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Modelling gradient elution of bioactive multicomponent systems in non-linear ion-exchange chromatography
A Wiesel1, H Schmidt-Traub, J Lenz
1Department of Chemical Engineering, University of Dortmund, 44221 Dortmund, Germany.
Journal of Chromatography. A
|August 27, 2003
Summary
A new model describes non-linear ion-exchange chromatography for bioactive substances, considering both ion-exchange and adsorption. This framework aids process design by revealing that column loading, not elution gradients, primarily determines separation.
Area of Science:
- Biochemical Engineering
- Separation Science
- Chromatography
Background:
- Non-linear ion-exchange chromatography is crucial for purifying bioactive substances.
- Existing models often simplify complex binding interactions, limiting process design accuracy.
Purpose of the Study:
- Develop a theoretical framework for non-linear ion-exchange chromatography of bioactive substances.
- Create a model basis for production-scale ion-exchange chromatography process design.
Main Methods:
- Developed a theoretical model incorporating ion-exchange and adsorption mechanisms.
- Utilized Gouy-Chapman theory for counter-ion distribution and extended it for selectivity.
- Simulated adsorption-elution cycles, varying column loading, eluent concentration, and multicomponent systems.
Main Results:
- Experimental data showed a transition from Langmuir to sigmoidal isotherms at higher eluent concentrations.
- The model accurately predicted non-linear elution profiles with desorption fronting.
- Simulations revealed that column loading significantly impacts separation more than elution gradients.
Conclusions:
- The developed model provides insights into biochromatography phenomena, including non-linear binding and the influence of contaminants.
- Separation is predominantly governed by the loading step, challenging conventional process design strategies.
- The framework supports the design of production-scale ion-exchange chromatography for diverse bioactive molecules.