Publications
2004
E. G. Vlakh, A. Tappe, C. Kasper, T. B. Tennikova
Journal of Chromatography B, 810 (2004) 15–23
Plasminogen activators are the proteases which convert plasminogen into plasmin dissolving, in its turn, the major component of blood clots, fibrin. They are extremely useful in heart attack therapy. Modern and most appropriate way of scaled up production of these valuable proteins is gene engineering. In this case, a separation and a purification of target product become the important steps of the whole process. Recently developed affinity chromatography on short monolithic columns seems to be a very attractive method for these purposes. High speed of a process prevents the protein’s denaturation due to temperature or/and solvents influence. The better mass transfer mechanism (convection rather than diffusion) allows considering only biospecific complexing as time limiting step. Specificity of several synthetic peptides to plasminogen activators have been studied by affinity chromatography on short monolithic columns. Peptide ligands were synthesized by conventional solid phase peptide synthesis (SPPS). The immobilization procedure was carried out as a one step process at static conditions. The results of quantitative evaluation of such affinity interactions were compared with those established for plasminogen that is the natural affinity counterpart to both proteases. Additionally, some of investigated peptides were synthesized directly on GMA–EDMA disks and their affinity properties were compared with those established for the case of immobilized ligands. The possibility of using of synthetic peptidyl ligands for plasminogen activators isolation from native cell supernatant and model protein mixtures has been demonstrated.
D. G. Glover, M. Barut, A. Podgornik, M. Peterka, A. Štrancar
BioProcess International, Oct 2004, 58-63
The sequencing of the human genome and the rise of proteomics have increased the numbers of potential therapeutic targets. Biotechnology companies need to increase productivity, decrease discovery and production costs, and use technologies that easily transfer across departments if they wish to remain competitive. The most important tools are those for separation (purification) of target substance(s). They should be easy to use and offer an identical performance and purification profile no matter where they are implemented — in discovery, production, or quality assurance (QA).
CIM Convective Interaction Media short monolithic columns are just such a unifying technology. Produced in shapes and sizes from microliter to liter scale, they represent an evolutionary approach to meeting biochromatographic separation requirements in research and product development. Able to withstand 1 M NaOH with no loss of capacity or resolution, these easily scalable columns have been optimized for analysis and cGMP production of complex biomolecules ranging from oligonucleotides and plasmid DNA (pDNA) to proteins and viruses.
E. G. Vlakh, A. Tappe, C. Kasper, T. B. Tennikova
Journal of Chromatography B, 810 (2004) 15–23
Plasminogen activators are the proteases which convert plasminogen into plasmin dissolving, in its turn, the major component of blood clots, fibrin. They are extremely useful in heart attack therapy. Modern and most appropriate way of scaled up production of these valuable proteins is gene engineering. In this case, a separation and a purification of target product become the important steps of the whole process. Recently developed affinity chromatography on short monolithic columns seems to be a very attractive method for these purposes. High speed of a process prevents the protein’s denaturation due to temperature or/and solvents influence. The better mass transfer mechanism (convection rather than diffusion) allows considering only biospecific complexing as time limiting step. Specificity of several synthetic peptides to plasminogen activators have been studied by affinity chromatography on short monolithic columns. Peptide ligands were synthesized by conventional solid phase peptide synthesis (SPPS). The immobilization procedure was carried out as a one step process at static conditions. The results of quantitative evaluation of such affinity interactions were compared with those established for plasminogen that is the natural affinity counterpart to both proteases. Additionally, some of investigated peptides were synthesized directly on GMA–EDMA disks and their affinity properties were compared with those established for the case of immobilized ligands. The possibility of using of synthetic peptidyl ligands for plasminogen activators isolation from native cell supernatant and model protein mixtures has been demonstrated.
M. Bartolini, V. Cavrini, V. Andrisano
Journal of Chromatography A, 1031 (2004) 27–34(2004) 27–34
The development and characterization of a human recombinant acetylcholinesterase (hrAChE) micro-immobilized-enzyme reactor (IMER), prepared by using an in situ immobilization procedure is reported. hrAChE was covalently immobilized on an ethylenediamine (EDA) monolithic convective interaction media (CIM) disk (12mm x 3mm i.d.), previously derivatized with glutaraldehyde. The optimal conditions for the immobilization were: 12 μg of enzyme dissolved in 800 μl of phosphate buffer (50 mM, pH 6.0). The mixture was gently agitated overnight at 4 °C. The resulting Schiff bases were reduced by cyanoborohydride and the remaining aldehydic groups were condensed with monoethanolamine. Under these conditions, 0.22 U of hrAChE were immobilized with retention of 3.0% of the initial enzymatic activity. The activity of the immobilized hrAChE was stable for over 60 days. The activity and kinetic parameters of the hrAChE micro-IMER were investigated by inserting the micro-IMER in a HPLC system and it was demonstrated that the enzyme retained its activity. The micro-IMER was characterized in terms of units of immobilized enzyme and best conditions for immobilization yield. IMERs were compared for their relative enzyme stability, immobilized units, yield and aspecific matrix interactions. The effect of AChE inhibitors was evaluated by the simultaneous injection of each inhibitor with the substrate. The relative IC50 values were found in agreement with those derived by the conventional kinetic spectrophotometric method. In comparison with previously developed AChE-based IMERs, AChE monolithic micro-IMER showed advantages in terms of reduction of analysis time (2 min), lower aspecific matrix interactions and lower backpressure. Included in a HPLC system, it can be used for the rapid screening of new compounds’ inhibitory potency. The advantages over the conventional methods are the increased enzyme stability and system automation which allows a large number of compounds to be analyzed in continuous.
