Publications
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.
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.
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.
L. Hernandez, D. Stewart, L. Zumalacarregui, D. Amaro
Chinese Journal of Chromatography A, 1000-8713 (2015) 642-646
Affinity and ion exchange conventional chromatography have been used to capture erythropoietin (EPO) from mammalian cell culture supernatant. Currently, chromatographic adsorbent perfusion is available, however a limited number of applications have been found in the literature. In this work, three anion exchange chromatographic supports (gel, membrane and monolithic) were evaluated in the capture step of the recombinant erythropoietin purification process. The influences of load and flow rate on each support performance were analyzed. Also the purity of the EPO molecules was determined. A productivity analysis, as a decision tool for larger scale implementation, was done. As a conclusion, the evaluated supports are technically suitable to capture EPO with adequate recovery and good purity. However, the monolithic column admits high operating velocity, showing the highest adsorption capacity and productivity.
2014
P. Leblebici, M. E. Leblebici, F. Ferreira-da-Silva, A. E.Rodrigues, L. S. Pais
Journal of Chromatography B, 962 (2014) 89-93
Monolithic columns have attracted significant attention for the purification of large biomolecules. In the present study, a step gradient elution method was evaluated for the separation of human immunoglobulinG (hIgG) into its subclasses on CIM (convective interaction media) r-protein A (recombinant protein A)monolithic column. hIgG was loaded onto the column and bound protein was eluted with a pH gra-dient. The subclass content of the eluted fractions was analyzed by enzyme-linked immunosorbentassay (ELISA). Results showed that separation of IgG3 from the other three subclasses can be success-fully achieved with high selectivity (100%) and throughput on monolithic media. It was also revealedthat enriched fractions of IgG1 and IgG2 could be obtained from purified hIgG in a 28 min long chro-matographic run. Three fractions with high IgG1 content (89.1%, 94.3% and 88.8%) were recovered. Furthermore, IgG2 was enriched to 64% successfully. A rapid step gradient elution scheme without any additives in buffers was proven to obtain enriched preparations of the two important subclasses with high throughput. The separation time can be reduced even more by increasing the flow rate without anyloss in selectivity, which will be beneficial in industrial scale applications.
M. M. St. Amand, B. A. Ogunnaike, A.S. Robinson
Published online in Wiley Online Library, 2013
One major challenge currently facing the biopharmaceutical industry is to understand how MAb microheterogeneity affects therapeutic efficacy, potency, immunogenicity, and clearance. MAb micro-heterogeneity can result from post-translational modifications such as sialylation, galactosylation, C-terminal lysine cleavage, glycine amidation, and tryptophan oxidation, each of which can generate MAb charge variants; such heterogeneity can affect pharmacokinetics (PK) considerably. Implementation of appropriate on-line quality control strategies may help to regulate bioprocesses, thus enabling more homogenous material with desired posttranslational modifications and PK behavior. However, one major restriction to implementation of quality control strategies is the availability of techniques for obtaining on-line or at line measurements of these attributes. In this work, we describe the development of an at-line assay to separate MAb charge variants in near real-time, which could ultimately be used to implement on-line quality control strategies for MAb production. The assay consists of a 2DHPLC method with sequential in-line Protein A and WCX-10 HPLC column steps. To perform the 2D-HPLC assay at-line, the two columns steps were integrated into a single method using
a novel system configuration that allowed parallel flow over column 1 or column 2 or sequential flow from column 1 to column 2. A bioreactor system was also developed such that media samples could be removed automatically from bioreactor vessels during production and delivered
to the 2D-HPLC for analysis. With this at-line HPLC assay, we have demonstrated that MAb microheterogeneity occurs throughout the cell cycle whether the host cell line is grown under different or the same nominal culture conditions.
