Publications
2007
I. V. Kalashnikova, N. D. Ivanova, T. G. Evseeva, A. Yu. Menshikova, E. G. Vlakh, T. B. Tennikova
Journal of Chromatography A, 1144 (2007) 40–47(2007) 40–47
The subject of this paper is an investigation of the peculiarities of dynamic adsorption behavior of nanoparticles. For this purpose, virus-mimicking synthetic particles bearing different proteins at their outer surface were specially constructed using two approaches, e.g. the cross-linking of proteins and modification of polystyrene microsphere surface by proteins. Two chromatographic modes, namely ion-exchange and affinity liquid chromatography on ultra-short monolithic columns [Convective Interaction Media (CIM) DEAE and CIM QA disks] have been used as a tool for dynamic adsorption experiments. Such parameters as maximum adsorption capacity and its dependence on applied flow rate were established and compared with those obtained for individual proteins. Similarly to individual proteins, it was shown that the maximum of adsorption capacity was not changed at different flow rates. In addition, the permeability of porous space of used monolithic sorbents appeared to be sufficient for efficient separation of large particles and quite similar to the well-studied process applied for individual proteins.
I.Vovk, B. Simonovska
Journal of Chromatography B, 849 (2007) 337-343
The most abundant isoforms of tomato pectin methylesterase (PME; EC 3.1.1.11; Mr 26 kDa), polygalacturonase (PG; EC 3.2.1.15; PG1 with Mr 82 kDa) and a basic protein with Mr 42 kDa and unknown function were isolated from fresh tomato fruit by a fast chromatographic procedure on a Convective Interaction Media (CIM®) short monolithic disk column bearing carboxymethyl (CM) groups. The extraction of the targeted enzymes with 1.2 M NaCl solution was followed by precipitation with ammonium sulfate at 60% of saturation, solubilisation of the pellet in 0.5 M NaCl and fractionation using a linear gradient from 0 to 700 mM NaCl. Among six fractions five had PME activity and four had PG activity, while one fraction containing a pure protein with Mr 42 kDa with neither of these activities. Two concentrated fractions, one with PG and one with PME were further purified. A linear gradient from 0 to 500 mM NaCl with 20% CH3CN in the mobile phase was used for the PG fraction and two CM disks and a linear gradient from 0 to 200 mM NaCl were used for the PME fraction as a greater capacity was necessary in this case. From 4 kg of fresh tomato flesh we obtained 22 mg of purified PME, 1.8 mg of purified, active PG1, 13.5 mg of additional basic protein and a fraction with PG2 contaminated by a PME isoform. Carboxymethyl CIM disk short monolithic columns are convenient for semi-preparative and analytical work with tomato fruit pectolytic enzymes.
N. Delmotte, U. Kobold, T. Meier, A. Gallusser, A. Strancar, C. G. Huber
Anal Bioanal Chem (2007) 389:1065–1074
Immunoadsorbers based on 2.0 × 6.0 mm i.d., epoxy-bearing, methacrylate-based monolithic disks were developed in order to target myoglobin and N-terminal pro-natriuretic peptide (NT-proBNP), two biomarkers involved in cardiovascular disease. In both cases, antibodies were successfully coupled to the polymeric disk material. The developed immunoadsorbers permitted the selective isolation of myoglobin and NT-proBNP from human serum. Myoglobin was successfully isolated and detected from serum samples at concentrations down to 250 fmol μL-1. However, the affinity of the antibodies was not sufficient for the analysis of low-concentration clinical samples. Frontal analysis of anti-NT-proBNP disks revealed the ability of the immunoadsorber to bind up to 250 pmol NT-proBNP, which is more than sufficient for the analysis of clinical samples. Anti-NT-proBNP disks showed good stability over more than 18 months and excellent batch-to-batch reproducibility. Moreover, anti-NT-proBNP disks permitted the isolation of NT-proBNP at concentrations down to 750 amol μL−1 in serum, corresponding to concentrations of strongly diseased patients. Using reversed-phase trapping columns, the detection of NT-proBNP eluted from immunoadsorbers by mass spectrometry was achieved for concentrations down to 7.8 fmol μL-1.
