Publications
2010
F. Smrekar, M. Ciringer, A. Štrancar, A. Podgornik
Journal of Chromatography A, 1218 (2011) 2438-2444
Binding of three different bacteriophages (phages), namely T7, lambda and M13 on methacrylate monoliths was investigated. Phage M13 exhibited the highest dynamic binding capacity of 4.5 × 1013 pfu/mL while T7 and lambda showed capacity of 1 × 1013 pfu/mL, all corresponding to values of around 1 mg/mL. Interestingly, capacity for lambda phage was increased 5-fold by increasing NaCl concentration in a loaded sample from 0 to 0.2 M while there was a constant capacity decrease for T7 and M13 phages. Under optimal conditions, recovery for all three phages approached 100%. Measurement of a pressure drop increase during loading enabled estimation of adsorbed phage layer thickness. At a maximal capacity it was calculated to be around 50 nm for T7 phage and 60 nm for lambda phage matching closely capside size thus indicating monolayer adsorption while 80 nm layer thickness was estimated for M13 phage showing its orientation along the pore.
P. Kramberger, R. C. Honour, R. E. Herman, F. Smrekar, M. Peterka
Journal of Virological Methods 166 (2010) 60–64166 (2010) 60–64
Bacteriophages (phages) are known to be useful in many fields from medicine to agriculture, and for a broad range of applications, including phage therapy and phage display. For some applications, especially in medicine, high purity and viability of phages are required. Methacrylate monoliths (Convective Interaction Media [CIM] monolithic columns), designed for purification of bionanoparticles, were applied for the purification of Staphylococcus aureus phages VDX-10 from bacterial lysate. With a single step purification method, more than 99% of host cell DNA and more than 90% of proteins were removed, with 60% recovery of viable phages. Comparable results were obtained when the purification method was scaled-up from a CIM monolithic disk to a larger CIM monolithic column. Additionally, the dynamic binding capacity of a methacrylate monolith column for S. aureus phages VDX-10 was determined.
M. Peterka, P. Kramberger, A. Štrancar
Wang, Perry G. (ur.). Monolithic chromatography and its modern applications. St Albans: ILM publications, 2010, pg. 489-508
Downstream processing (DSP) for purification can become a significant bottleneck in the production of novel biotherapeutics, such as viral vectors and vaccines (viral or DNA). Although different techniques can be used for the purification of large molecules and particles, liquid chromatography is the preferred method as it achieves the purity required by regulatory agencies. Despite the popularity of conventional chromatographic media, the diffusional mass transfer of large molecules and relatively small pore size remain limiting factors for the efficient separation of large biomolecules and particles.
E.A. Ponomareva, V.E. Kartuzova, E.G. Vlakh, T.B. Tennikova
Journal of Chromatography B, 878 (2010) 567–574
The effect of different modes of α-chymotrypsin attachment to the surface of methacrylate-based ultrashort monolithic minicolumns on enzyme activity has been studied. The immobilization of protease was carried out via direct covalent binding of chymotrypsin, as well as via its attachment through small and polymer spacers. It was established that the lowest enzyme activity against N-benzoyl-l-tyrosine ethyl ester was found for bioreactor obtained via direct attachment of chymotrypsin to the surface of GMA–EDMA minidisks, whereas the highest parameter close to that determined for dissolved enzyme was found in the case of bioreactor prepared by the introduction of copolymer of 2-deoxy-N-methacryloylamido-d-glucose with N-vinylpyrrolidone and acrolein as a long and flexible polymer spacer. Additionally, the effect of flow rate of substrate recirculation on bioconversion efficiency was examined. Independently on immobilization method, the increase of flow rate led to the raise of biocatalytic efficiency.
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.
Attachments
P. Gagnon
Roadmap to Process Development, issue 1/2009, BIA Separations
Introduction
Commercial purification process development involves harmonizing a complex hierarchy of safety, regulatory, and economic considerations with the unique physicochemical characteristics of the product and the suite of contaminants that must be removed. This can be challenging even with product classes that exhibit fairly consistent chromatographic behavior, such as IgG monoclonal antibodies. It is even more demanding with products that do not support a platform approach. In either case, process development requires detailed knowledge of how the product behaves relative to contaminants within the operating ranges of the methods that may be used in its purification. This knowledge can be obtained only by characterizing product retention experimentally, a process that begins with initial screening. Screening produces the first indications of what methods offer the most promising fractionation capabilities, under what conditions, and in what order different methods may be linked together to yield an integrated multi-step purification procedure.
