Publications
2021
Pete Gagnon, Blaz Goricar, Nina Mencin, Timotej Zvanut, Sebastijan Peljhan, Maja Lescovec and Ales Strancar
Pharmaceutics. 2021 Jan 17;13(1):113
Abstract:
HPLC is established as a fast convenient analytical technology for characterizing the content of empty and full capsids in purified samples containing adeno-associated virus (AAV). UV-based monitoring unfortunately over-estimates the proportion of full capsids and offers little value for characterizing unpurified samples. The present study combines dual-wavelength UV monitoring with intrinsic fluorescence, extrinsic fluorescence, and light-scattering to extend the utility of HPLC for supporting development of therapeutic AAV-based drugs. Applications with anion exchange (AEC), cation exchange (CEC), and size exclusion chromatography (SEC) are presented. Intrinsic fluorescence increases sensitivity of AAV detection over UV and enables more objective estimation of empty and full capsid ratios by comparison of their respective peak areas. Light scattering enables identification of AAV capsids in complex samples, plus semiquantitative estimation of empty and full capsid ratios from relative peak areas of empty and full capsids. Extrinsic Picogreen fluorescence enables semiquantitative tracking of DNA with all HPLC methods at all stages of purification. It does not detect encapsidated DNA but reveals DNA associated principally with the exteriors of empty capsids. It also enables monitoring of host DNA contamination across chromatograms. These enhancements support many opportunities to improve characterization of raw materials and process intermediates, to accelerate process development, provide rapid in-process monitoring, and support process validation.
2020
by Maribel Rios, Aleš Štrancar, J. Michael Hatfield and Pete Gagnon
BioProcess International, 2020
Abstract:
Adenoassociated viral (AAV) vectors have become synonymous with gene therapy delivery. However, because they are produced in such small quantities and because their upstream processes carry comparatively large amounts of host-cell DNA and other impurities, AAV purification can be challenging. Several researchers have applied different chromatographic strategies, but no universal method has been adopted in the biopharmaceutical industry.
This eBook features a discussion among several industry experts that explores challenges specific to AAV purification, shedding light on whether current strategies and separation technologies are up to the task. The conversation traverses issues relating to material handling at the upstream–downstream interface, removal of host-cell DNA, chromatographic separation of empty and full capsids, and a lack of fast and robust in-process analytics for downstream processes. Participants also explore whether the rise of AAV-based treatments will require downstream scientists to shift away from the antibody-centered conceptions of chromatography that have grown alongside the biotherapeutics industry.
U. Černigoj, A. Štrancar
DNA Vaccines. Methods in Molecular Biology, vol 2197, pp 167-192
Abstract
Purification of high-quality plasmid DNA in large quantities is a crucial step in its production for therapeutic use and is usually conducted by different chromatographic techniques. Large-scale preparations require the optimization of yield and homogeneity, while maximizing removal of contaminants and preserving molecular integrity. The advantages of Convective Interaction Media® (CIM®) monolith stationary phases, including low backpressure, fast separation of macromolecules, and flow-rate-independent resolution qualified them to be used effectively in separation of plasmid DNA on laboratory as well as on large scale. A development and scale-up of plasmid DNA downstream process based on chromatographic monoliths is described and discussed below. Special emphasis is put on the introduction of process analytical technology principles and tools for optimization and control of a downstream process.
Hietala V, Horsma-Heikkinen J, Carron A, Skurnik M, Kiljunen S.
Frontiers in microbiology vol. 10 1674. 23 Jul. 2019
Abstract
The production of phages for therapeutic purposes demands fast, efficient and scalable purification procedures. Phage lysates have a wide range of impurities, of which endotoxins of gram-negative bacteria and protein toxins produced by many pathogenic bacterial species are harmful to humans. The highest allowed endotoxin concentration for parenterally applied medicines is 5 EU/kg/h. The aim of this study was to evaluate the feasibility of different purification methods in endotoxin and protein toxin removal in the production of phage preparations for clinical use. In the purification assays, we utilized three phages: Escherichia phage vB_EcoM_fHoEco02, Acinetobacter phage vB_ApiM_fHyAci03, and Staphylococcus phage vB_SauM_fRuSau02. The purification methods tested in the study were precipitation with polyethylene glycol, ultracentrifugation, ultrafiltration, anion exchange chromatography, octanol extraction, two different endotoxin removal columns, and different combinations thereof. The efficiency of the applied purification protocols was evaluated by measuring phage titer and either endotoxins or staphylococcal enterotoxins A and C (SEA and SEC, respectively) from samples taken from different purification steps. The most efficient procedure in endotoxin removal was the combination of ultrafiltration and EndoTrap HD affinity column, which was able to reduce the endotoxin-to-phage ratio of vB_EcoM_fHoEco02 lysate from 3.5 × 104 Endotoxin Units (EU)/109 plaque forming units (PFU) to 0.09 EU/109 PFU. The combination of ultrafiltration and anion exchange chromatography resulted in ratio 96 EU/109 PFU, and the addition of octanol extraction step into this procedure still reduced this ratio threefold. The other methods tested either resulted to less efficient endotoxin removal or required the use of harmful chemicals that should be avoided when producing phage preparations for medical use. Ultrafiltration with 100,000 MWCO efficiently removed enterotoxins from vB_SauM_fRuSau02 lysate (from 1.3 to 0.06 ng SEA/109 PFU), and anion exchange chromatography reduced the enterotoxin concentration below 0.25 ng/ml, the detection limit of the assay.
