GATE BT 2016 • Q27 MCQ • 1 Mark

Section 4: Bioprocess Engineering and Process Biotechnology

Bioreactor types, scale-up

Subtopic: Fundamentals of Bioreactor types, scale-up

Question Statement:

Which set of the following events occurs during the elongation step of translation? P. Attachment of mRNA with the smaller subunit of ribosome Q. Loading of correct aminoacyl-tRNA into the A site R. Formation of a peptide bond between the amino acyl-tRNA in the A site and the peptide chain that is attached to the peptidyl-tRNA in the P site S. Dissociation of the ribosomal subunits T. Translocation of peptidyl-tRNA from the A site to the P site of the ribosome (A) P, Q and R (B) P, Q and T (C) Q, R and T (D) R, S and T

Options:

  • (A) P, Q and R
  • (B) P, Q and T
  • (C) Q, R and T
  • (D) R, S and T

Official Answer Key:

B

Step-by-Step Solution & Explanation

### **Official Solution & Step-by-Step Derivation (GATE BT 2016 Q.27)** **1. Governing Concept & Question Classification**: - **Section**: BT - **Question Type**: **MCQ** (1 Mark) - **Topic**: Bioprocess Engineering / Fermentation Technology (Fed-Batch Operation Advantages) **2. Detailed Step-by-Step Analysis**: - In **fed-batch cultivation**, nutrients are incrementally supplied to the bioreactor over time without removing culture fluid until the harvest: - **P. Processes with substrate inhibition**: - High starting concentrations of carbon sources (e.g., glucose, methanol) can inhibit microbial growth or trigger overflow metabolism (Crabtree effect in yeast, acetate accumulation in *E. coli*). Fed-batch cultivation maintains residual substrate concentration $[S]$ below the inhibitory threshold by feeding nutrients continuously at controlled rates. $\implies$ **P is SUITABLE**. - **Q. Processes with product inhibition**: - In fed-batch culture, volume increases and cells grow, but toxic products accumulate and are not removed (unlike continuous or perfusion systems). Severe product inhibition is typically mitigated by continuous product removal (chemostat with cell recycle or extractive fermentation), not standard fed-batch. - **R. High cell density cultivation (HCDC)**: - Achieving extreme biomass concentrations (
gt; 50 - 100\text{ g/L}$ dry cell weight) in batch culture is impossible because adding all necessary nutrients at the beginning causes severe osmotic stress and substrate inhibition. Fed-batch feeding delivers massive cumulative nutrients gradually while maintaining low osmotic pressure and optimal specific growth rates. $\implies$ **R is SUITABLE**. - Therefore, fed-batch cultivation is particularly suitable for **P and R only**. - **Option-by-Option Evaluation**: - **Option (A) [INCORRECT]**: Fed-batch does not remove inhibitory products. - **Option (B) [CORRECT]**: P (controlling substrate inhibition) and R (high cell density cultivation) are the primary engineering motivations for fed-batch fermentations. - **Option (C) [INCORRECT]**: Includes product inhibition. - **Option (D) [INCORRECT]**: Product inhibition is poorly managed by conventional fed-batch. **3. Final Answer / Verification Summary**: - **Official GATE Answer Key**: **B** - **Scoring Criteria**: +1.0 Mark (Negative marking: -0.33 marks).

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