K. Benčina, A. Podgornik, A. Štrancar, M. Benčina
Journal of Separation Science 2004, 27, 811-818
Monolithic Convective Interaction Media (CIM) have been activated with epoxide and imidazole carbamate functionalities and used as supports for covalent immobilization of protein A, deoxyribonuclease I, and trypsin. The efficiency of immobilization for these proteins was determined from the amount of bound IgG, degradation of DNA, and hydrolysis of Nα-benzoyl-L-arginine ethyl ester, respectively. The respective biological activities of trypsin and the binding capacity of protein A immobilized via imidazole carbamate groups were 11.45 and 2.25 times higher than those obtained for epoxide matrix while they were practically equal for deoxyribonuclease I. The kinetics of immobilization was studied in detail for trypsin under dynamic conditions and revealed that the enzyme immobilized via imidazole carbamate groups already reached its highest activity in 5 min. In contrast, a much longer time was required for immobilization via epoxy groups.
2003
I. Mihelič, T. Koloini, A. Podgornik
Journal of Applied Polymer Science, Vol. 87, 2326-2334 (2003)
Monolithic stationary phases are becoming increasingly important in the field of liquid chromatography. Methacrylate-based monoliths are produced via free-radical bulk polymerization. The preparation of large-volume monoliths is a major problem because the intensive heat released during polymerization causes distortion of the porous monolithic structure. This work presents experimental measurements of temperature distributions during polymerization in moulds of different sizes and at various experimental conditions. A mathematical model for the prediction of temporal and spatial temperature distribution during the polymerization of methacrylate-based monolithic columns is introduced. The polymerization is described by an unsteady-state heat conduction equation with the generation of heat related to the general kinetics of polymerization. Predictions from the mathematical model are in good agreement with the experimental measurements at different experimental conditions. A method for construction of large-volume monolithic columns is presented and an attempt is made to adopt the developed mathematical model in annular geometry.
P. Milavec Žmak, H. Podgornik, J. Jančar, A. Podgornik, A. Štrancar
Journal of Chromatography A, 1006 (2003) 195–205
Convective Interaction Media (CIM) columns are monolithic columns optimized for the separation of macromolecules. Some of them operate in the axial mode while others operate in the radial mode depending on the column size. In this work we tested the approach suggested by Yamamoto [Biotechnol. Bioeng., 48 (1995) 444] for transfer of gradient methods between columns of different size. A simplified equation for transfer was derived together with a criterion for its application. Separation was evaluated for a standard protein mixture and peroxidase enzymes present in fermentation broth. Salt and pH gradients were applied. Similar resolutions were obtained for each sample on all columns which demonstrates that the proposed approach can be successfully used for method scale-up on this type of column.
M. Merhar, A. Podgornik, M. Barut, M. Žigon, A. Štrancar
J. Sep. Sci. 2003, 26, 322–330
Methacrylate-based monoliths are formed during radical copolymerization as a consequence of the precipitation of polymeric chains from the reaction mixture, which consists of monomers, initiator, and the porogenic solvents. The effect of various methacrylate monomers on the porous structure of the monolith was investigated. Although the chemical structure of the monomers significantly affects the size of the pores and the porosity, the mechanism of pore formation in the case of the precipitation during polymerization is preserved. The porous structure was further correlated with the specific surface area, pressure drop, and dynamic binding capacity of the monoliths studied.