Keywords: antibiotic resistance, bacteriophage, phage therapy, endotoxin, enterotoxin
2019
Wang Chunlei, Mulagapati Sri Hari Raju, Chen Zhongying, Du Jing, Zhao Xiaohui, Xi Guoling, Chen Liyan, Linke Thomas, Gao Cuihua, Schmelzer Albert, Liu Dengfeng
Molecular Therapy Methods & Clinical Development, Volume 15, September 26 2019, Pages 257-263
Abstract
Adeno-associated virus (AAV) vectors are clinically proven gene delivery vehicles that are attracting an increasing amount of attention. Non-genome-containing empty AAV capsids are by-products during AAV production that have been reported to potentially impact AAV product safety and efficacy. Therefore, the presence and amount of empty AAV capsids need to be characterized during process development. Multiple methods have been reported to characterize empty AAV capsid levels, including transmission electron microscopy (TEM), analytical ultracentrifugation (AUC), charge detection mass spectrometry (CDMS), UV spectrophotometry, and measuring capsid and genome copies by ELISA and qPCR. However, these methods may lack adequate accuracy and precision or be challenging to transfer to a quality control (QC) lab due to the difficulty of implementation. In this study, we used AAV serotype 6.2 (AAV6.2) as an example to show the development of a QC-friendly anion exchange chromatography (AEX) assay for the determination of empty and full capsid percentages. The reported assay requires several microliters of material with a minimum titer of 5 × 1011 vg/mL, and it can detect the presence of as low as 2.9% empty capsids in AAV6.2 samples. Additionally, the method is easy to deploy, can be automated, and has been successfully implemented to support testing of various in-process and release samples.
Keywords: AAV, AAV6.2, Chromatography, Anion exchange chromatography (AEC), Empty capsids, AUC, High-throughput
Sofiya Fedosyuk, Thomas Merritt, Marco Polo Peralta-Alvarez, Susan J. Morris, Ada Lam, Nicolas Laroudie, Anilkumar Kangokar, Daniel Wright, George M. Warimwe, Phillip Angell-Manning, Adam J. Ritchie, Sarah C. Gilbert, Alex Xenopoulos, Anissa Boumlic, Alexander D. Douglas
Vaccine (2019).
Published online 30 April 2019.
A variety of Good Manufacturing Practice (GMP) compliant processes have been reported for production of non-replicating adenovirus vectors, but important challenges remain. There is a need for rapid production platforms for small GMP batches of non-replicating adenovirus vectors for early-phase vaccine trials, particularly in preparation for response to emerging pathogen outbreaks. Such platforms must be robust to variation in the transgene, and ideally also capable of producing adenoviruses of more than one serotype. It is also highly desirable for such processes to be readily implemented in new facilities using commercially available single-use materials, avoiding the need for development of bespoke tools or cleaning validation, and for them to be readily scalable for later-stage studies.
Here we report the development of such a process, using single-use stirred-tank bioreactors, a transgene-repressing HEK293 cell – promoter combination, and fully single-use filtration and ion exchange components. We demonstrate applicability of the process to candidate vaccines against rabies, malaria and Rift Valley fever, each based on a different adenovirus serotype.
