| t (min) | OD₆₀₀ | [S] g/L | [P] g/L |
|---|
Fitted kinetic constants μ_max = — and half-saturation K_s = 0.50 g/L ready to feed into Monod Bioreactor Yield & Maintenance (Step 4).
Step 3 of 5: Non-linear regression parameter estimation (Monod, Haldane, Hinshelwood, Moser, Tessier, Logistic) from experimental OD vs. time curves. • 100% Free & Open Access.
| t (min) | OD₆₀₀ | [S] g/L | [P] g/L |
|---|
Extracting robust kinetic constants from experimental fermentation data requires fitting sigmoidal mathematical growth models across the entire time-course. This tool performs non-linear least squares regression using Logistic, Gompertz, and Richards empirical models to identify maximum carrying capacity ($X_{\max}$), maximum specific growth rate ($\mu_{\max}$), and lag duration ($\lambda$).
| Model | Symmetry | Best Suited For | Parameters |
|---|---|---|---|
| Logistic | Symmetric | Standard batch fermentation without pronounced lag | X_0, X_max, μ_max |
| Gompertz | Asymmetric | Cultures with extended lag and decelerating plateau | X_0, A, μ_max, λ |
| Richards | Flexible Inflection | Complex multi-substrate or diauxic growth curves | X_0, A, μ_max, λ, ν |
This calculator is maintained by the simulation engineers at BioFlo Bioprocess Engineering. We specialize in industrial bioreactor design, computational fluid dynamics (CFD) modeling, oxygen mass transfer optimization, and custom digital twin development for pharmaceutical fermentation plants.