration ($S$) can be related to the kinetic parameters using a modified Monod equation that includes cell decay ($k_d$). The relationship derived from the mass balance and kinetics is:

$$ k_d + D = \frac{\mu_{max} S}{K_s + S} $$

Where:

  • $k_d$ = Decay coefficient = 0.06 day⁻¹
  • $D$ = Dilution rate = 0.25 day⁻¹
  • $\mu_{max}$ = Maximum specific growth rate = 3 day⁻¹
  • $K_s$ = Half-saturation constant = 60 mg BOD5/L
  • $S$ = Effluent substrate concentration (BOD5) in mg/L (what we need to find)

Step-by-Step Calculation of Effluent BOD5

Now, we substitute the known values into the equation:

$$ 0.06 \text{ day}^{-1} + 0.25 \text{ day}^{-1} = \frac{3 \text{ day}^{-1} \times S}{60 \text{ mg/L} + S} $$

Combine the terms on the left side:

$$ 0.31 \text{ day}^{-1} = \frac{3 S}{60 + S} $$

To solve for $S$, we rearrange the equation:

$$ 0.31 (60 + S) = 3 S $$

Distribute 0.31:

$$ 18.6 + 0.31 S = 3 S $$

Isolate the $S$ terms:

$$ 18.6 = 3 S - 0.31 S $$

$$ 18.6 = 2.69 S $$

Solve for $S$:

$$ S = \frac{18.6}{2.69} $$

$$ S \approx 6.9145 \text{ mg/L} $$

Final Result Comparison

The calculated effluent BOD5 concentration is approximately 6.92 mg/L. Comparing this value to the given options, it matches the first option.

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Important Questions from Sewage Treatment

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    1. It is less expensive compared to several other methods available.

    2. Processing of separable solids impacts the environment to a minimum.

    3. Quantity of separated solids requiring disposal is minimal

    4. Digested sludge is very readily dewatered able.

    Which of the above statements are correct?
  2. Chlorine is sometimes used in sewage treatment:

  3. The activated sludge process is an

  4. Consider the following statements regarding contact stabilization process:

    1. Primary settling tank is not required in some cases.

    2. BOD removal occurs in two stages.

    3. Aeration volume requirements are approximately 50% of those of a conventional – or tapered – aeration plant.

    4. Returned sludge is aerated for 30 min to 90 min in sludge aeration tank.

    Which of the above statements are correct?
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