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2024

Marta Leban, Tina Vodopivec Seravalli, Martina Hauer, Ernst Böhm, Nina Mencin, Sandra Potušek, Andrej Thompson, Jurij Trontelj, Aleš Štrancar & Rok Sekirnik

Analytical and Bioanalytical Chemistry, March 2024

The recent clinical success of messenger RNA (mRNA) technology in managing the Covid pandemic has triggered an unprecedented innovation in production and analytical technologies for this therapeutic modality. mRNA is produced by enzymatic transcription of plasmid DNA (pDNA) using polymerase in a cell-free process of in vitro transcription. After transcription, the pDNA is considered a process-related impurity and is removed from the mRNA product enzymatically, chromatographically, or by precipitation. Regulatory requirements are currently set at 10 ng of template pDNA per single human dose, which typically ranges between 30 and 100 µg. Here, we report the development of a generic procedure based on enzymatic digestion and chromatographic separation for the determination of residual pDNA in mRNA samples, with a limit of quantification of 2.3 ng and a limit of detection of less than 0.1 ng. The procedure is based on enzymatic degradation of mRNA and anion exchange HPLC separation, followed by quantification of residual pDNA with a chromatographic method that is already widely adopted for pDNA quality analytics. The procedure has been successfully applied for in-process monitoring of three model mRNAs and a self-amplifying RNA (saRNA) and can be considered a generic substitution for qPCR in mRNA in-process control analytical strategy, with added benefits that it is more cost-efficient, faster, and sequence agnostic.

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Klemen Božič, Ajda Sedlar, Špela Kralj, Urh Černigoj, Aleš Štrancar, Rok Sekirnik

Biotechnology and Bioengineering, 2024, 1–11

High purity of plasmid DNA (pDNA), particularly in supercoiled isoform (SC), is used for various biopharmaceutical applications, such as a transfecting agent for production of gene therapy viral vectors, for pDNA vaccines, or as a precursor for linearized form that serves as a template for mRNA synthesis. In clinical manufacturing, pDNA is commonly extracted from Escherichia coli cells with alkaline lysis followed by anion exchange chromatography or tangential flow filtration as a capture step for pDNA. Both methods remove a high degree of host cell contaminants but are unable to generically discriminate between SC and open-circular (OC) pDNA isoforms, as well as other DNA impurities, such as genomic DNA (gDNA). Hydrophobic interaction chromatography (HIC) is commonly used as polishing purification for pDNA. We developed HIC-based polishing purification methodology that is highly selective for enrichment of SC pDNA. It is generic with respect to plasmid size, scalable, and GMP compatible. The technique uses ammonium sulfate, a kosmotropic salt, at a concentration selective for SC pDNA binding to a butyl monolith column, while OC pDNA and gDNA are removed in flow-through. The approach is validated on multiple adeno-associated virus- and mRNA-encoding plasmids ranging from 3 to 12 kbp. We show good scalability to at least 300 mg of >95% SC pDNA, thus paving the way to increase the quality of genomic medicines that utilize pDNA as a key raw material.

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2023

Ivana Petrović Koshmak, Hana Jug, Katja Vrabec, Ana Mavri, Valentina Novak, Petra Dekleva, Veronika Fujs, Maja Leskovec and Aleš Štrancar

Electrophoresis 2023; 1–11

Adenoviruses are well-known viral vectors that have been previously used in gene therapy and as a vaccine-delivery vehicle for humans and animals. During the COVID-19 pandemic, it gained renewed attention, but at the same time, it raised concerns due to side effects observed with some of the resulting vaccines administered to patients. It has been indicated that these side effects might be attributed to impurities present in the final product. Therefore, constant enhancement of the vaccine purity and further improvement of impurity detection methods are needed. In this work, we showcase an example of industry-relevant adenovirus bioprocess optimization. Our data show the effect of upstream parameters on the bioburden introduced to the downstream process. We provide an example of process optimization using a combination of the PATfix analytical method, ddPCR, infectivity, total DNA, and total protein analyses to optimize cell density, multiplicity of infection, and length of production. Additionally, we provide data illustrating the robustness of the convective interaction media quaternary amine monolithic chromatography step. This anion exchange strategy was shown to remove over 99% of protein and DNA impurities, including those unable to be addressed by tangential flow filtration, while maintaining high adenovirus recoveries.

