Publications
2012
M. Lock, M. R. Alvira, J. M. Wilson
HUMAN GENE THERAPY METHODS: Part B 23:56-64 (February 2012)
Advances in adeno-associated virus (AAV)-mediated gene therapy have brought the possibility of commercial manufacturing of AAV vectors one step closer. To realize this prospect, a parallel effort with the goal of everincreasing sophistication for AAV vector production technology and supporting assays will be required. Among the important release assays for a clinical gene therapy product, those monitoring potentially hazardous contaminants are most critical for patient safety. A prominent contaminant in many AAV vector preparations is vector particles lacking a genome, which can substantially increase the dose of AAV capsid proteins and lead to possible unwanted immunological consequences. Current methods to determine empty particle content suffer from inconsistency, are adversely affected by contaminants, or are not applicable to all serotypes. Here we describe the development of an ion-exchange chromatography-based assay that permits the rapid separation and relative quantification of AAV8 empty and full vector particles through the application of shallow gradients and a strong anion-exchange monolith chromatography medium.
2011
S. H. Lubbad, M. R. Buchmeiser
Journal of Chromatography A, 1218 (2011) 2362-2367
Ring-opening metathesis polymerization- (ROMP) derived monoliths were prepared from 5-norborn-2-enemethyl bromide (NBE-CH2Br) and tris(5-norborn-2-enemethoxy)methylsilane ((NBE-CH2O)3SiCH3) within the confines of surface-silanized borosilicate columns (100 × 3 mm I.D.), applying Grubbs’ first generation benzylidene-type catalyst [RuCl2(PCy3)2(CHPh)]. Monoliths were converted into weak anion exchangers via reaction with diethyl amine. The resulting monolithic anion exchangers demonstrated a very good potential for the anion-exchange separation of nucleic acids applying a phosphate buffer (0.05 mol/L, pH 7) and NaCl (1.0 mol/L) as a gradient former. Fast and efficient separations, indicated by sharp and highly symmetric analyte peaks, were established. Except for the 267 and 298 base pair fragments, the eleven fragments of a ds-pUC18 DNA Hae III digest were baseline separated within ∼8 min. Nineteen fragments of a ds-pBR322 Hae III digest were separated within ∼12 min. There, only the 192 and 213 base pair fragments and the 458, 504 and 540 base pair fragments coeluted. A ds-pUC18 DNA Hae III digest was used as a control analyte in evaluating the influence of organic additives on the mobile phase such as methanol and acetonitrile on nucleic acid separation. Methanol, and even better, acetonitrile improved the separation efficiency and shortened the analysis time.
S. Yamamoto, T. Okada, M. Abe, N. Yoshimoto
Journal of Chromatography A, 1218 (2011) 2460-2466
The peak spreading of DNAs of various sizes [12-mer, 20-mer, 50-mer and 95-mer poly(T)] in linear gradient elution (LGE) chromatography with a thin monolithic disk was investigated by using our method developed for determining HETP in LGE. Electrostatic interaction-based chromatography mode (ion-exchange chromatography, IEC) was used. Polymer-based monolithic disks of two different sizes (12 mm diameter, 3 mm thickness and 0.34 mL; 5.2 mm diameter, 4.95 mm thickness and 0.105 mL) having anion-exchange groups were employed. For comparison, a 15-μm porous bead IEC column (Resource Q, 6.4 mm diameter, 30 mm height and 0.97 mL) was also used. The peak width did not change with the flow velocity for the monolithic disks where as it became wider with increasing velocity. For the monolithic disks the peak width normalized with the column bed volume was well-correlated with the distribution coefficient at the peak position KR. HETP values were constant (ca. 0.003–0.005 cm) when KR > 5. Much higher HETP values which are flow-rate dependent were obtained for the porous bead chromatography. It is possible to obtain 50–100 plates for the 3 mm monolithic disk. This results in very sharp elution peaks (standard deviation/bed volume = 0.15) even for stepwise elution chromatography, where the peak width is similar to that for LGE of a very steep gradient slope.
