This poster presents fully scalable non-affinity purification strategy that has been proven to be effective for all AAV serotype tested to date. Cell lysate is directly subjected to column purification after removal of cell debris without requiring a concentration step using tangential flow filtration. The process consists of three chromatographic steps. Hydrophobic interaction chromatography on a CIMmultus OH monolith is used for initial virus capture and purification. Precipitating salts are used at 1.0–2.0 M to achieve virus binding. Most of the small molecule contaminants and proteins are eliminated in the flow-through. AAV co-elutes with a highly reduced population of contaminating proteins. DNA-protein complexes are very strongly retained and require NaOH for removal. Intermediate polishing is performed with a CIMmultus SO3 cation exchange monolith. The AAV fraction from the capture step is titrated to a pH value of 3.5—5.0 and diluted to binding conditions. Sugars and surfactants are added to suppress non-specific interactions with tubing and containers, and the product is eluted in a salt gradient. Final polishing is conducted on a CIMmultus QA anion exchange monolith which separates empty capsids from full capsids. This is achieved in a salt gradient at alkaline pH. For more information please refer to BIA Application note A048 (www.biaseparations.com/applications).
Chromatography is a useful purification method for large biomolecules and virus manufacturing and it is easily scalable to large production volumes. Convective Interaction Media (CIM) monolithic columns constitute of large flow-through channels and consequently have high surface accessibility of binding sites. Preferences of CIM monolithic columns are flow independent performance, resulting in fast separation, concentration, purification, impurities removal, and analytics of biopharmaceuticals.
The aim of the study was to develop Influenza virus purification platform, which can be used for several virus strains. The main objective was to develop a process with as little as possible of intermediate steps, especially omitting Tangential Flow Filtration (TFF) or other sample pre-treatments with high host-cell DNA and protein removal, as well as to achieve high binding capacity of the Influenza virus per mL of monolithic support.
During recombinant adeno associated virus (rAAV) downstream processing, a large amount of host-cell and product related impurities needs to be removed from the product. Succesful process on laboratory scale, such as Cesium chloride purification, lacks scalability when the process is due to be transfered to larger industrial scale. The aim of the study was to develop robust, fast and effective rAAV virus purification platform, which can be used for several AAV serotypes with various inserts. Lysed harvest and supernatant of rAAV9 were first captured and concentrated on CIMmultus™ OH column, followed by intermediate step on CIMmultus™ SO3 column and further polishing on CIMmultus™ QA column. Derived purity of industrial scale monolith purification product was compared to laboratory scale purification.
New vaccines against Influenza A are required each year to keep up with the most virulent evolving strains. This highlights a need for predictive analytical tools that can aid purification process development and validation. Rapid and reliable quantification of Influenza A virus is therefore of the utmost importance for enabling good yields and controlling the costs of the downstream processing. Here we demonstrate the ability of monolithic chromatography media to produce process predictive profiles that can document ability to remove impurities and obtain high product recoveries.
CIMac™ Analytical Columns are short bed high performance monolithic columns offering all the advantages of CIM® monolithic technology. Their small volume and short column length allow the operation at high volumetric flow rates enabling to receive the information about the product quantity and purity in just a few minutes. Hence, the CIMac™ Analytical Columns can be effectively used for the in-process and final control of various samples from different purification process steps.
Adeno-associated virus (AAV) vectors of various serotypes are considered to have high potential for gene therapy applications. Currently, manufacturing of AAV vectors faces the challenge of co-production of incompletely formed particles lacking a recombinant viral genome. Empty capsids increase the dose of total AAV administered for efficient transduction and are thought to cause unwanted immunological reactions against the virus.Removal of empty capsids during manufacturing, as well as analysis of empty/full AAV particle content is therefore a critical requirement for any AAV production process. This poster demonstrates how CIMmultus™ QA monolithic columns can be used to remove empty AAV capsids from the product chromatographically in a single step.
Determining the concentration of viruses is a crucial step in any production process. The most commonly used methods for virus quantification are either based on the infectivity of the virus (plaque assay, TCID50) determination of their genomic material (qPCR), or protein content (SRID, ELISA) and are very cumbersome and time consuming. HPLC analytical methods represent a fast alternative to these assays since they provide information on the virus content and purity in a matter of minutes. Due to the structural properties of the monolithic supports, monolithic analytical columns offer a great advantage over particle based HPLC columns in terms of time and their ability to separate large biomolecules, like viruses, VLPs, pDNA.
