Analyze kLa using clean inputs and practical assumptions. View trends, saturation limits, and deficits instantly. Download reports, compare scenarios, and support bioprocess decisions confidently.
Effective saturation concentration: C*effective = C*clean × β × pressure factor.
Gassing-out method: kLa = -ln[(C* - Ct) / (C* - C0)] / t. Use this when oxygen uptake is negligible during the measurement window.
Dynamic method with oxygen uptake: Ct = Css + (C0 - Css)e-kLa·t, where Css = C* - OUR / kLa. The file solves kLa numerically from the measured endpoint.
Instantaneous oxygen transfer rate: OTR = kLa(C* - CL). Multiply OTR by working volume to estimate vessel oxygen transfer in mg/h.
Clean-water equivalent: kLa,clean = kLa,process / α. This is useful when you want a quick comparison against clean-water benchmark data.
| Mode | C0 | Ct | C*clean | β | Pressure | Time | Volume | α | Target DO | Approx. kLa |
|---|---|---|---|---|---|---|---|---|---|---|
| Gassing-out | 2.10 mg/L | 6.40 mg/L | 8.20 mg/L | 1.00 | 1.00 | 8 min | 1200 L | 0.75 | 3.00 mg/L | 9.15 1/h |
kLa combines the liquid-film transfer coefficient and gas-liquid interfacial area. It describes how quickly oxygen moves from bubbles into liquid volume. Higher values usually indicate better oxygen delivery under the tested operating conditions.
Use it when oxygen uptake during the measurement is negligible. That is common in water tests, media tests without active cells, or short trials where biological demand does not distort the dissolved oxygen rise.
Use it during live culture operation or any case where oxygen is consumed while dissolved oxygen recovers. A known oxygen uptake rate helps separate transfer performance from biological demand.
They adjust clean-water saturation to operating conditions. Beta reflects media effects on oxygen solubility. The pressure factor accounts for deviations from the reference pressure used for the clean-water saturation value.
Alpha relates process kLa to clean-water kLa. This page reports a clean-water equivalent by dividing the estimated process value by alpha, giving a quick benchmark for equipment comparison.
That output estimates oxygen transfer capacity at a control point you care about. It helps compare whether the aeration and agitation setup can support expected culture demand near the chosen dissolved oxygen target.
Enter OUR in mg/L/h in this file. The solver expects that basis. Keep dissolved oxygen and saturation values in mg/L and use one consistent time interval for the measured oxygen recovery.
Impossible combinations can cause solver failure. Examples include end dissolved oxygen above effective saturation, zero time, negative uptake, or values that do not fit the assumed first-order transfer model.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.