A. Podgornik, M. Barut, A. Štrancar
Encyclopedia of Chromatography DOI: 10.1081/E-ECHR 120016288, 2003
Chromatographic columns are typically several centimeters in length, resulting in a high number of column plates, and, consequently, such columns have high efficiency. These properties allow even very similar molecules to be separated. This is especially true for smaller molecules, where the separation is based on selective migration. For large molecules, a different separation mechanism is usually required. Large molecules normally interact with the matrix at several binding sites. Consequently, their adsorption isotherms are very steep, almost rectangular. For such molecules, there exists only a very narrow mobile phase range within which they interact with the active moieties on the stationary phase, but are not irreversibly retained. To elute them from the matrix, a change of the mobile phase composition is required. Therefore the separation is based upon the selective elution and requires the use of gradient chromatographic methods. For this type of separation, the column length is less important and the efficient separations can be achieved even with extremely short columns.
P. Kramberger, D. Glover, A. Štrancar
American Biotechnology Laboratory, 2003, 27-28
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 MNaOH), 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 application note will discuss the columns and their use on human models and plant viruses and pDNA.
I. Mihelič, A. Podgornik, T. Koloini
Journal of Chromatography A, 987 (2003) 159–168
This work investigates the influence of temperature on the binding capacity of bovine serum albumin (BSA), soybean trypsin inhibitor and l-glutamic acid to a CIM® (DEAE) weak anion-exchange disk monolithic column. The binding capacity was determined experimentally under dynamic conditions using frontal analysis. The effect on the dynamic binding capacity of dimers present in the BSA solution has been evaluated and a closed-loop frontal analysis was used to determine the equilibrium binding capacities. The binding capacity for both BSA and soybean trypsin inhibitor increased with increasing temperature. In the case of l-glutamic acid, an increase in the binding capacity was observed with temperature up to 20 °C. A further increase in temperature caused a decrease of the dynamic binding capacity.
M. Vodopivec, A. Podgornik, M. Berovič, A. Štrancar
Journal of Chromatography B, 795 (2003) 105-113
The immobilization of the enzymes citrate lyase, malate dehydrogenase, isocitrate dehydrogenase and lactate dehydrogenase to CIM monolithic supports was performed. The long-term stability, reproducibility, and linear response range of the immobilized enzyme reactors were investigated along with the determination of the kinetic behavior of the enzymes immobilized on the CIM monoliths. The Michaelis–Menten constant Km and the turnover number k3 of the immobilized enzymes were found to be flow-unaffected. Furthermore, the Km values of the soluble and immobilized enzyme were found to be comparable. Both facts indicate the absence of a diffusional limitation in immobilized CIM enzyme reactors.
2002
A. Podgornik, M. Barut, S. Jakša, J. Jančar, A. Štrancar
Journal of Liquid Chromatography & Related Technologies Vol. 25, No. 20, pp. 3097–3114, 2002
Convective Interaction Media® (CIM) disk monolithic columns are specific among the chromatographic columns because of their monolithic structure and extremely short column length. In this work, HETP values and Z factors for different groups of molecules—proteins, DNA, oligonucleotides, peptides, and organic acids on strong anion exchange CIM disk monolithic columns were determined. Results are discussed in terms of the molecule structures and applied to develop different approaches for successful separation of abovementioned group of molecules on these types of columns.
R. Hahn, M. Panzer, E. Hansen, J. Mollerup, A. Jungbauer
Separation Science and Technology, 37(7), 1545–1565 (2002)
The mass transfer properties of polyglycidylmethacrylate–ethylenedimethacrylate monolithic ion-exchangers (convective interaction media disks) were evaluated. As a reference material, the particulate ion-exchanger Source 30 was selected. The model proteins lysozyme, bovine serum albumin, and IgG were loaded at different concentrations and velocities. The mass transfer zones obtained with the monoliths were affected by neither the linear flow velocity nor the protein concentration in the mobile phase. The reduced height equivalent to one theoretical plate (HETP) of monoliths were independent of the reduced velocity. This was not the case for the particulate material.
A. Štrancar, A. Podgornik, M. Barut, D. Glover
BIOforum International 3/2002
In adsorptive chromatographic modes, the slope of the capacity factor k' (defined as the molar ratio of the separated compound in the stationary phase and the mobile phase) plot versus composition of the mobile phase is very steep. Up to a certain composition of the mobile phase, k' is so high that the protein is bound to the stationary phase and does not move along the column. Reaching a defined point, a small change of the mobile phase composition causes a rapid decrease in k' to a value near zero. At this point, the protein dissolves in the mobile phase and passes through the column practically without any retention. In other words, the protein remains adsorbed at the top of the column until the eluting power of the mobile phase reaches the point at which a small change in the composition of the mobile phase causes the movement of the protein without any retention. One can also speak about selective elution of the compound. As a result of this process, even very short columns can provide very good separations and recovery, while longer columns might cause problems due to unspecific binding, product degradation and minor changes in the structure of the protein which increase with the length of the column. On the other hand, short-beds are very difficult to pack with particles and form channels which eliminate the resolution power of the column. Monolithic supports offer an ideal solution to avoid most of these problems.