M. M. Segura, M. Puig, J. Piedra, S. Miravet
Adenovirus: Methods and protocols, Methods in Molecular Biology, vol. 1089
Adenovirus vectors are efficient gene delivery tools. A major caveat with vectors derived from common human adenovirus serotypes is that most adults are likely to have been exposed to the wild-type virus and exhibit active immunity against the vectors. This preexisting immunity limits their clinical success. Strategies to circumvent this problem include the use of nonhuman adenovirus vectors. Vectors derived from canine adenovirus type 2 (CAV-2) are among the best-studied representatives. CAV-2 vectors are particularly attractive for the treatment of neurodegenerative disorders. In addition, CAV-2 vectors have shown great promise as oncolytic agents in virotherapy approaches and as vectors for recombinant vaccines. The rising interest in CAV-2 vectors calls for the development of scalable GMP compliant production and purification strategies. A detailed protocol describing a complete scalable downstream processing strategy for CAV-2 vectors is reported here. Clarification of CAV-2 particles is achieved by microfiltration. CAV-2 particles are subsequently concentrated and partially purified by ultrafiltration–diafiltration. A Benzonase® digestion step is carried out between ultrafiltration and diafiltration operations to eliminate contaminating nucleic acids. Chromatography purification is accomplished in two consecutive steps. CAV-2 particles are first captured and concentrated on a propyl hydrophobic interaction chromatography column followed by a polishing step using DEAE anion exchange monoliths. Using this protocol, high-quality CAV-2 vector preparations containing low levels of contamination with empty viral capsids and other inactive vector forms are typically obtained. The complete process yield was estimated to be 38–45 %.
M.-C. Claudepierrea, et al.
Journal of Virology, February 2014
To identify novel stimulators of the innate immune system, we constructed a panel of eight HEK293-cells lines, double-positive for human Toll-like receptors (TLR) and a NF-κB-inducible reporter gene. Screening a large variety of compounds and cellular extracts detected a TLR3 activating compound in a microsomal yeast extract. Fractionation of this extract identified a RNA molecule of 4.6 kb, named Nucleic Acid Band 2 (NAB2) that was sufficient to confer the activation of TLR3. Digests with single- and double-strand-specific RNases showed the double-strand nature of this RNA, and its sequence was found to be identical to the genome of the dsRNA L-BC virus of Saccharomyces cerevisiae. A large scale production and purification process of this RNA was established based on chemical cell lysis and dsRNA-specific chromatography. NAB2 complexed with the cationic lipid Lipofectin, but neither NAB2 nor Lipofectin alone, induced the secretion of IL-12(p70), IFNα, IP-10, Mip-1β and IL-6 in human monocyte-derived dendritic cells. While NAB2 activated TLR3, Lipofectin-stabilized NAB2 signaled also via the cytoplasmic sensor for RNA recognition MDA-5. Significant increase of RMA-MUC1 tumor rejection and survival was observed in C57BL/6 mice after prophylactic vaccination with MUC1-encoding MVA and NAB2+Lipofectin. This combination of immunotherapeutics strongly increased the percentage of infiltrating Natural Killer (NK) cells and plasmacytoid dendritic cells (pDCs) at the injection sites, cell types which can modulate innate and adaptive immune responses.
M. Banjac, E. Roethl, F. Gelhart, P. Kramberger, B. Lah Jarc, M. Jarc, A. Štrancar, T. Muster, M. Peterka
Vaccine 2014
We explored the possibilities for purification of various ΔNS1 live, replication deficient influenza viruses on ion exchange methacrylate monoliths. Influenza A ΔNS1-H1N1, ΔNS1-H3N2, ΔNS1-H5N1 and ΔNS1-influenza B viruses were propagated in Vero cells and concentrated by tangential flow filtration. All four virus strains adsorbed well to CIM QA and CIM DEAE anion exchangers, with CIM QA producing higher recoveries than CIM DEAE. ΔNS1-influenza A viruses adsorbed well also to CIM SO3 cation exchanger at the same pH, while ΔNS1-influenza B virus adsorption to CIM SO3 was not complete. Dynamic binding capacity (DBC) for CIM QA, DEAE and SO3 methacrylate monoliths for influenza A ΔNS1-H1N1 virus were 1.9E+10 TCID50/ml, 1.0E+10 TCID50/ml and 8.9E+08 TCID50/ml, respectively. Purification of ΔNS1 viruses on CIM QA was scaled up and reproducibility was confirmed. Yields of infectious virus on CIM QA were between 70.8±32.3% and 87±30.8%. Total protein removal varied from 93.3±0.4% to 98.6±0.2% and host cell DNA removal efficiency was ranging from 76.4% to 99.9% and strongly depended on pretreatment with deoxyribonuclease.