Attachments
E.G. Vlakh, T.B. Tennikova
Journal of Chromatography A, 1216 (2009) 2637-2650
Monolithic columns were introduced in the early 1990s and have become increasingly popular as efficient stationary phases for most of the important chromatographic separation modes. Monoliths are functionally distinct from porous particle-based media in their reliance on convective mass transport. This makes resolution and capacity independent of flow rate. Monoliths also lack a void volume. This eliminates eddy dispersion and permits high-resolution separations with extremely short flow paths. The analytical value of these features is the subject of recent reviews. Nowadays, among other types of rigid macroporous monoliths, the polymethacrylate-based materials are the largest and most examined class of these sorbents. In this review, the applications of polymethacrylate-based monolithic columns are summarized for the separation, purification and analysis of low and high molecular mass compounds in the different HPLC formats, including micro- and large-scale HPLC modes.
J. L. Ammerman, J. H. Aldstadt III
Microchim Acta (2009) 164:185-196
We describe the development and optimization of a sensitive and selective screening method for the measurement of trace levels of microcystins in surface waters. Several sample preparation techniques were compared, including solid-phase microextraction (SPME), particle-based solid-phase extraction (SPE), and monolith-based SPE. A flow-injection (FI) based approach employing a reversed-phase monolithic SPE column was found to be optimal. Quantification was performed by directly interfacing the FI-based SPE system to an electrospray ionization-mass spectrometer (ESI-MS). To more safely simulate peptidyl toxins such as the microcystins, a model peptide (i.e., angiotensin II) was used for method optimization. Sample loading flow rate and volume, eluent composition, and elution flow rate were optimized. Sample throughput was six samples per hour, a detection limit of 1.31 ng angiotensin II was demonstrated for a linear dynamic range from 1–1,000 ng and 3.4% relative standard deviation (n = 4, 100 ng sample). Sample volumes up to 1,000 ml of surface water could be loaded onto the monolithic SPE disk without exceeding the sorbent’s capacity. Unlike conventional particle-based SPE methods, the monolithic SPE disk does not need to be replaced between samples and could be used indefinitely. The FI-based SPE-ESI-MS method was successfully applied to the determination of microcystin-LR, the most common of the microcystins, in environmental samples and was demonstrated for the direct monitoring of chlorinated drinking water, with trends tracked over a period of eight months.
K. Kovač, I. Gutierrez-Aguirre, M. Banjac, M. Peterka, M. Poljšak-Prijatelj, M. Ravnikar, J. Zimšek Mijovski, A. C. Schultze, P. Raspor
Journal of Virological Methods 162 (2009) 272–275
Human enteric viruses are detected frequently in various types of environmental water samples, such as irrigation water, wastewater, recreational water, ground or subsurface water and even drinking water, constituting a primary source of gastroenteritis or hepatitis outbreaks. Only a few, but still infective number of viral particles are normally present in water samples, therefore an efficient virus concentration procedure is essential prior to molecular detection of the viral nucleic acid. In this study, a novel chromatographic technology, Convective Interaction Media® (CIM) monolithic supports, were optimized and applied to the concentration of hepatitis A virus (HAV) and feline calicivirus (FCV), a surrogate of norovirus (NoV), from water samples. Two-step real-time RT-qPCR was used for quantitation of the virus concentration in the chromatographic fractions. Positively charged CIM QA (quaternary amine) monolithic columns were used for binding of HAV and FCV present in previously inoculated 1.5 l bottled water samples. Column bound viruses were eluted from the monolith using 1 M NaCl to a final volume of 15 ml. Elution volume was concentrated further by ultracentrifugation. When the CIM/ultracentrifugation method was compared with another concentration method employing positively charged membranes and ultrafiltration, the recovery of HAV was improved by approximately 20%.
E. I. Trilisky, H. Koku, K. J. Czymmek, A. M. Lenhoff
Journal of Chromatography A, 1216 (2009) 6365–6376
Commercially available polymer-based monolithic and perfusive stationary phases were evaluated for their applicability in chromatography of biologics. Information on bed geometry, including that from electron microscopy (EM), was used to interpret and predict accessible volumes, binding capacities, and pressure drops. For preparative purification of biologics up to at least 7 nm in diameter, monoliths and perfusive resins are inferior to conventional stationary phases due to their low binding capacities (20–30 g/L for BSA). For larger biologics, up to several hundred nanometers in diameter, calculations from EM images predict a potential increase in binding capacity to nearly 100 g/L. The accessible volume for adenovirus calculated from the EM images matched the experimental value. While the pores of perfusive resins are essentially inaccessible to adenovirus under binding conditions, under non-adsorbing conditions the accessible intrabead porosity is almost as large as the interbead porosity. Modeling of breakthrough curves showed that the experimentally observed slow approach to full saturation can be explained by the distribution of pore sizes.
