What Is the Hollow-Fiber Ultrafiltration Permeate Flux Calculator?
Crossflow ultrafiltration forces feed broth tangentially across hollow fibers to sweep rejected solutes away and limit fouling cake buildup.
As rejected proteins accumulate at the membrane wall, concentration polarization creates an osmotic backpressure and viscous gel layer.
How Does the Hollow-Fiber Ultrafiltration Permeate Flux Calculator Work?
At low TMP, flux increases linearly with pressure in the clean membrane Darcy regime.
At higher TMP, solute convective arrival matches back-diffusion into the bulk, causing flux to plateau at a constant gel-layer limit independent of pressure.
Hollow-Fiber Ultrafiltration Permeate Flux Calculator Formula & Variables
The core mathematical equation utilized by this calculator is expressed as:
Calculates pressure-driven clean flux and film-theory mass-transfer gel polarization limiting flux.
How to Use the Hollow-Fiber Ultrafiltration Permeate Flux Calculator
- Enter transmembrane pressure (TMP) in bar and membrane permeability in LMH/bar.
- Input bulk feed concentration and known gel polarization concentration Cg.
- Specify boundary layer mass transfer coefficient k (determined from Graetz-Leveque correlations).
Step-by-Step Example Calculation
Ultrafiltration Flux Standard Case
Input Values:
Understanding Your Result
Actual permeate flux indicates the sustainable operating processing rate in LMH (liters per m2 per hour).
Filtration regime indicates whether increasing TMP will yield higher throughput or merely compress foulant cakes.
Operating slightly below the gel-polarized threshold prevents severe membrane fouling.
Factors That Affect the Result
- Crossflow shear rate: Higher lumen recirculation velocity elevates k, directly raising the gel-limiting flux.
- Bulk concentration Cb: As filtration concentrates the retentate batch, ln(Cg/Cb) shrinks, reducing flux.
- Temperature: Higher temperatures lower broth viscosity and increase Brownian solute diffusivity.
When Should You Use This Calculator?
- Sizing membrane area for downstream biopharmaceutical ultrafiltration/diafiltration (UF/DF) systems.
- Optimizing crossflow harvest of monoclonal antibodies, vaccines, and recombinant enzymes.
Assumptions & Limitations
- Assumes 100% solute membrane rejection (reflection coefficient sigma = 1.0).
- Does not model long-term pore adsorption or irreversible chemical scaling.
Frequently Asked Questions
Calculation Accuracy & Reference Note
Film-theory concentration polarization formulation coupled with linear Darcy hydraulic permeability.