The cation-exchange capture step of a monoclonal antibody (mAb) purification process using single column batch and multicolumn continuous chromatography (MCSGP) was modeled with a lumped kinetic model. Model parameters were experimentally determined under analytical and preparative conditions: porosities, retention factors and mass transfer parameters of purified mAb were obtained through a systematic procedure based on retention time measurements. The saturation capacity was determined through peak fitting assuming a Langmuir-type adsorption isotherm. The model was validated using linear batch gradient elutions. In addition, the model was used to simulate the start-up, cyclic steady state and shut down behavior of the continuous capture process (MCSGP) and to predict performance parameters. The obtained results were validated by comparison with suitable experiments using an industrial cell culture supernatant. Although the model was not capable of delivering quantitative information of the product purity, it proved high accuracy in the prediction of product concentrations and yield with an error of less than 6%, making it a very useful tool in process development.

A two-step chromatography process for monoclonal antibody (mAb) purification from clarified cell culture supernatant (cCCS) was developed using cation exchange Multicolumn Countercurrent Solvent Gradient Purification (MCSGP) as a capture step. After an initial characterization of the cell culture supernatant the capture step was designed from a batch gradient elution chromatogram. A variety of chromatographic materials was screened for polishing of the MCSGP-captured material in batch mode. Using multi-modal anion exchange in bind-elute mode, mAb was produced consistently within the purity specification. The benchmark was a state-of-the-art 3-step chromatographic process based on protein A, anion and cation exchange stationary phases. The performance of the developed 2-step process was compared to this process in terms of purity, yield, productivity and buffer consumption. Finally, the potential of the MCSGP process was investigated by comparing its performance to that of a classical batch process that used the same stationary phase.