Model oxygen transfer with practical inputs and process assumptions. Check deficits, totals, efficiency, and aeration. Use responsive fields, exports, examples, formulas, and FAQs confidently.
| Parameter | Example Value |
|---|---|
| kLa | 2.50 1/h |
| Saturation Concentration C* | 7.80 mg/L |
| Current Dissolved Oxygen CL | 3.80 mg/L |
| Working Volume | 1200 L |
| Process Time | 6 h |
| OUR | 7.00 mg/L/h |
| Gas Flow | 1000 L/min |
| Oxygen Fraction | 21 % |
| Calculated Volumetric OTR | 10.0000 mg/L/h |
| Calculated Total OTR | 12.0000 g/h |
| Batch Oxygen Transferred | 72.0000 g |
| Required kLa for OUR | 1.7500 1/h |
The core oxygen transfer expression is OTR = kLa × (C* − CL). Here, kLa is the volumetric mass transfer coefficient, C* is the saturation oxygen concentration, and CL is the current dissolved oxygen concentration.
Volumetric OTR is reported in mg/L/h. Total oxygen transfer is found by multiplying volumetric OTR by working volume. Batch oxygen transfer is found by multiplying total OTR by process time. This gives a practical estimate of oxygen movement into the liquid phase.
When you select estimated saturation mode, the calculator approximates C* from temperature, altitude, and salinity corrections. Temperature reduces oxygen solubility, altitude lowers partial pressure, and salinity decreases dissolved oxygen capacity. These corrections support realistic screening calculations during fermentation and bioprocess planning.
Required kLa is estimated from Required kLa = OUR ÷ (C* − CL). A safety factor can then be applied to create a design target. Apparent transfer efficiency compares transferred oxygen against oxygen entering through the gas stream.
Oxygen transfer rate measures how quickly oxygen moves from gas into liquid. It helps evaluate whether aeration and mixing can support cell growth, respiration, or oxidation demand.
kLa combines liquid film transfer and interfacial area into one practical term. Higher kLa usually means stronger oxygen delivery under the same concentration driving force.
The driving force is the difference between saturation concentration and actual dissolved oxygen concentration. A larger difference produces a higher oxygen transfer rate for the same kLa.
Comparing OTR with OUR shows whether oxygen delivery can keep up with biological demand. If OTR is lower than OUR, dissolved oxygen may fall during operation.
Yes. Estimated saturation mode is useful for screening studies. It applies practical corrections for temperature, altitude, and salinity when direct C* measurements are unavailable.
Use kLa in 1/h, concentrations in mg/L, working volume in liters, time in hours, gas flow in liters per minute, and oxygen fraction in percent.
Transfer efficiency estimates how much incoming oxygen appears as transferred oxygen. It is a screening metric and should be interpreted with process assumptions and measurement limits in mind.
It is suitable for preliminary design, process checks, and training. Final equipment design should also consider hydrodynamics, pressure, broth rheology, probe calibration, and validated plant data.
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.