Rolf Hjorth

Confocal microscopy as a tool for studying protein adsorption to chromatographic matrices

Confocal scanning laser microscopy was used for studying protein adsorption to affinity chromatography matrices. The adsorption of Protein A to IgG Sepharose 6 Fast Flow was studied by batch incubation with varying amounts of fluorescently labeled Protein A. At low sample amounts, Protein A had been adsorbed to a thin outer layer. By increasing the sample-IgG Sepharose ratio, the adsorption layer also increased. Likewise, the adsorption depth was dependent on the incubation time. Finally, a stack of confocal images separated in space was used for three-dimensional reconstruction of the adsorption pattern in a particle.

Direct visualisation of plasmid DNA in individual chromatography adsorbent particles by confocal scanning laser microscopy.

Confocal microscopy was used for the measurement of plasmid DNA adsorbed to individual adsorbent particles intended for anion-exchange and triple helix affinity chromatography. Plasmid DNA was visualized with the fluorescent dye YOYO-1, that forms a highly fluorescent complex with double stranded DNA. Confocal images were translated into fluorescence intensity profiles and the distribution of plasmid DNA in the particles was measured. The results that adsorption of plasmid DNA mainly takes place in an outer layer of the particles. The described procedure can also be advantageously used to demonstrate triple helix formation between plasmid DNA and immobilized oligonucleotides.

Experimental measurement of particle size distribution and voidage in an expanded bed adsorption system

This paper presents an experimental analysis of matrix bead size distribution and voidage variations with axial height in an expanded bed adsorption system. Use of a specially constructed expanded bed with side ports has enabled sampling from within the expanded bed along the vertical axis. Particles removed from within the bed were measured for their size distributions. Residence time distribution studies were used to estimate bed voidage. Measurements of axial and radial particle size distributions and axial voidage distribution have been made at different flow rates. Particle size was found to be radially constant, indicating constant stratification in the column. The particle size was found to decrease with increasing axial height. Voidage increased with axial height from a settled bed value of 0.39 to approaching unity for high liquid velocities and increased at a constant axial position with increased flowrate. This information provides key insight into bed stability and data for the improved modeling of this important unit operation.

Integration of scale-down experimentation and general rate modelling to predict manufacturing scale chromatographic separations

Chromatography is an essential downstream processing step in the production of biopharmaceuticals. Here we present an approach to chromatography scale-up using scale-down experimentation integrated with general rate modelling. This type of modelling takes account all contributions to the mass transfer kinetics providing process understanding. The model is calibrated using a 2.5 cm height, 1 ml column and used to predict chromatograms for 20 cm height columns from 40 ml to 160 L volume. Simulations were found to be in good agreement with experimental results. The envisaged approach could potentially reduce the number of experiments, shorten development time and reduce costs.