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Question 62
GATE BT 2025 • Q62
NAT • 2 Marks
Section 4: Bioprocess Engineering and Process Biotechnology
Bioreactor types, scale-up
Subtopic: Fundamentals of Bioreactor types, scale-up
Question Statement:
A 2 L bioreactor is being operated as a chemostat, at a flow rate of 0.8 L/h and
sterile feed of 10 g/L substrate. The bacterial growth follows Monod kinetics at
a maximum specific growth rate of 0.6 h-1 with a Monod constant of 0.5 g/L and
a biomass yield coefficient of 0.4 g/g.
The exit biomass concentration is _______ g/L.
(Round off to one decimal place)
Official Answer Key:
3.4 to 3.8
Step-by-Step Solution & Explanation
### **Step-by-Step Solution & Mathematical Derivation (GATE BT 2025 Q.62)**
**1. Governing Concept & Definition**:
- **Topic**: Continuous Bioreactor Kinetics & Steady-State Chemostat Operation
- In a sterile-feed chemostat without cell death:
$D = \frac{F}{V} = \mu$
where $D$ is the dilution rate, and $\mu = \frac{\mu_{\max} S}{K_s + S}$.
- At steady state, biomass concentration $X$ is given by substrate balance:
$X = Y_{X/S} (S_0 - S)$
**2. Detailed Step-by-Step Calculation**:
- **Given**:
- Reactor volume $V = 2\text{ L}$, Flow rate $F = 0.8\text{ L/h}$
- Dilution rate: $D = \frac{F}{V} = \frac{0.8}{2} = 0.4\text{ h}^{-1}$
- Feed substrate concentration $S_0 = 10\text{ g/L}$
- $\mu_{\max} = 0.6\text{ h}^{-1}$, $K_s = 0.5\text{ g/L}$, $Y_{X/S} = 0.4\text{ g/g}$
- **Step 1: Calculate residual substrate concentration $S$**:
$D = \mu = \frac{\mu_{\max} S}{K_s + S} \implies 0.4 = \frac{0.6 S}{0.5 + S}$
$0.4(0.5 + S) = 0.6 S \implies 0.2 + 0.4 S = 0.6 S \implies 0.2 S = 0.2 \implies S = 1.0\text{ g/L}$
- **Step 2: Calculate steady-state exit biomass concentration $X$**:
$X = Y_{X/S} (S_0 - S) = 0.4 \times (10 - 1.0) = 0.4 \times 9.0 = 3.6\text{ g/L}$
**3. Final Answer**:
- **Calculated Value**: **3.6 g/L**
- **Official GATE Accepted Range**: **3.4 to 3.8**
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