23-Chem-B4 Biochemical Engineering · May 2017
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exam 16-Chem-B4, Biochemical Engineering — May 2017. 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.
Both approaches share the same underlying design tool — the Del factor (∇), a lumped measure of the "kill" delivered to the most heat-resistant contaminant (bacterial spores), obtained by integrating an Arrhenius-type first-order death-rate constant kd(T)=A·e−Ed/RT over the whole time–temperature history of the medium: $$\nabla=\int_0^{t_{total}} k_d(T)\,dt=\ln\!\left(\frac{N_0}{N_f}\right)$$ Because nutrients (vitamins, amino acids, some proteins) also degrade thermally but with a lower activation energy than spore destruction, a short burst at high temperature achieves the same spore-kill ∇ with far less nutrient loss than a long soak at low temperature — this single fact is what separates the two sterilization philosophies below.
In batch sterilization the entire medium charge is sterilized inside the production fermenter itself, usually by steam supplied to the vessel jacket/internal coil and/or injected directly into the bulk medium. Because the heat-up and cool-down ramps are slow (a large vessel of liquid, and often solid/particulate ingredients that heat more slowly than the bulk liquid, has a large thermal mass relative to the heat-transfer area), the medium spends a long time at intermediate temperatures where nutrients degrade with very little useful spore-kill credit — the ∇ contributed during the ramps is added to the hold-period ∇ to reach the design target, but a disproportionate share of nutrient loss also happens during those same slow ramps.
In continuous (HTST — high-temperature, short-time) sterilization, raw medium is pumped continuously through a small-diameter heater (a plate/tubular heat exchanger, or direct steam injection), then a holding tube sized so the residence time at temperature delivers the required ∇, then a cooler, before flowing into a pre-sterilized fermenter. Because the flowing medium is heated and cooled in a thin, high-surface-area stream, the heat-up and cool-down each take only seconds, so almost the entire ∇ is accumulated during the short, well-controlled hold — and comparatively little nutrient is destroyed during the (now negligible) ramps.
| Feature | Batch (in-situ) | Continuous (HTST) |
|---|---|---|
| Heat-up/cool-down time | Long (tens of minutes; large thermal mass, small area/volume ratio) | Short (seconds; thin flowing stream, high area/volume ratio) |
| Nutrient destruction | Higher — ramps contribute significant, poorly-controlled thermal exposure | Lower — ramps are brief, so ∇ is accumulated almost entirely in the controlled hold |
| Equipment/capital cost | Lower — uses the fermenter itself, no extra heat exchangers | Higher — dedicated heater, holding tube, cooler, and controls |
| Suitability for particulates | Better — solids/particulates heat with the bulk, no risk of plugging small passages | Poorer — particulates can foul/plug narrow heat-exchanger channels or lag the fluid's thermal history |
| Process control/reproducibility | Lower — batch-to-batch ramp variability, manual/PLC-timed hold | Higher — steady-state flow and temperature control, consistent ∇ every batch |
| Scale-up | Simple in concept, but ramps get proportionally slower (worse) as vessel size grows | Scales by increasing flow through the same tube/HX design, ramp times stay short regardless of total volume |
| Typical use | Small/pilot scale, particulate-containing or delicate media, simpler control systems | Large-scale industrial fermentation with clear/low-particulate, nutrient-sensitive media |
| Approach | Governing advantage | Governing disadvantage |
|---|---|---|
| Batch (in-situ) | Low capital, simple, handles particulates | Slow ramps destroy more nutrient, less reproducible |
| Continuous (HTST) | Short ramps preserve nutrient value, highly reproducible, scales cleanly | Higher capital, poor for particulate-laden media |