Publications
2008
P. Gagnon
MSS2008
When monoclonal antibodies were first beginning to be commercialized, expression levels over 100 mg/L were considered outstanding, and cell culture was viewed as the bottleneck in manufacturing productivity. Antibody expression levels now commonly exceed 1 g/L and reports of 10 and 15 g/L have been recently announced. Downstream processing is now considered the bottleneck.
In one sense, the bottleneck is artificial. Cell culture production takes about two weeks (not counting preparation of seed stock) and purification takes about a week. In another sense, the bottleneck is real, and a genuine concern. Process time for the protein A capture step from 20,000 L of cell culture supernatant (CCS) commonly requires 72-96 hours. This represents multiple cycles. The long hold time for IgG produced in the early cycles increases the risk of degradation by proteolysis, deamidation, etc. It also increases the risk of contamination.
C. Delattre, P. Michaud, M. A. Vijayalakshmi
Journal of Chromatography B, 861 (2008) 203–208
Fast production and purification of α-(1,4)-oligogalacturonides was investigated using a new enzymatic reactor composed of a monolithic matrix. Pectin lyase from Aspergillus japonicus (Sigma) was immobilized on CIM-disk epoxy monolith. Studies were performed on free pectin lyase and immobilized pectin lyase to compare the optimum temperature, optimum pH, and thermal stability. It was determined that optimum temperature for free pectin lyase and immobilized pectin lyase on monolithic support is 30 °C, and optimum pH is 5. Monolithic CIM-disk chromatography is one of the fastest liquid chromatographic method used for separation and purification of biomolecules due to high mass transfer rate. In this context, online one step production and purification of oligogalacturonides was investigated associating CIM-disk pectin lyase and CIM-disk DEAE. This efficient enzymatic bioreactor production of uronic oligosaccharides from polygalacturonic acid (PGA) constitutes an original fast process to generate bioactive oligouronides.
2007
K. Isobe, Y. Kawakami
Journal of Chromatography A, 1144 (2007) 85-89(2007) 85-89
A convection interaction media (trade name CIM, Sartorius BIA Separation, Ljubljana, Slovenia) isobutyl monolithic disc was prepared by incubating a CIM epoxy monolithic disc with isobutylamine, and it was then applied to the purification of secondary alcohol dehydrogenase (S-ADH) and primary alcohol oxidase (P-AOD). Both enzymes were adsorbed on this column and eluted with high purity. Thus, S-ADH was purified to an electrophoretically homogeneous state by four column chromatographies using CIM DEAE-8 and CIM C4-8 tube monolithic columns, blue-Sepharose column and CIM isobutyl disc monolithic column. P-AOD was also purified to an electrophoretically homogeneous state by three column chromatographies of CIM DEAE-8 tube, CIM C4-8 tube and CIM isobutyl disc columns.
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.
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).
M. Benčina, J. Babič, A. Podgornik
Journal of Chromatography A, 1144 (2007) 135–142
In gene therapy and DNA vaccination, RNA removal from DNA preparations is vital and is typically achieved by the addition of ribonuclease into the sample. Removal of ribonuclease from DNA samples requires an additional purification step. An alternative is the implementation of immobilized ribonuclease. In our work, ribonuclease was covalently coupled onto the surface of methacrylate monoliths via epoxy or imidazole carbamate groups. Various immobilization conditions were tested by changing immobilization pH. Ribonuclease immobilized on the monolith via imidazole carbamate groups at pH 9 was found to be six times more active than the ribonuclease immobilized on the monolith via epoxy groups. Under optimal immobilization conditions the Michaelis–Menten constant, Km, for cytidine-2,3-cyclic monophosphate, and turnover number, k3 were 0.52 mM and 4.6 s-1, respectively, and mirrored properties of free enzyme. Enzyme reactor was found to efficiently eliminate RNA contaminants from DNA samples. It was active for several weeks of operation and processed 300 column volumes of sample. Required residence time to eliminate RNA was estimated to be around 0.5 min enabling flow rates above 1 column volume per min.
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
K. Isobe, Y. Kawakami
Journal of Chromatography A, 1065 (2005) 129-134
Chromatography conditions for two types of convection interaction media (CIM) tube monolithic column, DEAE-8 and C4-8, were investigated using three enzymes from different microorganisms. The enzymes were adsorbed on a CIM DEAE-8 tube column under the same conditions as conventional DEAE columns. The CIM C4-8 tube column required a high concentration of ammonium sulfate compared to the conventional C4 column for adsorbing the enzymes. The separation of enzymes on the CIM tube column chromatography was not affected at flow rates between 0.15 and 1.25 volumes of the column per min. Both columns were successfully applied to the purification of enzymes from crude enzyme solution. Thus, both CIM tube monolithic columns proved useful in greatly reducing the purification time, and could be used at any stage of enzyme purification.