I. Vovk, B. Simonovska
Journal of Chromatography A, 1144 (2007) 90-96(2007) 90-96
An improved cation-exchange chromatographic procedure on Convective Interaction Media (CIM, Sartorius BIA Separations, Ljubljana, Slovenia) short monolithic methacrylate disk columns was used for the isolation of salt-independent pectin methylesterase (PME; EC 3.1.1.11) isoform and endo-polygalacturonase PG1 (PG, EC 3.2.1.15) from ripe tomato fruit extract after studying the chromatographic conditions including type of disk, binding buffer, pH, eluent composition and different gradients. Between 10 and 20 μg of proteins gave reliable chromatograms. Both carboxymethyl (CM) and sulfonyl (SO3) disks were equally suitable for the fractionation of tomato extract using the new gradient, but only CM disk was appropriate for further purification of the PME and PG fractions, and provided fast and sharp separation of proteins. The isolation of pure PG1 could be achieved only by addition of 20% of acetonitrile to the mobile phase. About 200 μg of proteins were loaded at one chromatographic run at the fractionation and purification. Determination of the molecular weights of the separated proteins showed that dimer of salt-independent PME isoform was formed in concentrated solutions of the enzyme but dissociated upon dilution of the solution. From 6 kg of fresh tomato flesh, 28 mg of purified salt-independent PME, 12.5 mg of purified and active PG1 and 4 mg of PG2 fraction contaminated with salt-dependent PME isoform were obtained by means of semi-preparative chromatography on CIM disks.
D. Josić, J. G. Clifton
Journal of Chromatography A, 1144 (2007) 2-13
An overview on the utilization of monoliths in proteomics technology will be given. Both silica- and polymer-based monoliths have broad use for microseparation of tryptic peptides in reversed-phase (RP) mode before identification by mass spectrometry (MS) or by MS/MS. For two-dimensional (2D) LC separation of peptides before MS or MS/MS analysis, a combination of ion-exchange, usually cation-exchange (CEX) chromatography with RP chromatography on monolithic supports can be employed. Immobilized metal ion affinity chromatography monoliths with immobilized Fe3+-ions are used for the isolation of phosphopeptides. Monoliths with immobilized affinity ligands are usually applied to the rapid separation of proteins and peptides. Miniaturized reactors with immobilized proteolytic enzymes are utilized for rapid on- or offline digestion of isolated proteins or protein mixtures prior to identification by LC–MS/MS. Monoliths also have broad potential for application in sample preparation, prior to further proteomic analyses. Monolithic supports with large pore sizes can be exploited for the isolation of nanoparticles, such as cells, organelles, viruses and protein aggregates. The potential for further adoption of monolithic supports in protein separation and enrichment of low abundance proteins prior to proteolytic digestion and final LC–MS/MS protein identification will be discussed.
E. Machtejevas, S. Andrecht, D. Lubda, K. K. Unger
Journal of Chromatography A, 1144 (2007) 97-101
The following particulate and monolithic silica columns were implemented in a fully automated and flexible multidimensional LC/MS system with integrated sample clean-up, to perform the analysis of endogeneous peptides from filtered urine and plasma samples: restricted access sulphonic acid strong cation-exchanger (RAM-SCX) for sample clean-up, RP 18 Chromolith guard columns as trap columns and 100 μm I.D. monolithic RP 18 fused silica capillary columns as last LC dimension. The results show sufficient overall system reproducibility and repeatability. Implementation of monolithic silica columns added an additional flexibility with respect to flow rate variation and adjustment due to the low column back pressures. Also, monolithic columns showed a lower clogging rate in long-term usage for biological samples as compared to particulate columns. The applied system set-up was tested to be useful for the routine peptide screening in search of disease biomarkers.