Z. Jiang, N. W. Smith, Z. Liu
Journal of Chromatography A, 1218 (2011) 2350-2361
Hydrophilic interaction chromatography (HILIC) has experienced increasing attention in recent years. Much research has been carried out in the area of HILIC separation mechanisms, column techniques and applications. Because of their good permeability, low resistance to mass transfer and easy preparation within capillaries, hydrophilic monolithic columns represent a trend among novel HILIC column techniques. This review attempts to present an overview of the preparation and applications of HILIC monolithic columns carried out in the past decade. The separation mechanism of various hydrophilic monolithic stationary phases is also reviewed.
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.
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.
F. Smrekar, M. Ciringer, J. Jančar, P. Raspor, A. Štrancar, A. Podgornik
Journal of Separation Science 2011, 34, 2152-2158
A process for manufacturing large quantities of lytic bacteriophages was developed. Determination of cultivation termination was found to be essential to achieve high phage quantity and purity. When optimal cultivation termination is missed, phage fraction was found to be highly contaminated with deoxyribonucleic acid released from Escherichia coli cells. Besides, an already established method for monitoring of phage cultivation based on optical density, where its peak indicates point when maximal phage titer is achieved, a new indirect chromatographic method using methacrylate monoliths is proposed for on-line estimation of phage titer. It is based on the measurement of released E. coli deoxyribonucleic acid and shows high correlation with phage titer obtained from plaque assay. Its main advantage is that the information is obtained within few minutes. In addition, the same method can also be used to determine purity of a final phage fraction. Two strategies to obtain highly pure phage fractions are proposed: an immediate purification of phage lysate using monolithic columns or an addition of EDTA before chromatographic purification. The developed protocol was shown to give phage purity above 90% and it is completed within one working day including cultivation and phage titer in the final formulation using developed chromatographic method.
C. Burden, J. Jin, A. Podgornik, D. G. Bracewell
Journal of Chromatography B, 880 (2012) 82- 89
Monoliths are an alternative stationary phase format to conventional particle based media for large biomolecules. Conventional resins suffer from limited capacities and flow rates when used for viruses, virus-like particles (VLP) and other nanoplex materials. The monolith structure provides a more open pore structure to improve accessibility for these materials and better mass transport from convective flow and reduced pressure drops. To examine the performance of this format for bioprocessing we selected the challenging capture of a VLP from clarified yeast homogenate. Using a recombinant Saccharomyces cerevisiae host it was found hydrophobic interaction based separation using a hydroxyl derivatised monolith had the best performance. The monolith was then compared to a known beaded resin method, where the dynamic binding capacity was shown to be three-fold superior for the monolith with equivalent 90% recovery of the VLP. To understand the impact of the crude feed material confocal microscopy was used to visualise lipid contaminants, deriving from the homogenised yeast. It was seen that the lipid formed a layer on top of the column, even after regeneration of the column with isopropanol, resulting in increasing pressure drops with the number of operational cycles. Removal of the lipid pre-column significantly reduces the amount and rate of this fouling process. Using Amberlite/XAD-4 beads around 70% of the lipid was removed, with a loss of VLP around 20%. Applying a reduced lipid feed versus an untreated feed further increased the dynamic binding capacity of the monolith from 0.11 mg/mL column to 0.25 mg/mL column.
