The tank is modelled as a well-mixed continuous stirred-tank reactor running unstructured Monod growth kinetics with double substrate/oxygen limitation, plus Luedeking-Piret product formation — the same equations used to design real fermenters for insulin, antibiotics, ethanol and enzymes:
μ = μmax(T) · S/(Ks+S) · DO/(Ko+DO)
dX/dt = (μ − D)·X
dS/dt = −μX/Yxs − msX + D(S₀−S)
dP/dt = αμX + βX − D·P
dDO/dt = kLa·(100−DO) − μX/Yxo
μmax(T) = μmax0 · exp(−(T−37)²/128)
- Dilution rate D — feed/outflow rate per reactor volume in continuous (chemostat) mode. Above the critical dilution rate D꜀ = μmax·S₀/(Ks+S₀), cells wash out faster than they can divide and biomass collapses to zero even though feed keeps flowing — a real, load-bearing failure mode in industrial continuous culture.
- Feed substrate S₀ — glucose concentration entering the vessel. Sets the steady-state biomass ceiling (X꜀ₛ ≈ Yxs·(S₀−S꜀ₛ)) but very high S₀ + high D pushes the system toward washout sooner in relative terms.
- Aeration kLa — the volumetric oxygen transfer coefficient (how fast the sparger + impeller can resupply dissolved O₂). If oxygen uptake by growing cells (μX/Yxo) outpaces kLa's resupply, dissolved oxygen collapses and throttles μ through the DO/(Ko+DO) term — the classic "oxygen-limited fermentation" every scale-up engineer fights.
- Temperature — μmax follows a Gaussian response peaking near 37 °C (mesophilic organism); too cold slows metabolism, too hot denatures enzymes — both cut growth rate.
Cell colour tracks instantaneous μ (yellow = slow/lag, green = fast exponential growth, grey = stalled or washing out); bubble rate tracks kLa; the liquid tint darkens toward amber as product P accumulates, the way a real fermentation broth changes colour as metabolites build up.