Industrial downstream process development – high load densities challenge modeling approaches
Within the past few years, model-based approaches have emerged as a flexible, fast and cheap tool for industrial process development, optimization and characterization, as well as facility fitting. Hereby, the commonly used model for ion exchange chromatography is “Steric Mass Action” theory (SMA). It is based on the assumption that a higher concentration of protein in a solution will always lead to a higher amount of adsorbed protein – which in fact is not always the case in industrial applications.
Complex elution behavior is a challenge for the modeling of industrial applications. The predictability of high protein load densities is one key requirement for the successful implementation of model-based process development in the industry. The SMA equation for ion exchange chromatography does not consider further thermodynamic effects. To account for this, concentration-dependent activities are necessary.
Implementing an asymmetric activity coefficient to the steric mass action isotherm. The SMA isotherm was extended with an additional coefficient to generate a generalized ion exchange isotherm. The asymmetric activity coefficient was thereby approximated by means of two protein-specific parameters. These could be identified through the inverse curve fitting method of the ChromX simulation software. The data needed to calibrate the model was from just three different gradient elution experiments with varying load densities and gradient slopes.
The new isotherm opens various possibilities for future applications. Now, processes with high load densities can be modeled and simulated. Furthermore, it allows model-based process development, for instance, in the case of continuous ion exchange chromatography or the operational mode of “overloaded chromatography”.