Publications
2011
E. F. Maksimova, E. G. Vlakh, T. B. Tennikova
Journal of Chromatography A, 1218 (2011) 2425-2431
A series of macroporous monolithic methacrylate-based materials was synthesized by in situ free radical UV-initiated copolymerization of functional monomers, such as glycidyl methacrylate (GMA), butyl methacrylate (BuMA), 2-aminoethyl methacrylate (AEMA), 2-hydroxyethyl methacrylate (HEMA) and 2-cyanoethyl methacrylate (CEMA), with crosslinking agent, namely, ethylene glycol dimethacrylate (EDMA). The materials obtained were applied as the stationary phases in simple and robust technique – planar chromatography (PLC). The method of separation layer fabrication representing macroporous polymer monolith bound to the specially prepared glass surface was developed and optimized. The GMA–EDMA and BuMA–EDMA matrixes were successfully applied for the separation of low molecular weight compounds (the mixture of several dies), as well as poly(vinylpyrrolidone) and polystyrene homopolymers of different molecular weights using reversed-phase mechanism. The materials based on copolymers AEMA–HEMA–EDMA and CEMA–HEMA–EDMA were used for normal-phase PLC separation of 2,4-dinitrophenyl amino acids and polystyrene standards.
M. R. Etzel, T. Bund
Journal of Chromatography A, 1218 (2011) 2445-2450
Proteins conjugated to neutral biopolymers are of keen interest to the food and pharmaceutical industries. Conjugated proteins are larger and more charge shielded than un-reacted proteins, making purification difficult using conventional beaded chromatographic supports because of slow mass transfer rates, weak binding, and viscous solutions. Past methods developed for pharmaceuticals are unsuitable for foods. In this work, a food-grade whey protein–dextran conjugate was purified from a feed solution also containing un-reacted protein and dextran using either a column packed with 800 mL of a beaded support that was specifically designed for purification of conjugated proteins or an 8 mL tube monolith. The monolith gave a similar dynamic binding capacity as the beaded support (4–6 g/L), at a 42-fold greater mass productivity, and 48-fold higher flow rate, albeit at somewhat lower conjugate purity. Performance of the monolith did not depend on flow rate. In conclusion, monoliths were found to be well suited for the purification of whey protein–dextran conjugates.
I. Pulko, V. Smrekar, A. Podgornik, P. Krajnc
Journal of Chromatography A, 1218 (2011) 2396-2401
Approximately 25 cm × 25 cm large sheets of crosslinked highly porous poly(glycidyl methacrylate-co-ethyleneglycol dimethacrylate-co-ethylhexyl methacrylate) membranes with an average thicknesses between 285 and 565 μm were prepared by casting a high internal phase emulsion (HIPE) containing monomers onto glass substrates and subsequent polymerisation. Open cellular porous polyHIPE type membranes were obtained with large pores (cavity) sizes between 3 and 10 μm while interconnecting pores were between 1 and 3 μm. The percentage of ethylhexyl acrylate and ethyleneglycol dimethacrylate influenced the flexibility and morphology of the resulting membranes. Porous membranes were chemically modified with diethylamine to yield functionalised supports for ion exchange chromatography. Cylindrical housings were used for positioning of the membranes and allowing flow of the mobile phase. Pulse experiments were used to study the flow characteristics and a homogeneous flow through the entire area of the membrane was found. Bovine serum albumin was purified by a 8 ml column containing functional membrane in modular shape; dynamic binding capacity was measured to be as high as 45 mg/ml.
C. Valasek, J. Cole, F. Hensel, P. Ye, M. A. Conner, M. E. Ultee
BioProcess International, Vol. 9, No. 11, December 2011, pp. 28–37
Immunoglobulin G (IgG) antibodies have been used to treat cancer for many years (1). Another class of antibodies—immunoglobulin M (IgM)—has been overlooked in spite of offering unique advantages that make them highly desirable as cancer therapeutics. Serving a valuable function in our innate immune system, IgM antibodies are the first to be secreted when an abnormal cell is present (2). These antibodies play a critical role in recognition and elimination of infectious particles (3,4), in removal of intracellular components, and in immunosurveillance mechanisms against malignant cells (5,6). IgMs also can bind to multiple copies of a target on a cancer cell surface. Such high avidity leads to cross-linking and more effective cell killing (7).