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Kaja Bažec, Mirjam Krašna, Andrej Mihevc, Maja Leskovec, Aleš Štrancar, Mojca Tajnik Sbaizero

Electrophoresis. 2023; 1–10

Adeno-associated virus (AAV) vectors are crucial tools for gene therapy applications. As AAVs are administered in vivo, stringent purity requirements must be met, necessitating the development of various downstream processing strategies in accordance with regulatory guidelines. In this context, we focus on the non-affinity serotype-independent recombinant AAV (rAAV) capture step, which involves the use of Convective Interaction Media (CIM) cation-exchange SO3 monoliths. We analyzed differentially pretreated viral samples obtained from the Sf9 cell line and applied these samples to the capture SO3 chromatography step. We conducted screening experiments using CIM SO3 0.05 mL monolithic 96-well plates with buffers of varying pH, sodium chloride concentrations, and the inclusion of poloxamer 188, aiming to select the optimal binding mobile phase. Dynamic binding capacity was defined for different pretreatments and the optimal conditions were subsequently retested using the industrial purification CIMmultus line. The results demonstrated a high overall vector recovery (51%) and a significant reduction in impurities (99.98% for protein reduction and 99.25% for DNA reduction) using the selected capture step parameters, thereby confirming the successful optimization of the rAAV capture step in the downstream process using monoliths.

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Maja Leskovec, Andrej Raspor, Veronika Fujs, Andrej Mihevc, Aleš Štrancar

Electrophoresis. 2023; 1–9

Preferential exclusion chromatography (PXC) sometimes described as hydrophobic interaction chromatography is a well-known, but not widely used technique for purification of Adeno-associated viruses. It employs high molarity of preferentially excluded cosolvent (salt in our case). The downside of this method is that high molarity of salt can lead to aggregation and precipitation of different compounds from the sample. In the case of viruses that are excreted to medium, the concentration of impurities is much lower compared to cell lysates, and PXC can be used as a first chromatographic, serotype independent step to concentrate and purify adeno-associated virus (AAV). Here, we explored PXC for adherent and suspension harvests using monolithic chromatographic columns (CIMmultus). Suspension extracellular adeno-associated virus, serotype 9 (AAV9) harvest had more impurities compared to adherent harvest, therefore it required higher input regarding method development. Final conditions for suspension harvest included higher molarity of binding salt and using more open channel format of chromatographic column (6 µm channel size). Vector genome analysis with droplet digital polymerase chain reaction (ddPCR) revealed 84% and 97% recovery for suspension and adherent AAV9 harvest, respectively. After PXC capture step, adherent AAV9 was purified by already described ion exchange techniques. Overall process vector genome recovery, from clarified harvest to anion exchange elution fraction, was 54% measured by ddPCR. Residual host cell DNA was measured at 40 ng per 1E13 vector genome, and empty AAV was below 5% in final anion exchange chromatography fraction.

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Troy Rogerson,  Guoling Xi,  Amanda Ampey,  Jon Borman,  Sally Jaroudi,  Dan Pappas,  Thomas Linke

Electrophoresis. 2023; 1– 11.

