Publications

M. Peterka, P. Kramberger, A. Štrancar

WANG, Perry G. (ur.). Monolithic chromatography and its modern applications. St Albans: ILM publications, 2010, pg. 489-508

Downstream processing (DSP) for purification can become a significant bottleneck in the production of novel biotherapeutics, such as viral vectors and vaccines (viral or DNA). Although different techniques can be used for the purification of large molecules and particles, liquid chromatography is the preferred method as it achieves the purity required by regulatory agencies. Despite the popularity of conventional chromatographic media, the diffusional mass transfer of large molecules and relatively small pore size remain limiting factors for the efficient separation of large biomolecules and particles. Methacrylate monoliths are a single-piece chromatographic support that consists of a highly porous material with an interconnected network of channels. The transport mechanism is predominantly based on convection, which allows rapid mass transfer between the mobile and stationary phase and so results in short separation times. Additionally, most of the active sites are located in the open, large channel structure and are therefore easily accessible, which results in a high DBC (DBC) for large molecules and viral particles. These characteristics make methacrylate monoliths an ideal chromatographic support for the separation and purification of extremely large molecules, such as large proteins, different types of DNA and virus particles.

P. Kramberger, D. Glover, A. Štrancar

American Biotechnology Laboratory, 2003, 21(13), 27-8.

Research in molecular and cell biology has shown that macromolecules such as pDNA and virus vectors, together called nanoparticles, have the potential to assist in the prevention and treatment of some human diseases. The most important step in their production is the downstream processing (isolation and cleaning). Precipitation, ultrafiltration, and LC techniques are the most widely used for these purposes, but only LC can purify the product so that it is recognized as safe for therapeutic use. Apart from reduced yield, downstream processing can cause minor or even major modifications in the structure of the biomolecule. Usually these modifications do not affect the activity of the product, but may change its antigenicity. Minimizing these changes to maintain product safety is the main objective in the downstream processing of nanoparticles. For the efficient isolation of labile biomolecules, liquid chromatographic supports should provide fast and efficient separation in order to decrease biomolecule degradation; have high, preferably flow-unaffected capacity and resolution; and exhibit low backpressure. They should be stable, even if harsh conditions are applied during sanitation (e.g., 1 M NaOH), and should be easy to handle and operate. CIM® (Convection Interaction Media) monolithic chromatographic columns (BIA Separations, Ljubljana, Slovenia) meet all of these requirements. This article will discuss the columns and their use on human models and plant viruses and pDNA.

R. Giovannini, R. Freitag, T. B. Tennikova

Anal. Chem. 1998, 70, 3348-3354

Membrane adsorbers are well established in protein chromatography. The present paper investigated for the first time the behavior of polynucleotides on these stationary phases, taking a 7.2-kb predominantly supercoiled plasmid as example. Gradient and isocratic elution was studied. In contrast to protein high-performance membrane chromatography (HPMC), isocratic elution is possible in DNA chromatography. In the case of gradient elution, much higher salt concentrations can be used in the starting buffer. Under optimized conditions, both approaches led to a splitting of the single plasmid peak into three maximums, which corresponded to the threealbeit isolated bands in the agarose gel. Presumably the three fractions were supercoiled, nicked, and open circular plasmid DNA. Linearization of the plasmid lowered the adsorption energy, and the linearized plasmid eluted earlier than the nonlinearized one. The HPMC experiments were compared to similar ones performed using a conventional packed-bed anion-exchange column (BioScale Q2, 7 × 52 mm, 10-μm porous particles) and a novel monolithic-type anion-exchange column (UNO Q1, 7 × 35 mm). The results and characteristic differences observed in these experiments were interpreted in the light of the newly developed theory of HPMC.

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