Keywords: Simian adenovirus, GMP, Clinical trials, Single-use, Biomanufacturing, Bioreactor, Purification
Dr. Xiaotong Fu, Dr. Wei-Chiang Chen, C. Argento, R. Dickerson, P. Clarner, V. Bhatt, G. Bou-Assaf, Dr. M. Bakhshayeshi, Dr. Xiaohui Lu, Dr. S. Bergelson, Dr. J. Pieracci
Human Gene Therapy (2019)
Recombinant adeno-associated virus (rAAV)-mediated gene therapy is a fast-evolving field in the biotechnology industry. One of the major challenges in developing a purification process for AAV gene therapy is establishing an effective yet scalable method to remove empty capsids, or viral vectors lacking the therapeutic gene, from full capsids—viral product containing the therapeutic sequence. Several analytical methods that can quantify the empty-to-full capsid ratio have been reported in the literature. However, as samples can vary widely in viral titer, buffer matrix, and the relative level of empty capsids, understanding the specifications and limitations of different analytical methods is critical to providing appropriate support to facilitate process development. In this study, we developed a novel anion-exchange high-performance liquid chromatography (AEX-HPLC) assay to determine the empty-to-full capsid ratio of rAAV samples. The newly developed method demonstrated good comparability to both the transmission electron microscopy (TEM) and analytical ultracentrifugation (AUC) methods used in empty-to-full capsid ratio quantification, yet providing much higher assay throughput and reducing the minimum sample concentration requirement to 2.7E11 viral genomes (vg)/ml.
K. Trabelsi, M. Ben Zakour, H. Kallel
Vaccine (2019)
Rabies is a viral zoonosis caused by negative-stranded RNA viruses of the Lyssavirus genus. It can affect all mammals including humans. Dogs are the main source of human rabies deaths, contributing up to 99% of all rabies transmissions to humans. Vaccination against rabies is still the sole efficient way to fight against the disease.
Cell culture vaccines are recommended by World Health Organization (WHO) for pre and post exposure prophylaxis; among them Vero cell rabies vaccines which are used worldwide. In this work we studied the purification of inactivated rabies virus produced in Vero cells grown in animal component free conditions, using different methods. Cells were grown in VP-SFM medium in stirred bioreactor, then infected at an MOI of 0.05 with the LP2061 rabies virus strain. Collected harvests were purified by zonal centrifugation, and by chromatography supports, namely the Capto Core 700 and the monolithic CIM-QA column. Generated data were compared in terms of residual DNA level, host cell proteins (HCP) level and the overall recovery yield.
2018
M. Tajnik Sbaizero, M. Wolschek, M. Reiter, T. Muster, Pete Gagnon and Aleš Štrancar
BioProcess International, 15 October 2018
Influenza is a global respiratory disease with an estimated mortality of up to a half million people per year. The majority of traditional influenza vaccines are still produced in eggs. Downstream processing typically consists of clarification by centrifugation, concentration by ultrafiltration, and purification by ultracentrifugation. Recombinant vaccines are most often purified by chromatography. Chromatographic purification of viruses already has achieved major improvements in recovery and scalability, but it also is important because it enables virus purification to keep pace with important regulatory and manufacturing trends across the field of biopharmaceuticals. One of those trends is process intensification, referring to development of processes that harmonize integration of fewer and more capable steps to achieve higher productivity and reproducibility as well as reduce manufacturing costs.
In this report we describe processes for purification of influenza A and influenza B, both lacking TFF steps, and both using a single chromatography step with a cation exchange monolith on a single-use basis. The choice of process buffers enables final formulation by simple dilution of the product pool. DNA digestion requires two hours. Capture, purification, and formulation are achieved within four hours. Host-cell DNA and host-cell protein (HCP) are reduced more than 99%, and final virus recovery is 80%.
Laura M. Fischer, Michael W. Wolff, Udo Reichl, Vaccine 2017 July 17
The continuously increasing demand for potent and safe vaccines and the intensifying economic pressure on health care systems underlines the need for further optimization of vaccine manufacturing. Here, we focus on downstream processing of human influenza vaccines, investigating the purification of serum free cell culture-derived influenza virus (A/PR/8/34 H1N1) using continuous chromatography. Therefore, quaternary amine anion exchange monoliths (CIM QA) were characterized for their capacity to capture virus particles from animal cells cultivated in different media and their ability to separate virions from contaminating host cell proteins and DNA. The continuous chromatography was implemented as simulated moving bed chromatography (SMB) in a three zone open loop configuration with a detached high salt zone for regeneration.