P. Gagnon, F. Hensel, S. Lee, S. Zaidi
Journal of Chromatography A, 1218 (2011) 2405-2412
This study documents the presence of stable complexes between monoclonal IgM and genomic DNA in freshly harvested mammalian cell culture supernatants. 75% of the complex population elutes from size exclusion chromatography with the same retention volume as IgM. DNA comprises 24% of the complex mass, corresponding to an average of 347 base pairs per IgM molecule, distributed among fragments smaller than about 115 base pairs. Electrostatic interactions appear to provide most of the binding energy, with secondary stabilization by hydrogen bonding and metal affinity. DNA-dominant complexes are unretained by bioaffinity chromatography, while IgM-dominant complexes are retained and coelute with IgM. DNA-dominant complexes are repelled from cation exchangers, while IgM-dominant complexes are retained and partially dissociated. Partially dissociated forms elute in order of decreasing DNA content. The same pattern is observed with hydrophobic interaction chromatography. All complex compositions bind to anion exchangers and elute in order of increasing DNA content. A porous particle anion exchanger was unable to dissociate DNA from IgM. Monolithic anion exchangers, offering up to15-fold higher charge density, achieved nearly complete complex dissociation. The charge-dense monolith surface appears to outcompete IgM for the DNA. Monoliths also exhibit more than double the IgM dynamic binding capacity of the porous particle anion exchanger, apparently due to better surface accessibility and more efficient mass transfer.
P. Gagnon, G. Rodriquez, S. Zaidi
Journal of Chromatography A, 1218 (2011) 2402-2404
A basic method for dissociation and fractionation of monoclonal IgG heavy and light chain is described. It employs less noxious and hazardous reagents than the classical mercaptoethanol/propionic acid process and replaces size exclusion chromatography with cation exchange on a monolith to improve productivity. Significant scope remains to refine the conditions. The method can be applied to other disulfide bonded proteins with significant affinity for cation exchangers.
S. Neff, A. Jungbauer
Journal of Chromatography A, 1218 (2011) 2374-2380
We have developed a method for quantification of a specific monoclonal IgM directed toward embryonic stem cells based on a peptide affinity monolith. A peptide affinity ligand with the sequence C–C–H–Q–R–L–S–Q–R–K was obtained by epitope mapping using peptide SPOT synthesis. The peptide ligand was covalently immobilized by coupling the N-terminal cysteine to a monolithic disk that was previously modified with iodated spacer molecules. The monolithic disc was used for quantification of purified IgM and for IgM present in mammalian cell culture supernatant. We observed 17% unspecific binding of IgM to the monolithic disk and additionally a product loss in the flow through of 20%. Nevertheless, calibration curves had high correlation coefficients and inter/intra-assay variability experiments proved sufficient precision of the method. A limit of quantification of 51.69 μg/mL for purified IgM and 48.40 μg/mL for IgM in cell culture supernatant could be calculated. The binding capacity was consistent within the period of the study which included more than 200 cycles. The analysis time of less than 2 min is an advantage over existing chromatographic methods that rely on pore diffusion.
A. Mönster, O. Hiller, D. Grüger, R. Blasczyk, C. Kasper
Journal of Chromatography A, 1218 (2011) 706–710
Monolithic columns have gained increasing attention as stationary phases for the separation of biomolecules and biopharmaceuticals. In the present work the performance of monolithic convective interaction media (CIM®) chromatography for the purification of blood group antigens was established. The proteins employed in this study are derived from blood group antigens Knops, JMH and Scianna, equipped both with a His-tag and with a V5-tag by which they can be purified. In a first step a monoclonal antibody directed against the V5-tag was immobilized on a CIM® Disk with epoxy chemistry. After this, the immobilized CIM® Disk was used in immuno-affinity chromatography to purify the three blood group antigens from cell culture supernatant. Up-scaling of the applied technology was carried out using CIM® Tubes. In comparison to conventional affinity chromatography, blood group antigens were also purified via His-tag using a HiTrap® metal-affinity column. The two purifications have been compared regarding purity, yield and purification speed. Using the monolithic support, it was possible to isolate the blood group antigens with a higher flow rate than using the conventional bed-packed column.