The use of viral vectors for vaccine, gene therapy, and oncolytic virotherapy applications has received increased attention in recent years. Large-scale purification of viral vector-based biotherapeutics still presents a significant technical challenge. Chromatography is the primary tool for the purification of biomolecules in the biotechnology industry; however, the majority of chromatography resins currently available have been designed for the purification of proteins. In contrast, convective interaction media monoliths are chromatographic supports that have been designed and successfully utilized for the purification of large biomolecules, including viruses, viruslike particles, and plasmids. We present a case study on the development of a purification method for recombinant Newcastle disease virus directly from clarified cell culture media using strong anion exchange monolith technology (CIMmultus QA). Resin screening studies showed at least 10 times higher dynamic binding capacity of CIMmultus QA compared to traditional anion exchange chromatography resins. Design of experiments was used to demonstrate a robust operating window for the purification of recombinant virus directly from clarified cell culture without any further pH or conductivity adjustment of the load material. The capture step was successfully scaled up from 1 mL CIMmultus QA columns to the 8 L column scale and achieved a greater than 30-fold reduction in process volume. Compared to the load material, total host cell proteins were reduced by more than 76%, and residual host cell DNA by more than 57% in the elution pool, respectively. Direct loading of clarified cell culture onto a high-capacity monolith stationary phase makes convective flow chromatography an attractive alternative to centrifugation or TFF-based virus purification procedures.

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Špela Kralj, Špela Meta Kodermac, Ines Bergoč, Tomas Kostelec, Aleš Podgornik, Aleš Štrancar, Urh Černigoj

Electrophoresis. 2023; 1– 13

Increased need for plasmid DNA (pDNA) with sizes above 10 kbp (large pDNA) in gene therapy and vaccination brings the need for its large-scale production with high purity. Chromatographic purification of large pDNA is often challenging due to low process yields and column clogging, especially using anion-exchanging columns. The goal of our investigation was to evaluate the mass balance and pDNA isoform composition at column outlet for plasmids of different sizes in combination with weak anion exchange (AEX) monolith columns of varying channel size (2, 3 and 6 µm channel size). We have proven that open circular pDNA (OC pDNA) isoform is an important driver of reduced chromatographic performance in AEX chromatography. The main reason for the behaviour is the entrapment of OC pDNA in chromatographic supports with smaller channel sizes. Entrapment of individual isoforms was characterised for porous beads and convective monolithic columns. Convective entrapment of OC pDNA isoform was confirmed on both types of stationary phases. Porous beads in addition showed a reduced recovery of supercoiled pDNA (on an 11.6 kbp plasmid) caused by diffusional entrapment within the porous structure. Use of convective AEX monoliths or membranes with channel diameter >3.5 µm has been shown to increase yields and prevent irreversible pressure build-up and column clogging during purification of plasmids at least up to 16 kbp in size.

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Nejc Pavlin, Urh Černigoj, Mojca Bavčar, Tjaša Plesničar, Jan Mavri, Martin Zidar, Matevž Bone, Urška Kralj Savič, Tadej Sever, and Aleš Štrancar

Electrophoresis. 2023; 1– 11

High-performance liquid chromatography (HPLC)-based analytical assays are used to effectively monitor purity and quantity of plasmid DNA (pDNA) throughout the purification process. However, the phenomenon of physical entrapment of open circular (OC) isoforms pDNA inside narrow channels of chromatographic support decreases its accuracy and precision and the effect increases with pDNA size. The purpose of the study was to develop a chromatographic method for accurate analytical separation between isoforms of <16 kbp pDNA using weak anion exchanging monolithic column with large (6 µm) convective channels. Purified samples of 4.7 and 15.4 kbp large pDNA with known isoform composition were prepared and their isoforms separated in ascending salt gradient. Both OC and supercoiled (SC) isoforms were baseline separated at a flow rate below 0.5 mL min−1 in a guanidinium chloride (GdnCl) gradient with a ≥95% OC pDNA elution recovery. However, these chromatographic conditions increased 2 times the peak width for linear (LIN) pDNA isoform compared to the results using monoliths with 1.4 µm channel size. If other chaotropic agents, such as urea or thiocyanate (SCN), were added to Gdn ions, the elution volume for LIN isoform decreased. Optimization of combined GdnCl/GdnSCN gradient for pDNA elution resulted in a simple and robust chromatographic method, where OC–LIN and LIN–SC pDNA (up to 15 kbp size) were separated with resolution above 1.0 and above 2.0, respectively. The accessibility and general acceptance of anion exchange chromatography for pDNA analytics give the newly developed method a great potential for in-process control monitoring of pDNA production processes.

