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23-Chem-B4 Biochemical Engineering · May 2018

Question 3 of 5: Continuous HTST Sterilization — Flowsheet and Advantages Over the Batch Process

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

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 3: Continuous HTST Sterilization — Flowsheet and Advantages Over the Batch Process (20 marks)

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.

Heater(HX orsteam)HoldingtubeCoolerRaw medium in(cold)Rapidheat-upHeld, sec–minSterile mediumout (cold)
Fig. 3 — continuous HTST sterilization train: medium flows through a heater (direct steam injection or an indirect heat exchanger), a holding tube sized for the required residence time, and a cooler, so heat-up and cool-down each take seconds instead of the tens of minutes a whole vessel needs.

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.

FeatureBatch (in-situ)Continuous (HTST)
Heat-up/cool-down timeLong (tens of minutes; large thermal mass, small area/volume ratio)Short (seconds; thin flowing stream, high area/volume ratio)
Nutrient destructionHigher — ramps contribute significant, poorly-controlled thermal exposureLower — ramps are brief, so ∇ is accumulated almost entirely in the controlled hold
Process control/reproducibilityLower — batch-to-batch ramp variabilityHigher — steady-state flow/temperature control gives consistent ∇ every run
Scale-upRamps get proportionally slower as vessel size growsScales by increasing flow through the same tube/HX design; ramp times stay short
Equipment/capital costLower — uses the fermenter itselfHigher — dedicated heater, holding tube, cooler, controls
Advantage of continuous HTST over batchUnderlying reason
Higher nutrient retentionSeconds-long ramps vs. tens-of-minutes ramps at the same target ∇
Reproducible sterility, batch to batchSteady-state flow/temperature control replaces manual/PLC-timed heat-up
Clean, ramp-independent scale-upLarger throughput = more flow through the same tube/HX geometry, not a bigger thermal mass
Check: continuous HTST is the better choice specifically for large-scale, low-particulate, nutrient-sensitive media; for particulate-laden or very small/pilot-scale batches the simpler in-situ batch process (Question 2(ii)) can still be the more practical engineering choice despite its lower nutrient retention.