In this poster the performance of the CIMac™ Adeno Analytical Column – a monolith based anion exchange column, designed for fast and reproducible analyses of adenoviruses was evaluated. CIMac Adeno column can be used for designing a fast finger printing method that is applicable for monitoring the DSP production process of adenoviruses. Once the basic analytical parameters like linearity and sensitivity are determined using a purified adenoviral standard, the metod can be applied for quantitative determination of adenoviruses.
In recent years bacteriophages were identified as a useful potential tool for different applications such as alternative to antibiotics, detection of pathogenic bacteria, delivery vehicles for protein and DNA vaccines and as gene therapy delivery vehicles. For all listed fields of use it is important that phages are highly purified with preserved biological activity. Phage and other virus purification have traditionally been carried out by CsCl2 density gradient ultracentrifugation, which is however difficult to be scaled-up. An alternative is chromatography, which already proved to be efficient for separation and purification of certain virus types. Methacrylate monoliths (CIM Convective Interaction Media® monolithic columns) were designed for purification of bionanoparticles and they already proved to be very efficient for concentration and purification of several plant and human viruses (influenza A, influenza B, adenovirus type 5, hepatitis A and others).
Our aim was to investigate whether CIM methacrylate monolithic columns can be implemented for purification of phages. Staphylococcus aureus phage VDX-10 was selected. Chromatographic support chemistry and buffer screening led to development of purification method on strong anion exchanger. Optimised single step purification method developed for S. aureus VDX-10 phage on CIM® QA monolithic column resulted in efficient removal of host cell DNA and proteins with high recovery of viable phage.
The challenge of efficient purification of gene therapy vectors
• The most commonly used gene transfer vectors are adenoviruses, lentiviruses, adeno-associated viruses, retroviruses, vaccinia viruses, and pDNA
• Due to their large size and sensitivity to pH, temperature and shear stress, purification is challenging and time-consuming
• A fast and efficient downstream processing purification method is required to isolate sufficient amounts of vectors with the final purity and state that conforms to stringent regulatory demands.
Solution: Convective Interaction Media Monoliths
• Convective interaction media (CIM) monolith chromatography
• Functionalised polydimethacrylate (QA, DEAE, OH, SO3)
• Precisely defined pore sizes
• Radial flow of solute
• Convective mass transfer
A monolith is a stationary phase made of single piece of porous material. Unlike conventional particle-shaped chromatographic supports, the pores of the monolith are interconnected and form a network of channels with diameters ranging around 1500 nm. The binding sites in these channels are highly accessible for target molecules and since the predominant mass transfer depends on convection rather than diffusion, the dynamic binding capacity is flow independent. These characteristics make the monolithic supports suitable for fast separation and purification of large biomolecules such as proteins, DNA and viruses, which sometimes exceed 200 nm in size and thus have low diffusion constants.
In this work we tried to quantify influenza A virus using an analytical CIM monolith column. First a screening of available CIM stationary phases was performed in order to establish the optimal stationary phase for the binding of the virus. The effect of the mobile phase composition and pH on the recovery and peak shape of the virus was investigated. Linearity was examined. The amount of virus in the flow-through and elution fractions was determined with the haemagglutination assay and the purity of the fractions with SDS PAGE. All experiments were performed with an inactivated Influenza A/Wisconsin PZC whole virus sample that was produced in eggs.
Recombinant Adenovirus (rAd) is commonly used for vaccination and gene transfer for cancer applications. This vector is widely used in phase I/II clinical trials. Therefore we believe that upstream and downstream processes should be improved.
We developed a production manufacturing process for rAd serotype 5 n HEK293 grown into disposable fixed-bed iCELLis™ bioreactors (ATMI LifeSciences). The purification process was reduced to one single chromatography step using the Convective Interaction Media, anion exchanger (CIM ® QA monolithic column, Bia Separations).
Briefly, rAd particles were extracted from cells using Triton X-100, depth filtered to discard cell debris, captured and purified out on CIM ® QA. The shallow gradient used for the elution of the vector allowed the separation of different rAd particles populations more or less enriched in full particles. A final step based on Tangential Flow Filtration (TFF) in hollow fibers allowed the removal of remaining impurities and the formulation of the vector batch.
In addition, we developed an analytical method on CIMac™ QA analytical column (Bia Separations) to characterize the different steps of the process, and to track the differences linked to the production runs to increase the robustness of the process. This method provided elution profiles for each step as well as titer of the purified rAd in the final step.
The rAd was produced in an iCELLis™ nano fixed-bed bioreactor (0.5-5.3 m2), purified in a 8mL CIM ® QA monolithic column, scaled up in a medium-scale size 80mL column. We are currently extending the rAd production in a 133m2 iCELLis I000™ bioreactor with a purification step using a 8L CIM® QA monolithic column to purify out up to 1x1015 vector particles.
