23-Chem-B4 Biochemical Engineering · May 2018
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exam 16-Chem-B4, Biochemical Engineering — May 2018. 3 hours, Closed-Book Exam (any non-communicating Casio or Sharp calculator permitted). Per the exam notes, FIVE (5) questions constitute a complete paper and all five must be answered; most require a short-essay-format answer, and clarity/organization of the answer are explicitly marked.
Reference texts: Shuler & Kargi, Bioprocess Engineering: Basic Concepts, 2nd ed.; Bailey & Ollis, Biochemical Engineering Fundamentals, 2nd ed.; Madigan et al., Brock Biology of Microorganisms, 13th ed.
Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.
Many valuable bioproducts (recombinant proteins, intracellular enzymes, some polysaccharides) accumulate inside the cell rather than being secreted, so downstream processing must first rupture the cell envelope to release them before purification can begin. Cell disruption methods fall into four broad categories — mechanical, physical, chemical, and enzymatic — that trade off disruption efficiency, product damage, scale-up cost, and selectivity.
High-pressure homogenization pumps a concentrated cell slurry through a narrow discharge valve at pressures of 500–1500+ bar; the combination of intense shear as the fluid accelerates through the gap, cavitation as it re-expands, and impingement on the valve seat ruptures the cell wall. It is the industrial standard for bacteria and yeast at large scale (continuous operation, high throughput, well-established equipment) but the heat generated by the pressure drop requires cooling, and it does relatively little for tough, fibrous, or filamentous organisms.
Bead milling agitates the cell suspension with small glass or ceramic beads in a high-speed stirred chamber; cells rupture from bead–cell collisions and shear in the flow field around the beads. It scales well continuously and handles a broad range of organisms including fungi, but generates significant heat (needs jacket cooling) and the equipment is harder to clean/sterilize (CIP) than a homogenizer valve.
Ultrasonication uses a probe vibrating at ultrasonic frequency to generate cavitation bubbles in the liquid; their violent collapse creates local shock waves and shear that rupture nearby cells. It is fast and effective at lab/bench scale, but poorly scalable (only a small volume near the probe tip is effectively treated) and generates substantial local heating, which can denature heat-sensitive products.
Freeze–thaw cycling repeatedly freezes and thaws the cell suspension; ice-crystal formation inside the cell physically ruptures the membrane. It is gentle on some products and simple to execute, but slow, energy-intensive at scale, and often gives incomplete disruption on its own (usually paired with another method).
Detergents (e.g. Triton X-100, SDS) and organic solvents solubilize the lipid bilayer, and alkali/acid treatment can hydrolyze wall components; osmotic shock (rapid transfer from a concentrated to a dilute buffer) ruptures osmotically-fragile cells by uncontrolled water influx. Chemical methods are gentle and highly selective (can be tuned to leak periplasmic content without fully lysing the cell), scale easily, and need no specialized equipment — but reagent cost is significant at large scale, the chemicals must be removed downstream (adding a purification step and cost), and they can be ineffective against organisms with a tough cell wall (e.g. some fungi, spores).
Lytic enzymes (e.g. lysozyme for the bacterial peptidoglycan wall, zymolyase for fungal cell walls) digest specific wall components, weakening the cell to the point that even mild subsequent osmotic or mechanical treatment completes lysis. Enzymatic lysis is the gentlest and most selective option (minimal damage to the target product) and works well combined with chemical permeabilization, but enzyme cost is high at production scale and the added protein itself becomes a downstream-processing contaminant that must later be removed.
| Category | Method | Key advantage | Key disadvantage |
|---|---|---|---|
| Mechanical | High-pressure homogenizer | Industrial-scale, continuous, high throughput | Heat generation; weak on tough/filamentous cells |
| Mechanical | Bead mill | Broad organism range incl. fungi | Heat generation; harder to clean/sterilize |
| Physical | Ultrasonication | Fast, effective at small scale | Poor scalability; local heating |
| Physical | Freeze–thaw | Gentle, simple | Slow; usually incomplete alone |
| Chemical | Detergent/solvent/osmotic shock | Gentle, selective, no special equipment | Reagent cost; must be removed downstream |
| Enzymatic | Lysozyme / zymolyase | Gentlest, most selective | High enzyme cost; adds a contaminant |