Nicht-isokratische SMB-Trennung von Proteinen mittels Ionenaustauschchromatographie

Step gradients in 3-zone simulated moving bed chromatography. Application to the purification of antibodies and bone morphogenetic protein-2

The simulated moving bed (SMB) technology is a proven tool for efficient separation of binary mixtures. However, relying on isocratic conditions limits the applicability of the classical SMB approach when considering the field of bioseparations. Here, the use of gradients opens up new possibilities. A gradient in a SMB process can be established by using different solvent strengths in the incoming feed and desorbent streams, resulting in two internal plateaus of elution strength. Thus, compared to the conventional process, the overall amount of solvent needed can be reduced, productivity can be increased and more concentrated product streams can be obtained. In this contribution, two case studies will be presented. At first, the separation of bovine IgG from lysozyme will be analyzed as a model system. Antibodies are a common target substance in bio-chromatography, as therapeutic monoclonal antibodies are among the most promising biopharmaceuticals. Using adsorption data obtained from single-column experiments, an appropriate SMB process was designed and implemented. The second target component is the active dimeric form of the bone morphogenetic protein-2 (BMP-2). This protein was isolated from a renaturation solution, which also contained its inactive monomeric form as well as other undefined proteins from the bacterial production strain. A 3-zone open-loop gradient-SMB approach was used successfully for both separations.

A continuous, counter-current multi-column chromatographic process incorporating modifier gradients for ternary separations

The existing literature of continuous chromatographic process indicates the scarcity of processes which allow the continuous separation of a ternary mixture and which also exploit the power of modifier gradients and counter-currency. A new process filling this gap is presented and analyzed using an equilibrium theory model and linear isotherms. The analysis leads to the explicit formulation of an operating region, where 100% purity and yield can be obtained. A normalized flow rate ratio is introduced, which allows an easy description and understanding of the process behavior. The gained insights are verified using a detailed simulation model, where the influence of changes in the normalized flow rate ratios on the unit performance is investigated.