Publications
2011
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.
M. J. Shin, L. Tan, M. H. Jeong, J.-H. Kim, W.-S. Choe
Journal of Chromatography A, 1218 (2011) 5273-5278
Immobilized metal affinity monolith column as a new class of chromatographic support is shown to be superior to conventional particle-based column as plasmid DNA (pDNA) purification platform. By harnessing the affinity of endotoxin to copper ions in the solution, a majority of endotoxin (90%) was removed from the alkaline cell lysate using CuCl2-induced precipitation. RNA and remaining endotoxin were subsequently removed to below detection limit with minimal loss of pDNA using either monolith or particle-based column. Monolith column has the additional advantage of feed concentration and flowrate-independent dynamic binding capacity for RNA molecules, enabling purification process to be conducted at high feed RNA concentration and flowrate. The use of monolith column gives three fold increased productivity of pDNA as compared to particle-based column, providing a more rapid and economical platform for pDNA purification.
2010
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.
F. Smrekar, A. Podgornik, M. Ciringer, S. Kontrec, P. Raspor, A. Štrancar, M. Peterka
Vaccine 28 (2010) 2039–2045
Plasmid DNA (pDNA) used in vaccination and gene therapy has to be highly pure and homogenous, which point out necessity to develop efficient, reproducible and scalable downstream process. Convective Interaction Media (CIM) monolithic chromatographic supports being designed for purification of large molecules and nanoparticles seem to be a matrix of choice for pDNA purification. In present work we describe a pDNA purification process designed on two different CIM monolithic columns, based on anion-exchange (AEX) chromatography and hydrophobic interaction chromatography (HIC) chemistry. HIC monolith enabled separation of supercoiled (sc) pDNA from open circular (oc) pDNA, genomic DNA (gDNA) and endotoxins regardless to flow rates in the range at least up to 380 cm/h. Dynamic binding capacity of new HIC monolith is up to 4 mg of pDNA per milliliter of support. Combination of both chromatographic steps using optimized CaCl2 precipitation enabled production of pure pDNA, satisfying all regulatory requirements. Process was found to be reproducible, scalable, and exhibits high productivity. In addition, in-line monitoring of pDNA purification process is shown, using CIM DEAE disk monolithic columns.
N. Lendero Krajnc, F. Smrekar, A. Štrancar, A. Podgornik
Journal of Chromatography A, 1218 (2011) 2413-2424
The objective of this study was to investigate the behavior of large plasmids on the monolithic columns under binding and nonbinding conditions. The pressure drop measurements under nonbinding conditions demonstrated that the flow velocities under which plasmid passing monolith became hindered by the monolithic pore structure depended on the plasmid size as well as on the average monolith pore size; however, they were all very high exceeding the values encountered when applying CIM monolithic columns at their maximal flow rate. The impact of the ligand density and the salt concentration in loading buffer on binding capacity of the monolith for different sized plasmids was examined. For all plasmids the increase of dynamic binding capacity with the increase of salt concentration in the loading solution was observed reaching maximum of 7.1 mg/mL at 0.4 M NaCl for 21 kbp, 12.0 mg/mL at 0.4 M NaCl for 39.4 kbp and 8.4 mg/mL at 0.5 M NaCl for 62.1 kbp. Analysis of the pressure drop data measured on the monolithic column during plasmid loading revealed different patterns of plasmid binding to the surface, showing “car-parking problem” phenomena under certain conditions. In addition, layer thickness of adsorbed plasmid was estimated and at maximal dynamic binding capacity it matched calculated plasmid radius of gyration. Finally, it was found that the adsorbed plasmid layer acts similarly as the grafted layer responding to changes in solution's ionic strength as well as mobile phase flow rate and that the density of plasmid layer depends on the plasmid size and also loading conditions.
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.
2009
P. Brne, Y.-P. Lim, A. Podgornik, M. Barut, B. Pihlar, A. Štrancar
Journal of Chromatography A, 1216 (2009) 2658-2663
Convective interaction media (CIM; Sartorius BIA Separations) monoliths are attractive stationary phases for use in affinity chromatography because they enable fast affinity binding, which is a consequence of convectively enhanced mass transport. This work focuses on the development of novel CIM hydrazide (HZ) monoliths for the oriented immobilization of antibodies. Adipic acid dihydrazide (AADH) was covalently bound to CIM epoxy monoliths to gain hydrazide groups on the monolith surface. Two different antibodies were afterwards immobilized to hydrazide functionalized monolithic columns and prepared columns were tested for their selectivity. One column was further tested for the dynamic binding capacity.