K. Pflegerl, A. Podgornik, E. Berger, A. Jungbauer
J. Comb. Chem. 2002, 4, 33-37
Solid-phase peptide synthesis was performed on glycidyle methacrylate-co-ethylene dimethacrylate monoliths using Fmoc chemistry. The native epoxy groups were amino-functionalized by reaction with ethylenediamine or ammonia ions. A peptide directed against human blood coagulation factor VIII was synthesized as a model peptide. Amino acid analysis revealed the correct amino acid ratio as present in the sequence. The ligand density of 5 μmol/mL was equal to that achieved with conventional peptide immobilization via epoxy groups. These supports were directly used as peptide affinity chromatography matrixes. The functionality of the CIM monolithic supports was proven by affinity chromatography of factor VIII. The ammonia-functionalized support performed with low hydrophobicity and did not show unspecific adsorption of proteins.
K. Pflegerl, A. Podgornik, E. Berger, A. Jungbauer
Biotechnology and Bioengineering 79 (2002) 733-740
Screening of peptide ligands for affinity chromatography usually involves incubation with the target protein in a batch system. In an additional step, peptides with fast binding kinetics have to be selected in respect to satisfactory performance under flow conditions on a support ensuring optimal three-dimensional presentation of the peptide. We have developed a rapid screening system based on peptide synthesis and screening on CIM® disks. The disk size was minimized to fit into microplates usually applied for solid-phase extraction. In combination with a vacuum manifold, semi-automated peptide synthesis and screening for binding to a target protein under simulated chromatography conditions are possible. Various analytical methods can be applied for parallel and automated determination of the quantity, integrity, or activity of the target protein in the flow through or bound to the affinity support. This system also allows parallel screening for suitable chromatographic conditions like running buffer, washing, and elution conditions. © 2002 Wiley Periodicals, Inc. Biotechnol Bioeng 79: 733–740, 2002.
T. Tennikova, A. Štrancar
LabPlus international February - March 2002, Volume 16
Monolithic supports are a novel generation of stationary phases that can be used for liquid and gas chromatography, capillary electrochromatography, bioconversions, as well as supports for solid phase synthesis. In contrast to individual particles packed into chromatographic columns, monolithic supports are cast as continuous homogeneous phases. They provide high rates of mass transfer at lower pressure drops and enable much faster separations. In addition to the speed, the nature of the pores allows easy permeability for large molecules. Monolithic supports are thus the method of choice for the separation of proteins, oligonucleotides, and nanoparticles such as pDNA and viruses. In this article we review the application of the monlithic columns to bioaffinity chromatography.
H. Podgornik, A. Podgornik
Enzyme and Microbial Technology 31 (2002) 855–861
The possibility of covalent attachment of LiP H2 and LiP H8 to CIM monoliths was studied. Due to negligible diffusional resistance, they can be useful tools to study characteristics of the immobilized lignin peroxidase (LiP). Immobilization to epoxy groups was performed using alkaline conditions (borate-phosphate buffer; pH 7.5). Characteristics of immobilized LiP were compared and factors that influence their biologic activity were evaluated using flow through experiments. Enzyme kinetics was determined via oxidation of veratryl alcohol (VA) into veratraldehyde (Vald). While VA oxidation rate increased by increasing flow rate (up to 1.5 ml/min) for LiP H2, it was almost constant in a wide flow rate range for LiP H8. This observation together with the stepwise deactivation of the enzyme by consecutive experiments was ascribed to accumulation of the formed Vald inside the support. Calculated kinetic parameters showed 3–5 times higher Km value for VA for both tested isoforms in comparison to free enzyme. The catalytic constant was found to be approximately 0.5 s-1 for both isoforms. Immobilized LiP H8 was used for decolorization of azo dye Mahogany.
K. Pflegerl, A. Podgornik, E. Berger, A. Jungbauer
Biotechnology and Bioengineering 79 (2002) 733-740
Screening of peptide ligands for affinity chromatography usually involves incubation with the target protein in a batch system. In an additional step, peptides with fast binding kinetics have to be selected in respect to satisfactory performance under flow conditions on a support ensuring optimal three-dimensional presentation of the peptide. We have developed a rapid screening system based on peptide synthesis and screening on CIM® disks. The disk size was minimized to fit into microplates usually applied for solid-phase extraction. In combination with a vacuum manifold, semi-automated peptide synthesis and screening for binding to a target protein under simulated chromatography conditions are possible. Various analytical methods can be applied for parallel and automated determination of the quantity, integrity, or activity of the target protein in the flow through or bound to the affinity support. This system also allows parallel screening for suitable chromatographic conditions like running buffer, washing, and elution conditions.