2013
A. Martinčič, M. Cemazar, G. Sersa, V. Kovač, R. Milačič, J. Ščančar
Talanta 116 (2013)141-148
Conjoint liquid chromatography (CLC) on monolithic convective interaction media (CIM) disks coupled on-line to UV and inductively coupled plasma mass spectrometry (ICP-MS) detectors was used for the first time in speciation analysis of Pt in human serum spiked with Pt-based chemotherapeutics. CIM Protein G and CIM DEAE disks were assembled together in a single housing forming a CLC monolithic column. Such a set-up allows rapid two-dimensional separation by affinity and ion-exchange (IE) modes to be carried out in a single chromatographic run. By applying isocratic elution with Tris–HCl–NaHCO3 buffer (pH 7.4) in the first minute, followed by gradient elution with 1 mol L-1 NH4Cl (pH 7.4) in the next 9 min, immunoglobulins (IgG) were retained by the Protein G disk enabling subsequent separation of unbound Pt from Pt bound to transferrin (Tf) and albumin (HSA) on the CIM DEAE disk. Further elution with acetic acid (AcOH) in the next 3 min allowed separation of Pt associated with IgG. Separated Pt species were quantified by post-column isotope dilution—ICP-MS. Pt recovery on the CLC column was close to 100%. In comparison to commonly applied procedures that involve separation of protein peaks by size-exclusion chromatography (SEC) followed by IE separation of metal-based chemotherapeutic fractions bound to serum proteins, the CLC method developed is much faster and simpler. Its sensitivity (LOQs adequate for quantification of all separated Pt species, lower than 2.4 ng Pt mL-1), good selectivity and method repeatability (RSD±3%) enabled investigation of the kinetics of interaction of Pt-based chemotherapeutics with serum proteins and the distribution of Pt species in spiked human serum. Pt species present in spiked serum were bound preferentially to HSA. The proportion of Pt associated with IgG and Tf was lower than 13%. Cisplatin and especially oxaliplatin react rapidly with serum proteins, while carboplatin much less. The method developed may be reliably applied in preclinical and clinical studies of the kinetics of the interaction and distribution of different metallodrugs with proteins in blood serum.
H. G. Schwelberger, J. Feurle, F. Ahrens
Journal of Neural Transmission 120 (2013) 983-986
Diamine oxidase (DAO) was purified to homogeneity from human seminal plasma by consecutive chromatographic fractionation on heparin-sepharose, phenyl-sepharose, CIM-QA, and Superdex 200. Human seminal plasma DAO behaves electrophoretically similar to DAO proteins from other human tissues and has very similar enzymatic properties with histamine and aliphatic diamines being the preferred substrates as well as significant conversion of polyamines. The cellular source and functional importance of DAO in human semen remain to be determined.
O. Zitka, S. Skalickova, S. Krizkova, M. Vlkova, V. Adam, R. Kizek
Chromatographia (2013) 76:611-619
In this study, we optimized method for the isolation and detection of lactoferrin from human saliva using 3 mm short monolithic disc. We optimized the conditions for separation as flow rate 4 mL min-1 and ionic strength of effluent as 2 M·NaCl. We estimated limit of detection of whole method, which was hyphenated to the Bradford’s assay, down to 100 ng mL-1. The purity of the isolated fractions was verified by sodium dodecyl sulphate-polyacrylamide gel electrophoresis and recovery of isolation was found to be 51 % using minimally processed sample of saliva. Further, we tested the optimized method on group of healthy volunteers (n = 7). We were able to distinguish between the healthy subjects and subject suffering from celiac disease, which reported at least 2.5× higher level of lactoferrin in comparison to healthy ones. The results were correlated with standard enzyme-linked immunosorbent assay (ELISA) kit with obtained correlation coefficient R2 = 0.8446. Analysis of lactoferrin in saliva by monolithic disc and subsequent offline photometric detection is faster and cheaper method compared to ELISA commercial kit. The total analysis of one sample takes.
D. A. Ribeiro, D. F. Passos, H. C. Ferraz, L. R. Castilho
Journal of Chromatography B, 938 (2013) 111-118
Both recombinant and plasma-derived factor IX concentrates are used in replacement therapies for the treatment of haemophilia B. In the present work, the capture step for a recombinant FIX (rFIX) purification process was investigated. Different strong anion-exchange chromatography media (the resins Q Sepharose® FF and Fractogel® TMAE, the monolith CIM® QA and the membrane adsorber Sartobind® Q) were tested for their rFIX binding capacity under dynamic conditions. In these experiments, crude supernatant from CHO cells was used, thus in the presence of supernatant contaminants and mimicking process conditions. The highest dynamic binding capacity was obtained for the monolith, which was then further investigated. To study pseudoaffinity elution of functional rFIX with Ca2+ ions, a design of experiments to evaluate the effects of pH, NaCl and CaCl2 on yield and purification factor was carried out. The effect of pH was not statistically significant, and a combination of no NaCl and 45 mM CaCl2 yielded a good purification factor combined with a high yield of active rFIX. Under these conditions, activity yield of rFIX was higher than the mass yield, confirming selective elution of functional, γ-carboxylated rFIX. Scaling-up of this process 8 fold resulted in very similar process performance. Monitoring of the undesired activated FIX (FIXa) revealed that the FIXa/FIX ratio (1.94%) was higher in the eluate than in the loaded sample, but was still within an acceptable range. HCP and DNA clearances were high (1256 and 7182 fold, respectively), indicating that the proposed process is adequate for the intended rFIX capture step.
