Q.38 Match the downstream processes in Group I with the products in Group II. Group I                                                                                       Group II P. Solvent extraction                                                              1. Lactic acid Q. Protein-A linked affinity chromatography                   2. Penicillin R. Extractive distillation                                                        3. Monoclonal antibody S. Salting out                                                                            4. Lipase (A) P-2, Q-3, R-1, S-4 (B) P-4, Q-1, R-2, S-3 (C) P-4, Q-1, R-3, S-2 (D) P-2, Q-4, R-1, S-3

Q.38 Match the downstream processes in Group I with the products in Group II.
Group I                                                                                       Group II
P. Solvent extraction                                                              1. Lactic acid
Q. Protein-A linked affinity chromatography                   2. Penicillin
R. Extractive distillation                                                        3. Monoclonal antibody
S. Salting out                                                                            4. Lipase
(A) P-2, Q-3, R-1, S-4 (B) P-4, Q-1, R-2, S-3
(C) P-4, Q-1, R-3, S-2 (D) P-2, Q-4, R-1, S-3

Downstream processing recovers and purifies bioproducts from fermentation broth, accounting for 50-80% of total costs in industrial biotechnology. Solvent extraction separates antibiotics like penicillin using organic solvents, while Protein-A affinity chromatography specifically purifies monoclonal antibodies. This MCQ tests critical matching skills for fermentation-derived products central to pharmaceutical biotech.

Technique-Product Matches

Solvent extraction (P): Organic solvent (butyl acetate) extracts penicillin G from acidic fermentation broth, exploiting its solubility shift at pH 2-3.
Protein-A linked affinity chromatography (Q): Bacterial Protein-A binds Fc region of monoclonal antibodies (mAbs), enabling >95% purity in single step for biotherapeutics.
Extractive distillation (R): Reactive distillation with aldehyde extractants converts lactic acid to lactate ester, facilitating purification from dilute aqueous streams.
Salting out (S): Ammonium sulfate precipitation selectively recovers extracellular lipase enzymes based on hydrophobicity differences.

Group II Products

  1. Lactic acid: Organic acid from Lactobacillus fermentation

  2. Penicillin: β-lactam antibiotic from Penicillium chrysogenum

  3. Monoclonal antibody: Immunoglobulin G from CHO/mammalian cell culture

  4. Lipase: Triacylglycerol hydrolase from microbial sources

Correct Answer

Option (A) P-2, Q-3, R-1, S-4 represents standard industrial bioprocess matching.

Group I Technique Matches Product Industrial Application
P Solvent extraction 2 Penicillin Classical antibiotic recovery [60% global production]
Q Protein-A chromatography 3 Monoclonal antibody mAb purification ($200B market)
R Extractive distillation 1 Lactic acid PLA biopolymer precursor
S Salting out 4 Lipase Detergent/biofuel enzyme

Option Explanations

(A) P-2, Q-3, R-1, S-4: Correct. Solvent extraction standard for penicillin since 1940s; Protein-A gold standard for mAbs; extractive distillation for lactic acid purification; salting-out routine for lipases.

(B) P-4, Q-1, R-2, S-3: Incorrect. Solvent extraction (P-4) unsuitable for lipase (aqueous enzyme); Protein-A (Q-1) doesn’t bind lactic acid; extractive distillation (R-2) mismatches penicillin chemistry.

(C) P-4, Q-1, R-3, S-2: Incorrect. Multiple mismatches: solvent extraction not primary for lipase; Protein-A irrelevant for lactic acid; salting-out ineffective for heat-stable penicillin.

(D) P-2, Q-4, R-1, S-3: Partially correct but wrong. Protein-A (Q-4) doesn’t purify lipases (no Fc region); salting-out (S-3) can’t recover antibodies from complex media.

Bioprocess Engineering Context

Penicillin solvent extraction achieves 90% recovery using dual-phase countercurrent systems. Protein-A chromatography costs $1000-2000/L resin but enables platform purification for 70% of approved mAbs. Extractive distillation solves lactic acid’s azeotrope issue for 100 g/L+ concentrations. Salting-out reduces lipase purification steps from 5 to 2, cutting costs 40%. These techniques optimize your fermentation processes for industrial-scale enzyme/antibiotic production.

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