M. R. Etzel, W. T. Riordan
Jorunal of Chromatography A 1216 (2009) 2621-2624
Clearance of biological impurities is an essential part of the manufacture of biotechnology-derived products such as monoclonal antibodies (mAbs). Salt is required during manufacture to solubilize the mAb product and stabilize it against aggregation, but salt can be a problem later during impurity clearance operations. In this work, the use of a traditional quaternary amine (Q) monolith, and a new salt-tolerant monolith were evaluated for the clearance of pathogenic impurities including viruses, DNA, and host-cell protein (HCP). The impact of flow rate, salt concentration, and presence of mixtures of impurities in the feed stream were evaluated. Both monoliths cleared DNA to the limit of detection at all salt concentrations, and both cleared virus and HCP equally well at no salt. At intermediate salt, clearance of HCP was greater for the salt-tolerant monolith, and only the salt-tolerant monolith cleared virus at elevated salt. In conclusion, monoliths successfully trapped impurities such as DNA, host-cell protein, and viruses, and at flow rates far greater than traditional chromatography columns packed with beads.
R. J. Whitfield, S. E. Battom, M. Barut, D. E. Gilham, P. D. Ball
Journal of Chromatography A, 1216 (2009) 2725-2729
To support effective process development there is a requirement for rapid analytical methods that can identify and quantitate adenoviral particles throughout the manufacturing process, from cellular lysate through to purified adenovirus. An anion-exchange high-performance liquid chromatography method for the analysis of adenovirus type 5 (Ad5) particles has been developed using a novel quaternary amine monolithic column (Bio-Monolith QA, Agilent). The developed method separates intact Ad5 from contaminating proteins and DNA, thus allowing analysis of non-purified samples during process development. Regeneration conditions were incorporated to extend the functional life of the column. Once developed, the method was qualified according to performance criteria of repeatability, intermediate precision and linearity. The linear working range of analysis was established between 7.5 × 108 to at least 2.4 × 1010 viral particles (3 × 1010 to 9.6 × 1011 viral particles/mL), with a correlation coefficient of 0.9992. Relative standard deviations (RSDs) for intra- and inter-day repeatability and precision for retention time and peak area were less than 1 and 2.5%, respectively.
M. C. Cheeks, N. Kamal, A. Sorrel, D. Darling, F. Farzaneh, N. K. H. Slater
Journal of Chromatography A, 1216 (2009) 2705–2711
Histidine-tagged lentiviral vectors were separated from crude cell culture supernatant using labscale monolithic adsorbents by immobilized metal affinity chromatography. The capture capacity, concentration factor, purification factor, and elution efficiency of a supermacroporous cryogel monolith were evaluated against the Sartorius BIA Separations convective interaction media (CIM) disc, which is a commercial macroporous monolith. The morphology of the polymeric cryogel material was characterised by scanning electron microscopy. Iminodiacetic acid was used as the metal chelating ligand in both monoliths and the chelating capacity for metal ions was found to be comparable. The CIM-IDA-Ni2+ adsorbent had the greatest capture capacity (6.7 × 108 IU/ml of adsorbent), concentration factor (1.3-fold), and elution efficiency (69%). Advantages of the cryogel monoliths included rapid, low pressure processing as well low levels of protein and DNA in the final purified vector preparations.
I. Gutiérrez-Aguirre, M. Banjac, A. Steyer, M. Poljšak-Prijatelj, M. Peterka, A. Štrancar, M. Ravnikar
Journal of Chromatography A, 1216 (2009) 2700–2704
Rotaviruses are the leading cause of diarrhoea in infants around the globe and, under certain conditions they can be present in drinking water sources and systems. Ingestion of 10–100 viral particles is enough to cause disease, emphasizing the need for sensitive diagnostic methods. In this study we have optimized the concentration of rotavirus particles using methacrylate monolithic chromatographic supports. Different surface chemistries and mobile phases were tested. A strong anion exchanger and phosphate buffer (pH 7) resulted in the highest recoveries after elution of the bound virus with 1 M NaCl. Using this approach, rotavirus particles spiked in 1 l volumes of tap or river water were efficiently concentrated. The developed concentration method in combination with a real time quantitative polymerase chain reaction assay detected rotavirus concentrations as low as 100 rotavirus particles/ml.