J. A. Martin, P. Parekh, Y. Kim, T. E. Morey, K. Sefah, N. Gravenstein, D. M. Dennis, W. Tan
PLOS ONE, March 2013, Volume 8, Issue 3, e57341
Adverse drug reactions, including severe patient bleeding, may occur following the administration of anticoagulant drugs. Bivalirudin is a synthetic anticoagulant drug sometimes employed as a substitute for heparin, a commonly used anticoagulant that can cause a condition called heparin-induced thrombocytopenia (HIT). Although bivalrudin has the advantage of not causing HIT, a major concern is lack of an antidote for this drug. In contrast, medical professionals can quickly reverse the effects of heparin using protamine. This report details the selection of an aptamer to bivalirudin that functions as an antidote in buffer. This was accomplished by immobilizing the drug on a monolithic column to partition binding sequences from nonbinding sequences using a low-pressure chromatography system and salt gradient elution. The elution profile of binding sequences was compared to that of a blank column (no drug), and fractions with a chromatographic difference were analyzed via real-time PCR (polymerase chain reaction) and used for further selection. Sequences were identified by 454 sequencing and demonstrated low micromolar dissociation constants through fluorescence anisotropy after only two rounds of selection. One aptamer, JPB5, displayed a dose-dependent reduction of the clotting time in buffer, with a 20 µM aptamer achieving a nearly complete antidote effect. This work is expected to result in a superior safety profile for bivalirudin, resulting in enhanced patient care.
P. Fernandes, C. Peixoto, VM Santiago, EJ Kremer, AS Coroadinha and PM Alves
Gene Therapy (2012), 1–8
Canine adenovirus type 2 (CAV-2) vectors overcome many of the clinical immunogenic concerns related to vectors derived from human adenoviruses (AdVs). In addition, CAV-2 vectors preferentially transduce neurons with an efficient traffic via axons to afferent regions when injected into the brain. To meet the need for preclinical and possibly clinical uses, scalable and robust production processes are required. CAV-2 vectors are currently produced in E1-transcomplementing dog kidney (DK) cells, which might raise obstacles in regulatory approval for clinical grade material production. In this study, a GMP-compliant bioprocess was developed. An MDCK-E1 cell line, developed by our group, was grown in scalable stirred tank bioreactors, using serum-free medium, and used to produce CAV-2 vectors that were afterwards purified using column chromatographic steps. Vectors producedin MDCK-E1 cells were identical to those produced in DK cells as assessed by SDS-PAGE and dynamic light scatering measurements (diameter and Zeta potential). Productivities of ~109 infectious particles (IP) ml-1 and 2x103 IP per cell were possible. A downstream process using technologies transferable to process scales was developed, yielding 63% global recovery. The total particles to IP ratio in the purified product (<20:1) was within the limits specified by the regulatory authorities for AdV vectors. These results constitute a step toward a scalable process for CAV-2 vector production compliant with clinical material specifications.
Attachments
P. Gerster, E.-M. Kopecky, N. Hammerschmidt, M. Klausberger, F. Krammer, R. Grabherr, C. Mersich, L. Urbas, P. Kramberger, T. Paril, M. Schreiner, K. Nöbauer, E. Razzazi-Fazeli, A. Jungbauer
Journal of Chromatography A, 1290 (2013) 36-45(2013) 36-45
A chromatographic process based on monoliths for purification of infective baculovirus without prior concentration step has been established. Baculovirus produced in Spodoptera frugiperda cells (Sf-9) were harvested by centrifugation, filtered through 0.8 μm filters and directly loaded onto radial 1 mL anion exchange monoliths with a channel size of 1.5–2.0 μm operated at a volumetric flow rate of one bed volume per minute. Optional an epoxy monolith was used as pre-column to reduce interfering compounds and substances influencing the capacity of anion exchange monoliths for baculovirus infectious virus could be eluted with a step gradient at salt concentrations of 440 mM NaCl. Recovery of infectious virus was highly influenced by composition and age of supernatant and ranged from 20 to >99% active baculovirus. Total protein content could be reduced to 1–8% and DNA content to 38–48% in main virus fraction. Infective virus could be 52-fold concentrated within 20.5 h and simultaneously an 82-fold volume reduction was possible when loading 1150 mL (2.1 × 108 pfu/mL) onto 1 mL scale support.