Monolithic supports represent a new generation of chromatographic media. Due to their large inner channel diameters and enhanced mass transfer characteristics, methacrylate monoliths (CIM® monolithic columns) offer efficient and fast separation of large biomolecules like pDNA, viruses and monoclonal antibodies. High binding capacity for viral particles, good product recovery and resolution are also benefits of monoliths. During loading of MDCK cell-derived H1N1 inactivated influenza virus particles onto monolithic columns, increased back pressure is sometimes observed. This is especially an issue if a large amount of virus needs to be purified since the back pressure depends on the loading volume. The goal of this work was to determine the factors contributing to this effect. We tried to prevent the increased back pressure by treating virus harvests with different precolumn phases (LRATM - Lipid removal agent, Amberlite® XAD 7HP, epoxy monolithic column) and by filtering the virus material before loading it onto the column. To compare different pre-treatment strategies of the virus material the dynamic binding capacity of CIMac QA for virus was first determined, resulting in approximately 1x1013 virus particles per ml. Than loadings of the pre-treated virus material at 75% of the column capacity were performed and mass balances for the virus, DNA and proteins were investigated. Another goal of this work was to find a good regeneration strategy for the columns where increased back pressure occurred. For this reason different regeneration procedures using lipase, benzonase, 2-propanol and NaOH treatment were tested on the columns with increased back pressure.
Traditional waste water treatment usually does not remove or inactivate all of the potentially pathogen microorganisms present in the waste water. This is especially true for enteric viruses that are introduced into the environment through the discharge of effluent from waste water treatment plants - WWTP (Simmons et al, 2011). Although discharged concentrations of viruses are low they can still lead to infection. For some enteric viruses ingestion of only 10 - 100 virus particles is enough to initiate the disease, what calls for very sensitive detection methods. It has been previously shown that CIM-quaternary amine (QA) monolithic supports are a good tool for concentration of viruses in water (Gutierrez-Aguirre et al, 2011). Here we go one step further and evaluate CIM monoliths not just for concentration of enteric viruses but also for their removal from effluent waters.
Potato spindle tuber viroid (PSTVd) is the causal agent of a number of agriculturally important diseases. It is a single-stranded, circular and uncapsidated RNA molecule with 359 nucleotides and no coding capacity. Because of its complex secondary/tertiary structure it is very stable ex vivo and it is easily transmitted mechanically by contaminated hands, tools, machinery, etc. In this work, we describe the development and optimization of a method for concentrating PSTVd using CIM monolithic supports.
Objective – Influenza VLP
• Complex structure
• Different protein components
• Host cell derived lipid membrane
• ESAT6 epitope of M. tuberculosis engineered into influenza hemagglutinin [1,2]
• Optimal vaccine candidates
• Induce strong immune response 
• Contain no genetic information
Over the last two decades,the potential of virus-based biopharmaceuticals for application in gene therapy and vaccination brought new challenges in bioprocess development. Particularly, the downstream processing (DSP) of enveloped viruses shifted from bench-scale towards robust, scalable and cost-effective strategies to produce clinical grade viralvectors. Lenti viralvectors(LVs) hold great potential in gene therapy due to their ability to transduce non dividing cells and their capacity to sustain long-term transgene expression in several target cells, invitro and invivo1. However, despite significant progress, the quality of LV preparations, the purification and the concentration of high titers of these vectors is still cumbersome and costly. In this work, disposable membrane technologies, involving microfiltration, anion-exchange chromatography (AEXc) and a final ultrafiltration step, were the basis for the development of an optimized purification process for LV.
Over the last years, lentiviral vectors have emerged as valuable tools for transgene delivery because of their ability to transduce non-dividing cells and their capacity to sustain long-term transgene expression in target cells in vitro and in vivo. However, despite significant progress, the purification and concentration of high titer and high quality vector stocks is still time-consuming and scale-limited. We aimed to develop a simple and cost-effective capture purification step capable of separating the produced lentiviral vectors from the preparation originally containing a load of recombinant baculoviruses used to transiently transfect 293T producer cells. Even though recombinant baculoviruses do not present major safety concerns1, the final product (purified lentiviral vectors) should be pure enough to be tested in (pre-)clinical studies2. A capture step has been preliminarily evaluated. Both lentiviruses and baculoviruses are enveloped, thus per se prone to degradation through processing. Furthermore, both show overall surface negative charges at physiological pH3,4. As such, our rationale was to use an anion-exchange bind-elute step with enough resolution to separate the two viruses upon elution. It was likely that the difference in the overall electrostatic charges of the two viruses can be used to our advantage if a sufficiently extended salt elution gradient is used.