P. Brne, A. Podgornik, K. Benčina, B. Gabor, A. Štrancar, M. Peterka
Journal of Chromatography A , 1144 (2007) 120-125
Certain diagnostic, analytical and preparative applications require the separation of immunoglobulin G (IgG) from immunoglobulin M (IgM). In the present work, different ion-exchange methacrylate monoliths were tested for the separation of IgG and IgM. The strong anion-exchange column had the highest dynamic binding capacity reaching more than 20 mg of IgM/ml of support. Additionally, separation of IgM from human serum albumin, a common contaminant in immunoglobulin purification, was achieved on the weak ethylenediamino anion-exchange column, which set the basis for the IgM purification method developed on convective interaction media (CIM) supports. Experiments also confirmed flow independent characteristics of the short monolithic columns.
C. K. Zacharis, E. A. Kalaitzantonakis, A. Podgornik, G. Theodoridis
Journal of Chromatography A, 1144 (2007) 126–134
In this study, sequential injection affinity chromatography was used for drug–protein interactions studies. The analytical system used consisted of a sequential injection analysis (SIA) manifold directly connected with convective interaction media (CIM) monolithic epoxy disks modified by ligand-immobilization of protein. A non-steroidal, anti-inflammatory drug, naproxen (NAP) and bovine serum albumin (BSA) were selected as model drug and protein, respectively. The SIA system was used for sampling, introduction and propulsion of drug towards to the monolithic column. Association equilibrium constants, binding capacity at various temperatures and thermodynamic parameters (free energy ΔG, enthalpy ΔH) of the binding reaction of naproxen are calculated by using frontal analysis mathematics. The variation of incubation time and its effect in on-line binding mode was also studied. The results indicated that naproxen had an association equilibrium constant of 2.90 × 106 M-1 at pH 7.4 and 39 °C for a single binding site. The associated change in enthalpy (ΔH) was −27.36 kcal mol-1 and the change in entropy (ΔS) was −73 cal mol-1 K-1 for a single type of binding sites. The location of the binding region was examined by competitive binding experiments using a biphosphonate drug, alendronate (ALD), as a competitor agent. It was found that the two drugs occupy the same class of binding sites on BSA. All measurements were performed with fluorescence (λext = 230 nm, λem = 350 nm) and spectrophotometric detection (λ = 280 nm).
T. Čerk Petrič, P. Brne, B. Gabor, L. Govednik, M. Barut, A. Štrancar, L. Zupančič Kralj
Journal of Pharmaceutical and Biomedical Analysis 43 (2007) 243–249
In order to enable the detection of low abundance proteins from human plasma, it is necessary to remove high abundance proteins. Among them, human serum albumin and immunoglobulin G represent more than 75% of all such proteins. In this paper, the characterization of short monolithic columns was performed followed by the optimization of a multidimensional approach, known as conjoint liquid chromatography, to deplete human serum albumin and immunoglobulin G from a human plasma sample. Two different chromatographic modes were used: ion-exchange chromatography and affinity chromatography. A monolithic stationary phase (convective interaction media disk) bearing strong anion-exchange groups and another immobilized with protein G were placed in series into one housing. The optimal binding conditions were found that removed a majority of human serum albumin and immunoglobulin G from the human plasma sample. This method was compared to the depletion using a combination of pseudo-affinity and affinity columns. The results of the human serum albumin and immunoglobulin G depletion were confirmed by 2D electrophoresis. It has been shown that anion-exchange and affinity chromatography using convective interaction media monolithic columns can represent an efficient complementary technique for human serum albumin and immunoglobulin G removal from human plasma.