J. Krenkova, A. Gargano, N. A. Lacher, J. M. Schneiderheinze, F. Švec
Journal of Chromatography A, 1216 (2009) 6824–6830
Poly(glycidyl methacrylate-co-ethylene methacrylate) monoliths have been prepared in 100 μm i.d. capillaries and their epoxy groups hydrolyzed to obtain poly(2,3-dihydroxypropyl methacrylate-co-ethylene methacrylate) matrix. These polymers were then photografted in a single step with 2-acrylamido-2-methyl-1-propanesulfonic acid and acrylic acid to afford stationary phases for a strong and a weak cation exchange chromatography, respectively. Alternatively, poly(ethylene glycol) methacrylate was used for grafting in the first step in order to enhance hydrophilicity of the support followed by photografting with 2-acrylamido-2-methyl-1-propanesulfonic acid or acrylic acid in the second step. These new columns were used for the separation of proteins and peptides. A mixture of ovalbumin, α-chymotrypsinogen, cytochrome c, ribonuclease A and lysozyme was used to assess the chromatographic performance for large molecules while a cytochrome c digest served as a model mixture of peptides. All tested columns featured excellent mass transfer as demonstrated with very steep breakthrough curves. The highest binding capacities were found for columns prepared using the two step functionalization. Columns with sulfonic acid functionalities adsorbed up to 21.5 mg/mL lysozyme while the capacity of the weak cation exchange column functionalized with acrylic acid was 29.2 mg/mL.
L. Urbas, P. Brne, B. Gabor, M. Barut, M. Strlič, T. Čerk Petrič, A. Štrancar
Joural of Chromatography A, 1216 (2009) 2689-2694
Human serum albumin (HSA) and immunoglobulin G (IgG) represent over 75% of all proteins present in human plasma. These high-abundance proteins prevent the detection of low-abundance proteins which are potential markers for various diseases. The depletion of HSA and IgG is therefore essential for further proteome analysis. In this paper we describe the optimization of conditions for selective depletion of HSA and IgG using affinity and pseudo-affinity chromatography. A Sartorius BIA Separations CIM (convective interaction media) Protein G disk was applied for the removal of IgG and the Mimetic Blue SA A6XL stationary phase for the removal of HSA. The binding and the elution buffer for CIM Protein G disk were chosen on the basis of the peak shape. The dynamic binding capacity was determined. It was shown to be dependent on the buffer system used and independent of the flow rate and of the concentration of IgG. Beside the binding capacity for the IgG standard, the binding capacity was also determined for IgG in human plasma. The Mimetic Blue SA A6XL column was characterized using human plasma. The selectivity of the depletion was dependent on the amount of human plasma that was loaded on the column. After the conditions on both supports had been optimized, the Mimetic Blue SA A6XL stationary phase was combined with the CIM Protein G disk in order to simultaneously deplete samples of human plasma. A centrifuge spin column that enables the removal of IgG and HSA from 20 μL of human plasma was designed. The results of the depletion were examined using sodium dodecyl sulfate polyacrylamide gel electrophoresis and two-dimensional gel electrophoresis.
A. Tscheliessnig, D. Ong, J. Lee, S. Pan, G. Satianegara, K. Schriebl, A. Choo, A. Jungbauer
Journal of Chromatography A, 1216 (2009) 7851–7864
A two-step purification strategy comprising of polyethylene glycol (PEG) precipitation and anion-exchange chromatography was developed for a panel of monoclonal immunoglobulin M (IgM) (pI 5.5–7.7) produced from hybridoma cultures. PEG precipitation was optimized with regards to concentration, pH and mixing. For anion-exchange chromatography, different resins were screened of which Fractogel EMD, a polymer grafted porous resin had the highest capacity. Despite its significantly slower mass transfer, the binding capacity was still higher compared to a convection driven resin (monolith). This purification strategy was successfully demonstrated for all 9 IgMs in the panel. In small scale most antibodies could be purified to >95% purity with the exception of two which gave a lower final purity (46% and 85%). The yield was dependent on the different antibodies ranging from 28% to 84%. Further improvement of recovery and purity was obtained by the digestion of DNA present in the hybridoma supernatant using an endonuclease, benzonase. So far this strategy has been applied for the purification of up to 2 l hybridoma supernatants.
K. Ralla, F. Anton, T. Scheper, C. Kasper
Journal of Chromatography A, 1216 (2009) 2671-2675
The aim of this study was to develop a chromatographic method, as a substitute for enzyme-linked immunosorbent assays, for the rapid and simultaneous detection of IgG, insulin, and transferrin present in a cell culture medium. Conjoint liquid chromatography (conjoint LC) using monolithic disks was applied for this purpose. An anion-exchange disk was combined with a Protein G affinity disk in a preparative HPLC system. IgG bound to the Protein G disk, whereas transferrin and insulin were captured on the quaternary ammonium (QA) disk. Using this method, it was possible to simultaneously determine the concentrations of IgG, transferrin, and insulin in the cell culture medium. Thus, conjoint LC could be used for the rapid and simultaneous detection of different proteins present in a cell culture medium.