Biomanufacturing of antibodies, therapeutic proteins and vaccines or gene delivery vectors (either DNA or virus based) is a very complicated process where many things can go wrong. This is even more pronounced as the target biomolecules are extremely susceptible to the environmental conditions both during cultivation (upstream processing) as well as during isolation and purification (downstream processing). One can always doubt whether we have enough information about our complex biomolecule samples to consistently develop a safe product by running a robust and efficient purification bioprocess.
By using and understanding novel technologies one can design new process analytic technology (PAT) initiatives to overcome some of these problems. Here, we present novel monolithic analytical columns — CIMac columns — that can bridge this gap. In the first example, CIMac columns were applied for monitoring the purification process of virus like particles (VLP) which are used for production of vaccines and as delivery systems in gene therapy. In the second example, the monolithic analytical columns were also applied for monitoring the fermentation process of bacteriophages.
Avir Green Hills Biotechnology is developing innovative seasonal and pandemic influenza vaccines based on the deletion of the NS1 gene (del NS1 vaccine).The vaccine is replication-defective and applied intranasally. Recently,clinical phase I studies for H1N1 monovalent vaccine and H5N1 avian influenza vaccine were completed. Both were confirmed to be safe and immunogenic for humans. A production and purification process, which was successfully employed for the pilot-scale production of H1N1 and H5N1 influenza A vaccine virus, will be presented and compared to standard ultracentrifugation method. Details on obtained life virus yields as well as impurity removal will be given. The vaccine virus is produced in static cell culture using Vero (African Green monkey kidney) cells. After clarification the vaccine virus bulk is purified using the same(chromatography-based) scheme for all different subtypes: Concentration by tangential ultrafiltration, AEX chromatography using a CIM QA monolith, and an SEC polishing step allowing for buffer exchange. This purification scheme guarantees the thorough depletion of host cell DNA and total protein. For the ultracentrifugation approach chromatographic steps were replaced by a gradient ultracentrifugation step, comparison data are shown. In addition, an HPLC method for quantifying influenza virus in the vaccine with the use of CIM monolithic columns will be presented and the results will be compared with haemagglutination method.
Rabies virus cause acute encephalitis. It is widely distributed around the globe and more than 55,000 people perish yearly and an additional 10 million post-exposure treatment are reported. About 95% of human deaths occur in Asia and Africa. In countries that are endemic to rabies an immense need for cost-effective large-scale production of the Rabies vaccine occurs. Achieving required quality is challenging because majority of rabies vaccines are produced in Vero cells. This makes Rabies vaccine difficult to manufacture due to low titre of vaccine with lots of residual cellular DNA and serum proteins.
The objective of this work was to improve purity of rabies vaccine regarding residual DNA presence. Different mobile phases with different pH values were explored. Moreover, to develop cost-efficient downstream process for Rabies vaccine, monolith-based purification step was performed in different stages of downstream processing. Chromatographical fractions were analyzed for efficiency of DNA removal. In addition, recovery of Rabies vaccine was monitored. Finally, knowing the optimal conditions, a step-wise gradient was used for purification of larger amount of Rabies vaccine.
Adeno-associated virus (AAV) vectors continue to hold immense promise as gene transfer vehicles for a variety of gene therapy applications. Numerous pre-clinical and human clinical studies have been undertaken with rAAV, employing several of the identified serotypes to leverage their differing tissue tropism to correct a broad spectrum of genetic diseases. Despite the advantageous characteristics of rAAV and the extensive research into pre-clinical applications, production and purification scale-up continues to limit recombinant AAV (rAAV) use in large clinical trials that require even moderate vector doses. Therefore, AGTC has developed a high-yielding, scalable rAAV production system in suspension BHK cells that employs co-infection with two hybrid rHSV-rAAV vectors to provide all cis and trans-acting rAAV elements and the requisite helper virus functions for rAAV manufacturing.
In contrast to traditional, resin-based chromatography methods for rAAV purification, we have developed a two-step chromatographic process that employs a novel anion exchange Convective Interaction Media® monolithic column (CIM® monolith, BIA Separations) capture step followed by affinity chromatography (AVB Sepharose™, GE Healthcare), which yields rAAV vector stocks in very high purity. This scalable process allows significant reduction in processing time due to the high capture step dynamic binding capacity, flow rates and resolution. The resulting overall chromatography recovery compares favorably to our first and second generation processes which used three-step, resin-based column chromatography and membrane-based two step chromatography, respectively.
The CIM QA-AVB process was scaled to accommodate 10 L suspension production runs and was successful at recovering as much as 1 × 1015 purified AAV1 DRP in a single day. The process is highly reproducible and it is applicable for the purification of multiple AAV serotypes with over 95% purity and overall yield of > 30%.