SMBs exploiting 10% and 50% of the monoliths’ dynamic binding capacity, respectively, allowed the depletion of >98% of the DNA and >52% of the total protein. Based on the hemagglutination assay (HA assay), the virus yield was higher at 10% capacity use (89% vs. 45%). Both SMB separations resulted in a ratio of total protein to hemagglutinin antigen (based on single radial diffusion assay, SRID assay) below the required levels for manufacturing of human vaccines (less than 100 mg of protein per virus strain per dose). The level of contaminating DNA was five-times lower for the 10% loading, but still exceeded the required limit for human vaccines. A subsequent Benzonase treatment step, however, reduced the DNA contamination below 10 ng per dose. Coupled to continuous cultivations for virus propagation, the establishment of integrated processes for fully continuous production of vaccines seems to be feasible.
Miladys Limonta, Lourdes Zumalacarregui, Urska Vidic, Nika Lendero Krajnc
The main component of the Center for Genetic Engineering and Biotechnology (CIGB) candidate vaccine against Hepatitis C virus (HCV) is the pIDKE2 plasmid. The current designed downstream process for the production of pIDKE2 fulfils all regulatory requirements and renders the required quantities of pharamceutical-grade plasmid DNA (pDNA)with 95% purity. The advantages of this procedure include high plasmid purity and the elimination of undesirable additives. such as toxic organic extractants and animal-derived enzymes. However, yields and consequently the productivity of the process are low. Previous work demonstrated that the most critical step of the process is the reverse phase chromatography, where conventional porous particle resins are used. Therefore, to increase the process productivity alternative technologies such as membranes and chromatographic monoliths were tested as alternative options for this critical step. Here, a comparison between the behaviours of CIM® C4-HLD and Sartobind phenyl matrices was performed.
Attachments
2017
Alicia T Lucero, Sergio A Mercado, Anamaría C Sánchez,Carolina A Contador, Barbara A Andrews and Juan A Asenjo, Journal of chemical technology and biotechnology, (2017)
BACKGROUND: Gene therapy is a potent alternative for long-lasting inhibition of alcohol consumption. This study compares the purification of a recombinant adenoviral vector serotype 5 (rAdV5) for use in gene therapy against alcoholism using two anion-exchange methods.
RESULTS: Two anion-exchange chromatography methods using fast protein liquid chromatography were compared using a packed-bed column (Q-Sepharose™ XL) and two monolithic columns (CIM™ QA-1 and CIM™ DEAE-1). An improved and reproducible separation of recombinant adenovirus type 5 from cell lysate contaminants was achieved using the two strong anion-exchange columns in a two-step gradient chromatography. Higher adenovirus yields were achieved using the CIM QA-1 tube monolithic column at sample volumes of both 1 and 10 mL compared with the Q-Sepharose XL column. At higher flow rates, the CIM QA-1 tube monolithic column achieved better separation of the target fraction. Process recovery was improved from 28% using the Q-Sepharose XL column to 34% with the CIM QA-1 tube monolithic column quantified as vector genome. Analysis by SDS-PAGE demonstrated a purity of 70% for purified adenovirus using the CIM QA-1 tube monolithic column.
CONCLUSION: This study indicated that the use of a CIM QA-1 tube monolithic column is a better alternative than Q-Sepharose XL, and CIM DEAE-1 tube monolithic columns for the primary purification process of rAdV5 carrying the human aldehyde dehydrogenase-2 antisense gene. This purification strategy has been used as a basis to scale-up a GLP process for the production of material at the National Research Council of Canada to be used in preclinical trials of this gene therapy against alcoholism
David Vincent, Petra Kramberger, Rosana Hudej, Aleš Štrancar, Yaohe Wang,Yuhong Zhou, Ajoy Velayudhan
The purification of large viruses remains an important field of research and development. The development of efficient purification trains is limited by limited analytical methods, as well as by the complexity of large viruses, as well as the high variability in starting material from cell culture. Vaccinia virus holds great potential as an oncolytic and immunotherapeutic vaccine against a broad spectrum of cancers. In this work, monolith-based capture and polishing chromatographic steps for vaccinia virus Lister strain has been developed. Virus produced in CV-1 cells was harvested and passed through a 0.8μm pre-filter before loading onto CIEX, AIEX and HIC CIM monoliths. Without the need for nuclease treatment, up to 99% of the total DNA loaded can be removed from the vaccinia feed stream by the CIM OH monolith, which also reduces the total protein concentration in the product pool to LLOQ levels, and achieves infectious virus recoveries of 90%. Binding capacities of greater than 1x109 pfu of vaccinia per mL of matrix were obtained on both CIM SO3 and CIM OH monoliths. Multiple orthogonal analytical methods have been used to develop process knowledge and understanding.