C. Delattre, M. A. Vijayalakshmi
Journal of Molecular Catalysis B: Enzymatic 60 (2009) 97–105
Recent research in the area of bioactive carbohydrates has shown the efficiency of oligosaccharides as signal molecules in a lot of biological activities. Newly observed functions of oligosaccharides and their abilities to act as specific regulatory molecules on various organisms have been more and more described. A successful development of these bioactive molecules in future needs efficient processes for specific oligosaccharides production. To exploit them for putative industrial scale up processes, two main strategies are currently investigated: the synthesis (chemical or bioconversion processes) and the polysaccharide cleavage (chemical, physical or biological processes). Nevertheless, if new manufacturing biotechnologies have considerably increased the development of these functional molecules, the main drawback limiting their biological applications is the complexity to engender specific glycosidic structures for specific activities. In the recent years, new enzymatic reactors have been developed, allowing the automatic synthesis of oligosaccharide structures. This review focuses on the knowledge in the area of bioactive oligosaccharides and gives the main processes employed to generate them for industrial applications with challenges of monolith microreactors.
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.
V. Frankovič, A. Podgornik, N. Lendero Krajnc, F. Smrekar, P. Krajnc, A. Štrancar
Journal of Chromatography A, 1207 (2008) 84–93(2008) 84 – 93
A weak ion-exchange grafted methacrylate monolith was prepared by grafting a methacrylate monolith with glycidyl methacrylate and subsequently modifying the epoxy groups with diethylamine. The thickness of the grafted layer was determined by measuring permeability and found to be approximately 90 nm. The effects of different buffer solutions on the pressure drop were examined and indicated the influence of pH on the permeability of the grafted monolith. Protein separation and binding capacity (BC) were found to be flow-unaffected up to a linear velocity of 280 cm/h. A comparison of the BC for the non-grafted and grafted monolith was performed using β-lactoglobulin, bovine serum albumin (BSA), thyroglobulin, and plasmid DNA (pDNA). It was found that the grafted monolith exhibited 2- to 3.5-fold higher capacities (as compared to non-grafted monoliths) in all cases reaching values of 105, 80, 71, and 17 mg/ml, respectively. It was determined that the maximum pDNA capacity was reached using 0.1 M NaCl in the loading buffer. Recovery was comparable and no degradation of the supercoiled pDNA form was detected. Protein z-factors were equal for the non-grafted and grafted monolith indicating that the same number of binding sites are available although elution from the grafted monolith occurred at higher ionic strengths. The grafted monolith exhibited lower efficiency than the non-grafted ones. However, the baseline separation of pDNA from RNA and other impurities was achieved from a real sample.
A. Jungbauer, R. Hahn
Journal of Chromatography A, 1184 (2008) 62–79(2008) 62 – 79
Monoliths are considered as the fourth-generation chromatography material. Their use for preparative separation of biomolecules has been evolved over the past decade. Monolithic columns up to 8 L in size are already commercially available for separation of large biomolecules such as proteins, protein aggregates, plasmid DNA, and viruses. These applications leverage monoliths’ inherent properties, such as fast operation and high capacity for large biomolecules. The height equivalent to a theoretical plate (HETP) and dynamic binding capacity do not change with velocity. This is explained by the convective transport through the channels with a diameter of above 1000 nm and has been experimentally verified and also supported by theoretical analyses. Despite low absolute surface area, these large channels provide enough area for adsorption of these large biomolecules, which cannot penetrate into conventional chromatography media designed for protein separation. Monoliths for preparative separations are mainly cast as polymethacrylate or polyacrylamide blocks and have been functionalized as ion exchangers or hydrophobic interaction chromatography media. So-called cryogels have channels more than 30 μm wide, enabling efficient processing of suspensions or even cell-chromatography. This review discusses the pressure drop characteristics, mass transfer properties, scale-up, and applications of monoliths in the context of conventional chromatography media.
E. S. Sinitsyna, E. N. Vlasova, E. G. Vlakh, T. B. Tennikova
Russian Journal of Applied Chemistry, 2008, Vol. 81, No. 8, pp. 1403–1409
Copolymers containing aldehyde, succinimidyl carbonate, and imidazolecarbamate groups were prepared by polymer-analogous transformations of epoxy groups of a macroporous monolithic polymeric support derived from glycidyl methacrylate and ethylene glycol dimethacyrlate. The effect of certain parameters on the course of the copolymer modification and immobilization of a protein on the surface of the polymeric support was studied. The possibility of using the matrices obtained for development of biorecognizing systems was examined.