R. D. Arrua, C. I. Alvarez Igarzabal
J. Sep. Sci. 2011, 34, 1974–1987
In the early 1990s, three research groups simultaneously developed continuous macroporous rod-shaped polymeric systems to eliminate the problem of flow through the interparticle spaces generally presented by the chromatography columns that use particles as filler. The great advantage of those materials, forming a continuous phase rod, is to increase the mass transfer by convective transport, as the mobile phase is forced to go through all means of separation, in contrast to particulate media where the mobile phase flows through the interparticle spaces. Due to their special characteristics, the monolithic polymers are used as base-supports in different separation techniques, those chromatographic processes being the most important and, to a greater extent, those involving the separation of biomolecules as in the case of affinity chromatography. This mini-review reports the contributions of several groups to the development of macroporous monoliths and their modification by immobilization of specific ligands on the products for their application in affinity chromatography.
S. Neff, A. Jungbauer
Journal of Chromatography A, 1218 (2011) 2374–2380
We have developed a method for quantification of a specific monoclonal IgM directed toward embryonic stem cells based on a peptide affinity monolith. A peptide affinity ligand with the sequence C–C–H–Q–R–L–S–Q–R–K was obtained by epitope mapping using peptide SPOT synthesis. The peptide ligand was covalently immobilized by coupling the N-terminal cysteine to a monolithic disk that was previously modified with iodated spacer molecules. The monolithic disc was used for quantification of purified IgM and for IgM present in mammalian cell culture supernatant. We observed 17% unspecific binding of IgM to the monolithic disk and additionally a product loss in the flow through of 20%. Nevertheless, calibration curves had high correlation coefficients and inter/intra-assay variability experiments proved sufficient precision of the method. A limit of quantification of 51.69 μg/mL for purified IgM and 48.40 μg/mL for IgM in cell culture supernatant could be calculated. The binding capacity was consistent within the period of the study which included more than 200 cycles. The analysis time of less than 2 min is an advantage over existing chromatographic methods that rely on pore diffusion.
H. Shirataki, C. Sudoh, T. Eshima, Y. Yokoyama, K. Okuyama
Journal of Chromatography A, 1218 (2011) 2381–2388
It is widely recognized that membrane adsorbers are powerful tools for the purification of biopharmaceutical protein products and for this reason a novel hollow-fiber AEX type membrane adsorber has been developed. The membrane is characterized by grafted chains including DEA ligands affixed to the pore surfaces of the membrane. In order to estimate the membrane performance, (1) dynamic binding capacities for pure BSA and DNA over a range of solution conductivity and pH, (2) virus reduction by flow-through process, and (3) HCP and DNA removal from cell culture, are evaluated and compared with several other anion-exchange membranes. The novel hollow-fiber membrane is tolerant of high salt concentration when adsorbing BSA and DNA. When challenged with a solution containing IgG the membrane has high impurity removal further indicating this hollow-fiber based membrane adsorber is an effective tool for purification of biopharmaceutical protein products including IgG.
A. Trauner, M. H. Bennett, H. D. Williams
PLoS ONE 6(2): e16273. doi:10.1371/ journal.pone.0016273
We report the development of a rapid chromatographic method for the isolation of bacterial ribosomes from crude cell lysates in less than ten minutes. Our separation is based on the use of strong anion exchange monolithic columns. Using a simple stepwise elution program we were able to purify ribosomes whose composition is comparable to those isolated by sucrose gradient ultracentrifugation, as confirmed by quantitative proteomic analysis (iTRAQ). The speed and simplicity of this approach could accelerate the study of many different aspects of ribosomal biology.
2010
P. Gagnon
BioProcess International, Nov 2010
The enabling value of monoliths was strongly in evidence at the 4th International Monolith Symposium, held 29 May – 2 June in the Adriatic resort city of Portoroz, Slovenia. Forty-seven oral presentations and 34 posters highlighted important advances in vaccines, gene therapy, phage therapy for infectious disease, and monoclonal antibodies, as well as continuing advances in the performance of monoliths themselves. As these fields advance in parallel, it becomes increasingly apparent that monoliths offer industrial capabilities substantially beyond traditional methods.
