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.
Continuous HTST sterilization pumps the medium steadily through a small-diameter heater, a holding tube sized for the required residence time, and a cooler, rather than heating and cooling one large batch charge in place inside the fermenter.
Raw medium is heated rapidly (a plate/tubular heat exchanger, or direct steam injection) to the sterilization temperature, held for a precisely-timed interval in the holding tube, then cooled, before flowing into a pre-sterilized fermenter. Because the flowing medium presents a thin, high-surface-area-to-volume stream to the heater and cooler, the heat-up and cool-down each take only seconds — the same physical reason the batch process (Question 2(ii)) is slow, but inverted: HTST deliberately maximizes the heat-transfer area relative to the volume being processed at any instant, instead of heating one large fixed volume through a comparatively small vessel wall.
| 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 |
| Process control/reproducibility | Lower — batch-to-batch ramp variability | Higher — steady-state flow/temperature control gives consistent ∇ every run |
| Scale-up | Ramps get proportionally slower as vessel size grows | Scales by increasing flow through the same tube/HX design; ramp times stay short |
| Equipment/capital cost | Lower — uses the fermenter itself | Higher — dedicated heater, holding tube, cooler, controls |
| Advantage of continuous HTST over batch | Underlying reason |
|---|---|
| Higher nutrient retention | Seconds-long ramps vs. tens-of-minutes ramps at the same target ∇ |
| Reproducible sterility, batch to batch | Steady-state flow/temperature control replaces manual/PLC-timed heat-up |
| Clean, ramp-independent scale-up | Larger throughput = more flow through the same tube/HX geometry, not a bigger thermal mass |