A. Steyer, I. Gutierrez-Aguire, M. Kolenc, S. Koren, D. Kutnjak, M. Pokorn, M. Poljšak-Prijatelj, N. Rački, M. Ravnikar, M. Sagadin, A. Fratnik Steyer, N. Toplak
Journal of Clinical Microbiology, November 2013
Mammalian orthoreoviruses (MRV) are known to cause mild enteric and respiratory infections in humans. They are widespread and infect a broad spectrum of mammals. We report here the first case of MRV detected in a child with acute gastroenteritis, which showed the highest similarity to MRV reported recently in European bats. Stool sample examination of the child was negative for most common viral and bacterial pathogens. Reovirus particles were identified by electron microscopic examination of both stool suspension and cell culture supernatant. The whole genome sequence was obtained with the Ion Torrent next generation sequencing platform. Prior to sequencing, stool sample suspension and cell culture supernatant were pre-treated with nucleases and/or the convective interaction media (CIM) monolithic chromatographic method to purify and concentrate the target viral nucleic acid. Whole genome sequence analysis revealed that the Slovenian SI-MRV01 isolate was most similar to MRV found in bat in Germany. High similarity was shared in all genome segments, with nucleotide and amino acid identities between 93.8-99.0% and 98.4-99.7%, respectively. It was shown that CIM monolithic chromatography alone is an efficient method for enriching the sample in viral particles before nucleic acid isolation and next generation sequencing application.
2012
H. M. Oksanen, A. Domanska, D. H. Bamford
Virology Volume 434, Issue 2, 20 December 2012
We report anion exchange chromatographic purification method powerful for preparation of virus particles with ultra pure quality. The technology is based on large pore size monolithic anion exchangers, quaternary amine (QA) and diethylaminoethyl (DEAE). These were applied to membrane-containing icosahedral bacteriophage PRD1, which bound specifically to both matrices. Virus particles eluted from the columns retained the ir infectivity, and were homogenous with high specific infectivity. The yields of infectious particles were up to 80%. Purified particles were recovered at high concentrations, approximately 5mg/ml, sufficient for virological, biochemical and structural analyses. We also tested the applicability of the monolithic anion exchange purification on a filamentous bacteriophage phi 05_2302. Monolithic ion exchange chromatography is easily scalable and can be combined with other preparative virus purification methods.
C. Scott
BioProcess International, November 2012, pg. 31-42
Monoclonal antibodies (MAbs) remain the largest segment of the biopharmaceutical market, but they are not the only recombinant proteins in development. Remember that the first biopharmaceutical approved for sale was recombinant insulin — a hormone — back in the 1980s. And proteins aren't the only recombinant biologics. The sector has expanded since then to include gene therapies and viral vectors, vaccines, and even cells and tissues. Companies around the world are developing such products for cancer, neurological, infectious disease, metabolic, autoimmune, and cardiovascular disorders, to name just the most prominent. And although MAbs are finally fulfilling their “magic bullet” promise, many other approaches are becoming available to drug developers targeting those markets — and others.
Meanwhile, funding challenges are increasing emphasis on manufacturing and development efficiencies. Even though total funding of the biotechnology industry has rebounded since the 2008 recession — from about US$13 billion for the United States industry in 2008 to about $21 billion in 2010, for example — a growing share of that money is going to the less risky investments. According to Ernst & Young's 2011 Beyond Borders report, that means mature and already-profitable companies are taking a larger portion of the financial pie.
At the same time, the average number of drug approvals per year has decreased: from about three dozen in the United States from 1996 to 2004 to under two dozen for the years since. And even though markets are opening up in China, India, and other countries, the cost of doing business on a global scale makes it no easy task to reach them. So biopharmaceutical companies need to curb the rise of development and manufacturing costs. Single-use technologies are helping with the latter in large part. And platform technologies have helped antibody makers shorten development times by starting out with certain rules of thumb — rather than trying out hundreds of available purification technologies, for example, in many different combinations to find what works best for every new product candidate.
Do nonantibody makers have similar options when it comes to their own process development work? As is so often the case in bioprocessing, the answer to that question is “It depends. ..” on the product class; on the expression system; and on the regulatory history of the company, process, and type of molecule.