R. Nicoli, N. Gaud, C. Stella, S. Rudaz, J.-L. Veuthey
Journal of Pharmaceutical and Biomedical Analysis 48 (2008) 398–407
The preparation and characterization of three trypsin-based monolithic immobilized enzyme reactors (IMERs) developed to perform rapid on-line protein digestion and peptide mass fingerprinting (PMF) are described. Trypsin (EC 3.4.21.4) was covalently immobilized on epoxy, carboxy imidazole (CDI) and ethylenediamine (EDA) Convective Interaction Media® (CIM) monolithic disks. The amount of immobilized enzyme, determined by spectrophotometric measurements at 280 nm, was comprised between 0.9 and 1.5 mg per disk. Apparent kinetic parameters K*m and V*max, as well as apparent immobilized trypsin BAEE-units, were estimated in flow-through conditions using N-α-benzoyl-l-arginine ethyl ester (BAEE) as a low molecular mass substrate. The on-line digestion of five proteins (cytochrome c, myoglobin, α1-acid glycoprotein, ovalbumin and albumin) was evaluated by inserting the IMERs into a liquid chromatography system coupled to an electrospray ionization ion-trap mass spectrometer (LC-ESI–MS/MS) through a switching valve. Results were compared to the in-solution digestion in terms of obtained scores, number of matched queries and sequence coverages. The most efficient IMER was obtained by immobilizing trypsin on a CIM® EDA disk previously derivatized with glutaraldehyde, as a spacer moiety. The proteins were recognized by the database with satisfactory sequence coverage using a digestion time of only 5 min. The repeatability of the digestion (R.S.D. of 5.4% on consecutive injections of myoglobin 12 μM) and the long-term stability of this IMER were satisfactory since no loss of activity was observed after 250 injections.
M. Bartolini, V. Cavrini, V. Andrisano
Journal of Chromatography A, 1144 (2007) 102–110
The aim of the present study was the application of a human AChE-CIM-IMER (enzyme reactor containing acetylcholinesterase immobilized on a monolithic disk) for the rapid evaluation of the thermodynamic and kinetic constants, and the mechanism of action of new selected inhibitors. For this application, human recombinant AChE was covalently immobilized onto an ethylenediamine (EDA) monolithic Convective Interaction Media (CIM) disk and on-line studies were performed by inserting this IMER into a HPLC system. Short analysis time, absence of backpressure, low nonspecific matrix interactions and immediate recovery of enzyme activity were the best characteristics of this AChE-CIM-IMER. Mechanisms of action of selected reversible inhibitors (tacrine, donepezil, edrophonium, ambenonium) were evaluated by means of Lineweaver–Burk plot analysis. Analyses were performed on-line by injecting increasing concentrations of the tested inhibitor and substrate and by monitoring the product peak area. AChE-CIM-IMER kinetic parameters (Kmapp and vmaxapp ) were derived as well as inhibitory constants (Kiapp of selected compounds. Moreover, noteworthy results were obtained in the application of the AChE-CIM-IMER to the characterization of the carbamoylation and decarbamoylation steps in pseudo-irreversible binding of carbamate derivatives (physostigmine and rivastigmine). AChE-CIM-IMER appeared to be a valid tool to determine simultaneously the kinetic constants in a reliable and fast mode. The obtained values were found in agreement with those obtained with the classical methods with the free enzyme. Furthermore, after inactivation by carbamates, activity could be fully recovered and the AChE-CIM-IMER could be reused for further studies. Results showed that the AChE-CIM-IMER is a valid tool not only for automated fast screening in the first phase of the drug discovery process but also for the finest characterization of the mode of action of new hit compounds with increased accuracy and reproducibility and with saving of time and materials.