Attachments
2016
P. Stepperta, D. Burgstallera, M. Klausbergera, E. Bergerb, P.P. Aguilara, T.A. Schneiderb, P. Krambergerc, A. Toverd, K. Nöbauere, E. Razzazi-Fazelie, A. Jungbauer, Journal of Chromatography A, 1455 (2016)
Enveloped virus-like particles (VLPs) are increasingly used as vaccines and immunotherapeutics. Frequently, very time consuming density gradient centrifugation techniques are used for purification ofVLPs. However, the progress towards optimized large-scale VLP production increased the demand for fast, cost efficient and scaleable purification processes. We developed a chromatographic procedure for purification of HIV-1 gag VLPs produced in CHOcells. The clarified and filtered cell culture supernatant was directly processed on an anion-exchange monolith. The majority of host cell impurities passed throughthe column, whereas the VLPs were eluted by a linear or step salt gradient; the major fraction of DNA waseluted prior to VLPs and particles in the range of 100–200nm in diameter could be separated into two fractions. The earlier eluted fraction was enriched with extracellular particles associated to exosomes or microvesicles, whereas the late eluting fractions contained the majority of most pure HIV-1 gag VLPs. DNA content in the exosome-containing fraction could not be reduced by Benzonase treatment which indicated that the DNA was encapsulated. Many exosome markers were identified by proteomic analysisin this fraction. We present a laboratory method that could serve as a basis for rapid downstream processing of enveloped VLPs. Up to 2000 doses, each containing 1×109 particles, could be processed witha 1mL monolith within 47 min. The method compared to density gradient centrifugation has a 220-fold improvement in productivity.
2015
J. Transfiguracion, A. P. Manceur, E. Petiot, C. M. Thompson, A. A. Kamen
Vaccine (2014)
The influenza virus continuously undergoes antigenic evolution requiring manufacturing, validation and release of new seasonal vaccine lots to match new circulating strains. Although current production processes are well established for manufacturing seasonal inactivated influenza vaccines, significant limitations have been underlined in the case of pandemic outbreaks. The World Health Organization called for a global pandemic influenza vaccine action plan including the development of new technologies. A rapid and reliable method for the quantification of influenza total particles is crucially needed to support the development, improvement and validation of novel influenza vaccine manufacturing platforms. This work presents the development of an ion exchange-high performance liquid chromatography method for the quantification of influenza virus particles. The method was developed using sucrose cushion purified influenza viruses A and B produced in HEK 293 suspension cell cultures. The virus was eluted in 1.5 M NaCl salt with 20 mM Tris–HCl and 0.01% Zwittergent at pH 8.0. It was detected by native fluorescence and the total analysis time was 13.5 min. A linear response range was established between 1 × 109 and 1 × 1011 virus particle per ml (VP/ml) with a correlation coefficient greater than 0.99. The limit of detection was between 2.07 × 108 and 4.35 × 109 whereas the limit of quantification was between 6.90 × 108 and 1.45 × 1010 VP/ml, respectively. The coefficient of variation of the intra- and inter-day precision of the method was less than 5% and 10%. HPLC data compared well with results obtained by electron microscopy, HA assay and with a virus counter, and was used to monitor virus concentrations in the supernatant obtained directly from the cell culture production vessels. The HPLC influenza virus analytical method can potentially be suitable as an in-process monitoring tool to accelerate the development of processes for the manufacturing of influenza vaccines.
A.M. Almeida, J.A. Queiroz, F. Sousa, A. Sousa
Journal of Chromatography B, 978–979 (2015) 145–150
The progress of DNA vaccines is dependent on the development of suitable chromatographic procedures to successfully purify genetic vectors, such as plasmid DNA. Human Papillomavirus is associated with the development of tumours due to the oncogenic power of E6 and E7 proteins, produced by this virus. The supercoiled HPV-16 E6/E7 plasmid-based vaccine was recently purified with the arginine monolith, with 100% of purity, but only 39% of recovery was achieved. Therefore, the present study describes the application of experimental design tools, a newly explored methodology in preparative chromatography, in order to improve the supercoiled plasmid DNA recovery with the arginine monolith, maintaining the high purity degree. In addition, the importance and influence of pH in the pDNA retention to the arginine ligand was also demonstrated. The Composite Central Face design was validated and the recovery of the target molecule was successfully improved from 39% to 83.5%, with an outstanding increase of more than double, while maintaining 100% of purity.
J-P Pirnay et al.
