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Related Concept Videos

Dialysis01:15

Dialysis

Dialysis is a diffusion-based purification process that separates analyte molecules from a complex matrix. This is accomplished by allowing molecules in the solution to pass through a semipermeable membrane into a liquid on the other side. The membrane is usually made of cellulose acetate or cellulose nitrate, and the second liquid must be miscible with the solution. Ions (e.g., chloride or sodium) or organic molecules (e.g., glucose) can pass through the membrane pores, which generally have...
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Three-Dimensionally Printed Microfluidic Cross-flow System for Ultrafiltration/Nanofiltration Membrane Performance Testing
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Dynamic ultrafiltration model for proteins: a colloidal interaction approach.

W R Bowen1, P M Williams

  • 1Biochemical Engineering Group, Department of Chemical Engineering, University of Wales, Swansea, SA2 8PP United Kingdom.

Biotechnology and Bioengineering
|April 20, 1996
PubMed
Summary
This summary is machine-generated.

A new mathematical model accurately predicts protein ultrafiltration rates by detailing protein interactions near membranes. This model offers quantitative predictions without adjustable parameters, validated with bovine serum albumin (BSA) filtration data.

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Area of Science:

  • Biophysics
  • Chemical Engineering
  • Materials Science

Background:

  • Ultrafiltration is crucial for protein separation and purification.
  • Accurate prediction of permeation rates is essential for optimizing membrane processes.
  • Existing models often lack detailed descriptions of protein-protein interactions at the membrane interface.

Purpose of the Study:

  • To develop a rigorous dynamic mathematical model for predicting protein ultrafiltration rates.
  • To incorporate sophisticated descriptions of protein-protein interactions controlling permeation.
  • To enable quantitative, a priori predictions of filtration rates based on system parameters.

Main Methods:

  • Developed a dynamic mathematical model based on protein-protein interactions near the membrane surface.
  • Accounted for electrostatic interactions using a Wigner-Seitz cell approach and nonlinear Poisson-Boltzmann equation.
  • Calculated London-van der Waals forces using approximated screened, retarded Lifshitz-Hamaker constants.
  • Incorporated configurational entropy effects and electroviscous effects.

Main Results:

  • The model quantitatively predicts protein filtration rates.
  • Predictions are a function of zeta potential, pH, ionic strength, applied pressure, protein size, and membrane resistance.
  • The model shows excellent agreement with experimental data for bovine serum albumin (BSA) filtration.

Conclusions:

  • The developed model provides a robust framework for predicting protein ultrafiltration.
  • The model's accuracy is demonstrated through validation with experimental BSA filtration data.
  • This a priori model, with no adjustable parameters, advances the understanding and optimization of membrane-based protein separation processes.