2005
M. Barut, A. Podgornik, P. Brne, A. Štrancar
J. Sep. Sci. 2005, 28, 1876-1892
New therapeutics that are being developed rely more and more on large and complex biomacromolecules like proteins, DNA, and viral particles. Manufacturing processes are being redesigned and optimized both upstream and downstream to cope with the ever-increasing demand for the above target molecules. In downstream processing, LC still represents the most powerful technique for achieving high yield and high purities of these molecules. In most cases, however, the separation technology relies on conventional particle-based technology, which has been optimized for the purification of smaller molecules. New technologies are, therefore, needed in order to push the downstream processing ahead and into the direction that will provide robust, productive, and easy to implement methods for the production of novel therapeutics. New technologies include the renaissance of membranes, various improvements of existing technologies, but also the introduction of a novel concept – the continuous bed or monolithic stationary phases. Among different introduced products, Convective Interaction Media short monolithic columns (SMC) that are based on methacrylate monoliths exhibit some interesting features that make them attractive for these tasks. SMC can be initially used for fast method development on the laboratory scale and subsequently efficiently transferred to preparative and even more importantly to industrial scale. A brief historical overview of methacrylate monoliths is presented, followed by a short presentation of theoretical considerations that had led to the development of SMC. The design of these columns, as well as their scale-up to large units, together with the methods for transferring gradient separations from one scale to another are addressed. Noninvasive methods that have been developed for the physical characterization of various batches of SMC, which fulfill the regulatory requirements for cGMP production, are discussed. The applications of SMC for the separation and purification of large biomolecules, which demonstrate the full potential of this novel technology for an efficient downstream processing of biomolecules, are also presented.
A. Podgornik, A. Štrancar
Biotechnology Annual Review, 11 (2005) 281-333
Modern downstream processing requires fast and highly effective methods to obtain large quantities of highly pure substances. Commonly applied method for this purpose is chromatography. However, its main drawback is its throughput since purification, especially of large molecules, requires long process time. To overcome this problem several new stationary phases were introduced, among which short layer monoliths show superior properties for many applications. The purpose of this review is to give an overview about short methacrylate monolithic columns commercialised under the trademark Convective Interaction Media® (CIM). Their unique properties are described from different perspectives, explaining reasons for their application on various areas. Approaches to prepare large volume methacrylate monolithic column are discussed and optimal solutions are given. Different examples of CIM monolithic column implementation are summarised in the last part of the article to give the reader an idea about their advantages.
A. Jungbauer
Journal of Chromatography A, 1065 (2005) 3–12
Bioseparation processes are dominated by chromatographic steps. Even primary recovery is sometimes accomplished by chromatographic separation, using a fluidized bed instead of a fixed bed. In this review, the action principles, features of chromatography media regarding physical and chemical properties will be described. An attempt will be made to establish categories of different media. Characteristics for bioseparation are the large pores and particle sizes. To achieve sufficient capacity for ultralarge molecules, such as plasmids or nanoparticles, such as viruses monoliths are the media of choice. In these media, the mass transport is accomplished by convection, and thus, the low diffusivity can be overcome. Common to all modern chromatography media is the fast operation. There are examples where a residence time of less then 3 min, is sufficient to reach the full potential of the adsorbent.
P. Krajnc, N. Leber, D. Štefanec, S. Kontrec, A. Podgornik
Journal of Chromatography A, 1065 (2005) 69-73(2005) 69 - 73
Poly(glycidyl methacrylate-co-ethyleneglycol dimethacrylate) monolithic supports were prepared by radical polymerisation of the continuous phase of water in oil high internal phase emulsions. Morphology of monolithic materials was studied by scanning electron microscopy and mercury intrusion porosimetry. The ratio of phase volume and the degree of crosslinking influenced the void size and pore size distribution of resulting polymers. Void sizes between 1 and 10 μm were observed and average pore sizes around 100 nm. Polymers with 60, 75, 80 and 90% pore volume were prepared and even samples with highest pore volume showed good mechanical stability. They were modified to bear weak-anion exchange groups and tested on the separation of standard protein mixture containing myoglobin, conalbumine and trypsin inhibitor. Good separation was obtained in a very short time similar to the separation obtained by commercial methacrylate monoliths. However, higher dispersion was observed. Bovine serum albumin dynamic binding capacity for monolith with 90% porosity was close to 9 mg/ml.