M. Abe, P. Akbarzaderaleh, M. Hamachi, N. Yoshimoto, S.Yamamoto
Biotechnol. J. 2010, 5, 477-483
The retention and binding mechanisms in electrostatic interaction-based chromatography (ion-exchange chromatography) of PEGylated proteins (covalent attachment of polyethylene glycol chains to protein) were investigated using our previously developed model. Lysozyme and bovine serum albumin were chosen as model proteins. The retention volume of PEGylated proteins shifted to lower elution volumes with increasing PEG molecular weight compared with the non-modified (native) protein retention volume. However, PEGylation did not affect the number of binding sites appreciably. The enzyme activity of PEGylated lysozyme measured with a standard insoluble substrate in suspension decreased considerably, whereas the activity with a soluble small-molecule substrate did not drop significantly. These findings indicate that when a protein is mono-PEG-ylated, the binding site is not affected and the elution volume reduces due to the steric hindrance between PEGylated protein and ion-exchange ligand.
R. Nian, D. S. Kim, T. Nguyen, L. Tan, C.-W. Kim, I.-K. Yoo, W. S. Choe
Journal of Chromatography A, 1217 (2010) 5910-5949
Toxic heavy metal pollution is a global problem occurring in air, soil as well as water. There is a need for a more cost effective, renewable remediation technique, but most importantly, for a recovery method that is selective for one specific metal of concern. Phage display technology has been used as a powerful tool in the discovery of peptides capable of exhibiting specific affinity to various metals or metal ions. However, traditional phage display is mainly conducted in batch mode, resulting in only one equilibrium state hence low-efficiency selection. It is also unable to monitor the selection process in real time mode. In this study, phage display technique was incorporated with chromatography procedure with the use of a monolithic column, facilitating multiple phage-binding equilibrium states and online monitoring of the selection process in search of affinity peptides to Pb2+. In total, 17 candidate peptides were found and their specificity toward Pb2+ was further investigated with bead-based enzyme immunoassay (EIA). A highly specific Pb2+ binding peptide ThrAsnThrLeuSerAsnAsn (TNTLSNN) was obtained. Based on our knowledge, this is the first report on a new chromatographic biopanning method coupled with monolithic column for the selection of metal ion specific binding peptides. It is expected that this monolith-based chromatographic biopanning will provide a promising approach for a high throughput screening of affinity peptides cognitive of a wide range of target species.
R. R. Prasanna, M. A. Vijayalakshmi
Journal of Chromatography A, 1217 (2010) 3660–3667
Dynamic binding capacity (DBC) of commercial metal-chelate methacrylate monolith-convective interaction media (CIM) was performed with commercial human immunoglobulin G (IgG) (Cohn fraction II, III). Monoliths are an attractive stationary phase for purification of large biomolecules because they exhibit very low back pressure even at high flow rates and flow-unaffected binding properties. Adsorption of IgG onto CIM-IDA disk immobilized with Cu2+, Ni2+ and Zn2+ were studied with Tris-acetate (TA), phosphate-acetate (PA) and MMA (MES, MOPS and acetate) buffer systems at different flow rates. Adsorption and elution of IgG varied with different buffers and adsorption of IgG was maximum with MMA buffer. Adsorption of human IgG from Cohn fractions (II, III) was high when Cu2+ was used as ligand. CIM-IDA disk showed dynamic binding capacity in the range of 14–16 mg/ml with Cu2+ and 7–9 mg/ml with Ni2+ for human IgG with MMA buffer. In the case of CIM-IDA-Zn2+ column, the binding capacity was only about 0.5 mg/ml of support. Different desorption strategies like lowering of pH and increasing of competitive agent were also studied to achieve maximum recovery. Chromatographic runs with human serum and mouse ascites fluid were also carried out with metal chelate methacrylate monolithic disk and the results indicate the potential of this technique for polyclonal human IgG and monoclonal IgG purification from complex biological samples.
