NivaarExam PrepOfficial exam papers ↗

23-Chem-B4 Biochemical Engineering · May 2017

Question 3 of 5: Batch vs. Continuous Sterilization of Nutrient Media

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

Notes on this paper

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 3: Batch vs. Continuous Sterilization of Nutrient Media (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.

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.

(a) Batch (in-situ) sterilization

Tt (time)T set-point (~121°C)heat-upholdcool-down
Fig. 3a — batch (in-situ) sterilization: the whole fermenter and its full medium charge is heated (typically by steam injection or a jacket/coil), held at the sterilization temperature, then cooled, all as one continuous time profile inside the same vessel.

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.

(b) Continuous sterilization

Heater(HX orsteam)HoldingtubeCoolerRaw medium in(cold)Rapidheat-upHeld, sec–minSterile mediumout (cold)
Fig. 3b — continuous sterilization: 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.

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.

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
Equipment/capital costLower — uses the fermenter itself, no extra heat exchangersHigher — dedicated heater, holding tube, cooler, and controls
Suitability for particulatesBetter — solids/particulates heat with the bulk, no risk of plugging small passagesPoorer — particulates can foul/plug narrow heat-exchanger channels or lag the fluid's thermal history
Process control/reproducibilityLower — batch-to-batch ramp variability, manual/PLC-timed holdHigher — steady-state flow and temperature control, consistent ∇ every batch
Scale-upSimple in concept, but ramps get proportionally slower (worse) as vessel size growsScales by increasing flow through the same tube/HX design, ramp times stay short regardless of total volume
Typical useSmall/pilot scale, particulate-containing or delicate media, simpler control systemsLarge-scale industrial fermentation with clear/low-particulate, nutrient-sensitive media
ApproachGoverning advantageGoverning disadvantage
Batch (in-situ)Low capital, simple, handles particulatesSlow ramps destroy more nutrient, less reproducible
Continuous (HTST)Short ramps preserve nutrient value, highly reproducible, scales cleanlyHigher capital, poor for particulate-laden media