A continuous 6-column configuration has been applied to the purification of a polypeptide mixture and a semi-continuous 3-column setup to the separation of polypeptides and to a mixture of monoclonal antibody variants.
To increase the productivity and to decrease the investment- as well as maintenance costs of the multicolumn equipment, the process has been transferred from a continuous 6-column configuration to a semi-continuous 3-column setup.
Simulations and experiments of both configurations are discussed in detail and the experimental performance for a highly nonlinear adsorption isotherm is discussed with a simulation model.
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