N. Lendero, J. Vidič, P. Brne, A. Podgornik, A. Štrancar
Journal of Chromatography A, 1065 (2005) 29-38(2005) 29 - 38
The objective of this study was to develop a fast, simple, non-destructive, non-toxic and low-priced method for determining the amount of ionic groups on resins, since the conventional titration method fails to give proper results on methacrylate monoliths. After the column had been pre-saturated with a high concentration buffer solution, a low concentration buffer solution of the same pH value was pumped through the column. Measuring pH and absorbance, the profiles with a shape of typical break-through curve were obtained. It was shown that the time of the pH transient, which appeared under such conditions, could be used as a measure of the total ionic capacity of ion-exchange monolithic columns. The effect of the column length, linear velocity and varying concentrations of buffer solutions on the time of the pH transient was examined. The method was shown to be suitable for determining the amount of ionic groups on both anion and cation monolithic columns. In addition, it could also be applied to particle bed columns. The time of the pH transient and the protein dynamic binding capacity were also compared and it was concluded that for a given monolith the protein capacity can be derived from the data obtained by the new method.
I. Mihelič, D. Nemec, A. Podgornik, T. Koloini
Journal of Chromatography A, 1065 (2005) 59-67(2005) 59 - 67
Pressure drop analysis in commercial CIM disk monolithic columns is presented. Experimental measurements of pressure drop are compared to hydrodynamic models usually employed for prediction of pressure drop in packed beds, e.g. free surface model and capillary model applying hydraulic radius concept. However, the comparison between pressure drop in monolith and adequate packed bed give unexpected results. Pressure drop in a CIM disk monolithic column is approximately 50% lower than in an adequate packed bed of spheres having the same hydraulic radius as CIM disk monolith; meaning they both have the same porosity and the same specific surface area. This phenomenon seems to be a consequence of the monolithic porous structure which is quite different in terms of the pore size distribution and parallel pore nonuniformity compared to the one in conventional packed beds. The number of self-similar levels for the CIM monoliths was estimated to be between 1.03 and 2.75.
T. B. Tennikova, J. Reusch
Journal of Chromatography A, 1065 (2005) 13-17(2005) 13 - 17
The history of the development of short monolithic beds is described.
J. Vidić, A. Podgornik, A. Štrancar
Journal of Chromatography A, 1065 (2005) 51-58(2005) 51-58
The influence of glass surface modification in order to determine strength of the monolith attachment was studied. Modification consists of pre-treatment of the glass with chemicals or boiling in deionized water, silanization and drying has been investigated on different types of glass. Amount of silane groups was determined by measurement of the contact angle between the glass surface and water drop. The highest values were found for soda–lime glass. Strength of the monolith attachment was established by pumping ethanol through the monolithic capillaries and measuring the pressure drop at which monolith was dislodged. Surprisingly, it was found that the critical part of the glass surface modification procedure is glass pre-treatment. Good results were obtained with glass boiled in water for 2.5 h or more.
S. Yamamoto, A. Kita
Journal of Chromatography A, 1065 (2005) 45-50(2005) 45-50
Although linear salt gradient elution ion-exchange chromatography (IEC) of proteins is commonly carried out with relatively short columns, it is still not clear how the column length affects the separation performance and the economics of the process. The separation performance can be adjusted by changing a combination of the column length, the gradient slope and the flow velocity. The same resolution can be obtained with a given column length with different combinations of the gradient slope and the flow velocity. This results in different separation time and elution volume at the same resolution. Based on our previous model, a method for determining the separation time and the elution volume relationship for the same resolution (iso-resolution curve) was developed. The effect of the column length and the mass transfer rate on the iso-resolution curve was examined. A long column and/or high mass transfer rate results in lesser elution volume. The resolution data with porous bead packed columns and monolithic columns were in good agreement with the calculated iso-resolution curves. Although the elution volume can be reduced with increasing column length, the pressure drop limits govern the optimum conditions.