I. Vovk, B. Simonovska, M. Benčina
Journal of Chromatography A, 1065 (2005) 121-128
One of the main forms of tomato pectin methylesterase (PME; EC 3.1.1.11) that is applicable to the food industry was isolated from fresh tomato fruit. The extraction of the PME isoenzymes involved washing the fresh tomato flesh with water in order to remove sugars and than solubilizing the enzymes with a diluted HCl solution at pH 1.6. The extract was then neutralized to pH 7.4 using buffer solution. After filtration, the solution was directly fractioned using Convective Interaction Media (CIM®) short monolithic disk column bearing sulfonyl (SO3) groups and using a linear gradient from 0 to 700 mM NaCl. The injection volume was 3 ml and the diameter of the column was 12 mm and length 3 mm. The isolated fractions were monitored for protein content and PME activity. The fraction with the targeted enzyme, which showed NaCl independent activity, was further purified and concentrated by ultrafiltration and finally purified by a second semi-preparative cation-exchange chromatography step using a CIM carboxymethyl (CM) disk monolithic column consisting of two disks and applying a step gradient. From 1 kg of fresh tomato fruits, 7.5 mg of purified PME with molecular mass estimated to be 26 000 by sodium dodecyl sulfate–polyacrylamide gel electrophoresis (SDS–PAGE) was obtained. A fraction with mixed PME and polygalacturonase activity was also obtained. Compared to the published procedures for the isolation and purification of PME from plant materials, this new procedure is much faster and more efficient. The potential application of CIM disk short monolithic columns in the analysis and semi-preparative extraction and isolation of the PME isoenzyme is presented.
Y.-P. Lim, D. Josić, H. Callanan, J. Brown, D. C. Hixson
Journal of Chromatography A, 1065 (2005) 39–43(2005) 39–43
Epoxy-activated monolithic CIM disks seem to be excellent supports for immobilization of protein ligands. The potential use of enzymes, immobilized on monolithic disks for rapid preparative cleavage proteins in solution was investigated. Digestion of complex plasma proteins was demonstrated by using inter-alpha inhibitors with elastase, immobilized on epoxy-activated CIM disks. Recently, a monoclonal antibody against human inter-alpha inhibitor proteins (MAb 69.31) was developed. MAb 69.31 blocks the inhibitory activity of inter-alpha inhibitor proteins to serine proteases. These results suggest that the epitope defined by this antibody is located within or proximal to the active site of the inhibitor molecule. This antibody, immobilized on monolithic disk, was used for very rapid isolation of inter-alpha proteins. The isolated complex protein was used for enzymatic digestion and isolation of cleavage products, especially from inter-alpha inhibitor light chain to elucidate precisely the target sequence for MAb 69.31 by N-terminal amino acid sequencing. Bovine pancreatic elastase immobilized on monolithic disk cleaves inter-alpha inhibitor protein complex into small fragments which are still reactive with MAb 69.31. One of these proteolytic fragments was isolated and partially sequenced. It could be shown that this sequence is located at the beginning of two proteinase inhibitor domains of the inter-alpha inhibitor light chain (bikunin). Elastase immobilized on monolithic disk offers a simple and rapid method for preparative isolation of protease cleavage fragments. The immobilized enzyme is stable and still active after repeated runs. A partial or complete digestion can be achieved by varying the flow rate.
You'll need Skype CreditFree via Skype
M. Benčina, K. Benčina, A. Štrancar, A. Podgornik
Journal of Chromatography A, 1065 (2005) 83–91(2005) 83–91
A deoxyribonuclease bioreactor was prepared by immobilization of deoxyribonuclease I through epoxy groups inherently present on poly (glycidyl methacrylate-co-ethylene dimethacrylate) monoliths. Columns with various levels of DNase activity were prepared varying immobilization temperature, pH, time and method. The apparent Michaelis–Menten constant, Kmapp, and turnover number, k3app, for immobilized DNase determined by on-line frontal analysis method were, respectively, 0.28 g of DNA l-1 and 16 dA260nm min-1 mg-1 of immobilized DNase. The highest activity of immobilized DNase was detected at 1 mM calcium ions concentration and mirrored properties of free enzyme; however, reaction temperature in the range from 25 to 37 °C has no significant effect on activity of immobilized DNase in contrary to free enzyme. The CIM DNase bioreactor was used for elimination of DNA contaminants in RNA samples prior to reverse transcription followed by PCR.
You'll need Skype CreditFree via Skype
M. Bartolini, V. Cavrini, V. Andrisano
Journal of Chromatography A, 1065 (2005) 135-144
The aim of the present study was to optimize the preparation of an immobilized acetylcholinesterase (AChE)-based micro-immobilized enzyme reactor (IMER) for inhibition studies. For this purpose two polymeric monolithic disks (CIM, 3 mm × 12 mm i.d.) with different reactive groups (epoxy and ethylendiamino) and a packed silica column (3 mm × 5 mm i.d.; Glutaraldehyde-P, 40 μm) were selected as solid chromatographic supports. All these reactors were characterized in terms of rate of immobilization, stability, conditioning time for HPLC analyses, optimum mobile phase and peak shape, aspecific interactions and costs. Advantages and disadvantages were defined for each system. Immobilization through Schiff base linkage gave more stable reactors without any significant change in the enzyme behaviour; monolithic matrices showed very short conditioning time and fast recovery of the enzymatic activity that could represent very important features in high throughput analysis and satisfactory reproducibility of immobilization yield. Unpacked silica material allowed off-line low costs studies for the optimization of the immobilization step.
2004
T. Hall, D. C. Wood, C. E. Smith
Journal of Chromatography A, 1041 (2004) 87–93(2004) 87–93
Monolithic media were compared with Q- and SP-Sepharose high performance chromatography for preparative purification and with Q- and SP-5PW chromatography for analysis of a pegylated form of myelopoietin (MPO), an engineered hematopoietic growth factor. The use of either monolithic or Sepharose based supports for preparative chromatography produced highly purified pegylated MPO with the monolithic media demonstrating peak resolution and repeatability at flow rates of 1 and 5 ml/min resulting in run times as much as five-fold shorter compared to Sepharose separations. The monolithic disks also resulted in 10-fold shorter run times for the analytical chromatography, however, their chromatographic profiles and peak symmetry were not as sharp compared to their Q-5PW and SP-5PW counterparts.