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 )
6.92 mg/L
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 ($\mu_{max}$).
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:
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:
$$ D = \frac{1}{\theta} = \frac{1}{4 \text{ days}} = 0.25 \text{ day}^{-1} $$
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:
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 $S$:
$$ S = \frac{18.6}{2.69} $$
$$ S \approx 6.9145 \text{ mg/L} $$
The calculated effluent BOD5 concentration is approximately 6.92 mg/L. Comparing this value to the given options, it matches the first option.
Consider the following statements in respect of anaerobic sludge digester:
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?Chlorine is sometimes used in sewage treatment:
The activated sludge process is an
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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?