Pharm Res, Springer, 14 Jan 2015
The worldwide antibiotic crisis has led to a renewed interest in phage therapy. Since time immemorial phages control bacterial populations on Earth. Potent lytic phages against bacterial pathogens can be isolated from the environment or selected from a collection in a matter of days. In addition, phages have the capacity to rapidly overcome bacterial resistances, which will inevitably emerge.
To maximally exploit these advantage phages have over conventional drugs such as antibiotics, it is important that sustainable phage products are not submitted to the conventional long medicinal product development and licensing pathway. There is a need for an adapted framework, including realistic production and quality and safety requirements, that allows a timely supplying of phage therapy products for 'personalized therapy' or for public health or medical emergencies.
This paper enumerates all phage therapy product related quality and safety risks known to the authors, as well as the tests that can be performed to minimize these risks, only to the extent needed to protect the patients and to allow and advance responsible phage therapy and research.
J. Ruscic, I. Gutiérrez-Aguirre, M. Tusek Znidaric, S. Kolundzija, A. Slana, M. Barut, M. Ravnikar, M. Krajacic
Journal of Chromatography A, 1388 (2015) 69–78
The emergence of next-generation "deep" sequencing has enabled the study of virus populations with much higher resolutions. This new tool increases the possibility of observing mixed infections caused by combinations of plant viruses, which are likely to occur more frequently than previously thought. The bio-logical impact of co-infecting viruses on their host has yet to be determined and fully understood, and the first step towards reaching this goal is the separation and purification of individual species. Ion-exchange monolith chromatography has been used successfully for the purification and concentration of different viruses, and number of them have been separated from plant homogenate or bacterial and eukaryoticlysate. Thus, the question remained as to whether different virus species present in a single sample could be separated. In this study, anion-exchange chromatography using monolithic supports was optimized for fast and efficient partial purification of three model plant viruses: Turnip yellow mosaic virus, Tomato bushy stunt virus, and Tobacco mosaic virus. The virus species, as well as two virus strains, were separated from each other in a single chromatographic experiment from an artificially mixed sample. Based on A260/280 ratios, we were able to attribute specific peaks to a certain viral morphology/structure (icosa-hedral or rod-shaped). This first separation of individual viruses from an artificially prepared laboratory mixture should encourage new applications of monolithic chromatographic supports in the separation of plant, bacterial, or animal viruses from all kinds of mixed samples.
Zunyang Ke, Yu Wang and Zhongming Li
Anion-exchange chromatography is a key capture step in downstream processing plasmid DNA (pDNA). Separation of pDNA using traditional particle-based anion-exchange supports is usually slow and has a low capacity for pDNA due to steric exclusion effects. Due to convective mass transfer properties, and large flow-through channels for binding large biomolecules, monoliths have been shown to provide a fast and efficient alternative for pDNA purification. This study describes the use of monoliths for purification of a therapeutic pDNA vaccine against multidrug resistant tuberculosis (MDR TB).
Attachments
M. Zaveckas, S. Snipaitis, H. Pesliakas, J. Nainys, A. Gedvilaite
Journal of Chromatography B, 991 (2015) 21–28
Diseases associated with porcine circovirus type 2 (PCV2) infection are having a severe economic impacton swine-producing countries. The PCV2 capsid (Cap) protein expressed in eukaryotic systems self-assemble into virus-like particles (VLPs) which can serve as antigens for diagnostics or/and as vaccinecandidates. In this work, conventional adsorbents as well as a monolithic support with large pore sizeswere examined for the chromatographic purification of PCV2 Cap VLPs from clarified yeast lysate. QSepharose XL was used for the initial separation of VLPs from residual host nucleic acids and some hostcell proteins. For the further purification of PCV2 Cap VLPs, SP Sepharose XL, Heparin Sepharose CL-6Band CIMmultus SO3 monolith were tested. VLPs were not retained on SP Sepharose XL. The purity of VLPsafter chromatography on Heparin Sepharose CL-6B was only 4–7% and the recovery of VLPs was 5–7%.Using ion-exchange chromatography on the CIMmultus SO3 monolith, PCV2 Cap VLPs with the purityof about 40% were obtained. The recovery of VLPs after chromatography on the CIMmultus SO3 mono-lith was 15–18%. The self-assembly of purified PCV2 Cap protein into VLPs was confirmed by electronmicroscopy. Two-step chromatographic purification procedure of PCV2 Cap VLPs from yeast lysate wasdeveloped using Q Sepharose XL and cation-exchange CIMmultus SO3 monolith.