L. Urbas, B. Lah Jarc, M. Barut, M. Zochowska, J. Chroboczek
Journal of Chromatography A, 1218 (2011) 2451-2459
Adenovirus type 3 dodecahedric virus-like particles (Ad3 VLP) are an interesting delivery vector. They penetrate animal cells in culture very efficiently and up to 300,000 Ad3 VLP can be observed in one cell. The purification of such particles usually consists of several steps. In these work we describe the method development and optimization for the purification of Ad3 VLP using the Convective Interaction Media analytical columns (CIMac). Results obtained with the CIMac were compared to the already established two-step purification protocol for Ad3 VLP based on sucrose density gradient ultracentifugation and the Q-Sepharose ion-exchange column. Pure, concentrated and bioactive VLP were obtained and characterized by several analytical methods. The recovery of the Ad3 VLP was more than 50% and the purified fraction was almost completely depleted of DNA; less than 1% of DNA was present. The purification protocol was shortened from five days to one day and remarkably high penetration efficacy of the CIMac-purified vector was retained. Additionally, CIMac QA analytical column has proven to be applicable for the final and in-process control of various Ad3 VLP samples.
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.
H. P. Lesch, A. Laitinen, C. Peixoto, T. Vicente, K.-E. Makkonen, L. Laitinen, J. T. Pikkarainen
Gene Therapy advance online publication, 20 January 2011
Lentivirus can be engineered to be a highly potent vector for gene therapy applications. However, generation of clinical grade vectors in enough quantities for therapeutic use is still troublesome and limits the preclinical and clinical experiments. As a first step to solve this unmet need we recently introduced a baculovirus-based production system for lentiviral vector (LV) production using adherent cells. Herein, we have adapted and optimized the production of these vectors to a suspension cell culture system using recombinant baculoviruses delivering all elements required for a safe latest generation LV preparation. High-titer LV stocks were achieved in 293T cells grown in suspension. Produced viruses were accurately characterized and the functionality was also tested in vivo. Produced viruses were compared with viruses produced by calcium phosphate transfection method in adherent cells and polyethylenimine transfection method in suspension cells. Furthermore, a scalable and cost-effective capture purification step was developed based on a diethylaminoethyl monolithic column capable of removing most of the baculoviruses from the LV pool with 65% recovery.
I. Gutierrez-Aguirrea, A. Steyer, M. Banjac, P. Kramberger, M. Poljšak-Prijatelj, M. Ravnikar
Journal of Chromatography A, 1218 (2011) 2368-2373
Rotaviruses are the leading cause of gastroenteritis in children and they exist widely in water environments. Ingestion of 10–100 viral particles is enough to initiate disease, what calls for extremely sensitive detection methods. In this study we have confirmed the validity of a recently published method for rotavirus concentration and detection based on the combination of methacrylate monoliths and real-time reverse transcription-quantitative PCR (RT-qPCR). The method was used to concentrate rotaviruses from different tap water and environmental water samples collected in Slovenia within years 2007 and 2009. The performance of virus concentration using monolithic supports was improved in comparison to the one of tangential ultrafiltration upon application of both methods on a range of environmental samples. Several samples were successfully concentrated on-site after successful adaptation of the method to field requirements. In such on-site format, the combination of concentration using CIM and detection using RT-qPCR detected as low as 30 rotavirus particles/ml, spiked in an environmental water sample.
L. Urbas, B. Košir, M. Peterka, B. Pihlar, A. Štrancar, M. Barut
Journal of Chromatography A, 1218 (2011) 2432-2437
Monoliths are chromatographic stationary phases, which were specially designed for efficient purification of large biomolecules, like proteins, viruses and DNA. In this work, the small scale monolithic butyl (C4) and styrene-divinyl benzene (SDVB) columns were applied for reversed phase analyses of various degraded influenza viruses. The binding of the HA1 subunit of haemagglutinin to the monolithic columns was confirmed by sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS-PAGE) and the Western blot. The working linear range was determined as 1.60 × 1010 viral particles/mL to at least 1.64 × 1011 viral particles/mL, the limit of detection was found to be 2.56 × 109 virus particles/mL and the limit of quantification was 5.12 × 109 virus particles/mL. The analytical HPLC method developed with the H1N1 virus was also applicable for the analytics of the HA1 subunit of H3N2 influenza virus and the influenza B virus.
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.
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.