CAPACITY, MASS TRANSFER KINETICS, FLOW-PROPERTIES and OPTIMIZATION of A NEW PROTEIN-A ADSORBENT: UNOsphere SUPrA

Wednesday, November 11, 2009: 3:40 PM
Canal B (Gaylord Opryland Hotel)

Ernie X. Perez-Almodovar, Department of Chemical Engineering, University of Virginia, Charlottesville, VA
Giorgio Carta, Department Chemical Engineering, University of Virginia, Charlottesville, VA

The paper discusses the experimental determination and modeling of IgG binding capacity and mass transfer kinetics and of the flow properties of a new Protein A adsorbent based on a macroporous resin. The new adsorbent consists of polymeric beads based on hydrophilic acrylamido and vinyl monomers with a pore structure optimized to allow favorable interactions of recombinant Protein A, coupled to the resin, with IgG. The particles are sized with an average diameter of 57 um and a narrow particle size distribution. This combination results in pressures of less than 2 bar at 600 cm in 20 cm long columns. An equilibrium adsorption capacity of 43 mg/mL particle is obtained from batch equilibrium experiments. The mass transfer kinetics for both adsorption and desorption conditions, obtained from transient batch adsorption and microscopic experiments, is consistent with a pore diffusion model with an effective pore diffusivity of 6.0x10-8 cm2/s, essentially independent of protein concentration. Flow properties are determined experimentally in laboratory, preparative, and process scale columns, 1, 20, 30, and 45 cm in diameter. A modified version of the model of Stickel and Fotopoulos [Biotechnol. Progr., 17, 744 (2001)] is developed to describe the packing and pressure drop behavior resulting in a packing compressibility parameter that is approximately independent of column diameter over the range studied. The cyclic adsorption-desorption behavior of IgG in single column systems is thus readily predicted from these measurements allowing the definition of a productivity curve for the optimization of operating conditions. A final component of this work is the extension and use of the new adsorbent in periodic countercurrent systems where multiple columns are used in a merry-go-round sequence to maximize the utilization of the available adsorption capacity. Operation with two or three columns in series is shown to provide substantial productivity improvements, without excessive equipment complexities. A numerical model used to predict the periodic countercurrent behavior is found to be in good agreement with laboratory scale experiments.
Extended Abstract: File Not Uploaded
See more of this Session: Advances in Bioseparations
See more of this Group/Topical: Separations Division