A. Dhivya, B. Kumar, R. Prasanna, N. Vijayalakshmi
Chromatographia 2010, 72, December (No. 11/12), pg 1183-1188
Purified monoclonal antibodies (mAb) have been used in therapeutics and some analytical procedures. Purification of mAb by use of high-throughput anion-exchange methacrylate monolithic systems has been attempted in this work. Monolithic macroporous convective interaction media (CIM) with diethylaminoethyl (DEAE) and ethylene diamine (EDA) as anion-exchange ligands were used and evaluated for purification of anti-glycophorin-A IgG1 mouse mAbs from cell culture supernatant (CCS) after precipitation with 50% ammonium sulfate. The adsorption and elution of mAb from the CCS on CIM-DEAE and CIM-EDA disks were studied with three different buffer systems, acetate, MOPS (3-(N-morpholino)propanesulfonic acid), and Tris, to study the effect of the nature of buffer ions and to find the optimum buffer conditions for purification of mAb. The optimum buffers for purification of mAb using CIM-DEAE and CIM-EDA were 50 mM acetate buffer, pH 5.1 and 20 mM Tris buffer, pH 8.0, respectively. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) and enzyme-linked immunosorbent assay (ELISA) showed the antibody fractions obtained were highly pure, with high antigen-binding efficiency. High specific activity with purification factors of 130 ± 34 (unretained fraction with acetate buffer) and 74 ± 13 (fraction eluted with Tris buffer containing 0.6 M NaCl) was obtained for IgG1 using the CIM-DEAE and CIM-EDA disks, respectively. The results indicate that rapid separation and efficient recovery of high-purity anti-glycophorin-A mAbs could be achieved by use of anion-exchange CIM disks.
A. Čevdek, M. Franko
Analytical and Bioanalytical Chemistry 398 (2010), 555-562
This work presents a comparison of convective interaction media (CIM) and controlled pore glass (CPG) as solid supports for immunoglobulin antibodies used in bioanalytical detection of allergens in foodstuffs. A flow-injection manifold with highly sensitive thermal lens spectrometric detection was used for this purpose. Using beta-lactoglobulin, a milk allergen, as a model analyte, CIM disc supports had a higher linear range (0.2–3.5 μg L-1), better reproducibility (intra-day RSD = 1%, inter-day RSD = 10%), lower consumption of reagents, and better immunocolumn stability (1 month, over 240 injections of substrate), while providing comparable LODs (0.1 μg L-1). Application of CIM discs as solid supports in immunocolumns for allergen detection enables fast and sensitive screening of allergens in foodstuffs with sample throughput of up to eight samples per hour.
P. Gagnon
Roadmap to Process Development, issue 3/2010, Sartorius BIA Separations
Introduction
The first two articles in this series addressed column selectivity and capacity. This article discusses how to apply results from these preliminary studies to create fully functional multi-step purification procedures. The principles described here can be applied to proteins, plasmids, or virus particles.
Process modeling represents a nexus at which the theoretical ideals of purification meet the practical limitations of the laboratory, or in less elegant terms: where the rubber meets the road. The key theoretical principle is the notion of developing an orthogonal purification process. Orthogonal means pertaining to right angles. In purification terms, it translates to combining purification methods that are highly complementary to one another. Its value resides in the presumption that different purification methods bind the product by different sites, along with a unique subset of contaminants. The more complementary the methods, the lower the overlap in contaminant subsets, and the higher the purification factor offered by the particular combination of methods.
Attachments
2009
P. Gagnon
Roadmap to Process Development, issue 2/2009, Sartorius BIA Separations
Introduction
Determination of column loading capacity is a critical component of purification process development. Its most obvious link is to process economics, since the more product that can be loaded per unit of media volume, the smaller the column and volume of buffers, and the smaller the process footprint (manufacturing space requirement). But binding capacity is also linked directly to loading conditions, and beyond that, loading is a key determinant of purification performance and reproducibility. In practice, determination of optimal loading is tedious, time consuming, and expensive, especially due to the large amounts of sample it requires. This makes it all the more important to get it right the first time.
The objectives of this article are to highlight the process considerations that pertain to loading, and to provide you with a set of practical tools to determine capacity values that are meaningful in your particular usage context.