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Lucija Rebula, Andrej Raspor, Mojca Bavčar, Aleš Štrancar and Maja Leskovec

Journal of Chromatography B, Volume 1217, 15 February 2023

Bacteriophages represent immense potential as therapeutic agents. Many of the most compelling applications of bacteriophages involve human therapy, some pertinent to gene therapy, others involving antibiotic replacement. Phages themselves are considered safe for humans. However, phage lysates may contain many kinds of harmful by-products, especially endotoxins of gram-negative bacteria and protein toxins produced by many pathogenic bacterial species. In bacteriophage research and therapy, most applications ask for highly purified phage suspensions, as such it is crucial to reduce proteins, endotoxins, DNA and other contaminants.
In this article we present an efficient two-step chromatographic purification method for P. aeruginosa bacteriophage PP-01, using Convective Interaction Media (CIM®) monoliths, that is cGMP compliant and easy to scale-up for most stringent production of the therapeutic phage. First chromatographic step on CIMmultus OH resulted in 100% bacteriophage recovery with a reduction of 98 % protein and more than 99 % DNA content. Polishing was conducted using three different column options, CIMmultus with QA, H-Bond and PrimaS ligands. For PP-01 bacteriophage all three different options worked, but multimodal ligands H-Bond and PrimaS outperformed traditional QA in endotoxin removal (7 log step reduction). Additionally, an HPLC analytical method was developed to estimate phage concentration and impurity profile in different in-process samples. The HPLC method shows good correlation with drop assay titration, provides useful insights and can be run very fast with just 20 min per sample analysis.

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Hana Jug, Natalija Hosta, Mojca Tajnik Sbaizero, Aleš Štrancar, Daniela Brodesser, Bianca Tisch, Theresa Heger, Markus Wolschek, Joachim Seipelt and Manfred Reiter

BioProcess International, 9 February 2023

Newcastle disease is an extremely infectious condition among domesticated poultry and other avian species. Its high morbidity and mortality rates among infected birds give the disease significant economic importance. Thus, many commercially available vaccines based on live or inactivated virions are used globally to protect against Newcastle disease infection.
The causative agent is Newcastle disease virus (NDV), which belongs to the Paramyxoviridae family. NDV is a single-stranded, negative sense, enveloped RNA virus of avian origin that is highly attenuated in humans and other primates because of strong host-range restriction. Attenuated NDV has been evaluated as a vector for vaccines against SARS-CoV-2, Ebola, H5N1 influenza, West Nile, and simian immunodeficiency viruses. Oncolytic NDV vectors also hold much promise for immunotherapies against various cancers.
Whether for vaccines or viral-vector therapies, NDV particles must meet certain criteria for yield, purity, and concentration. Previously, we have described a highly effective process for purification of influenza virus produced in Vero cells. Based on CIMmultus SO3 (sulfonate) monolith columns, the process yielded excellent recovery and impurity removal and enabled good manufacturing practice (GMP) scale-up to produce clinical-grade material. Here, we describe our adaptation of the process to NDV purification and thus demonstrate the broad applicability of SO3 monolith technology.

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2022

Rok Žigon, Mojca Tajnik Sbaizero, Ivana Petrović Koshmak, Veronika Fujs, Maja Leskovec & Aleš Štrancar

Cell & Gene Therapy Insights 2022; 8(10), 1315–1328

Manufacture and purification of recombinant adeno-associated viruses (rAAV) require development and optimization of processes to ensure the best possible quality of the final rAAV product. To do so, different strategies in upstream can be used to achieve the highest possible viral titer and lowest amount of impurities, both of which further influence downstream. Second challenge involves removal of cell debris where different pre-treatments can be utilized. In the next step, optimized capture of rAAV on a cation-exchange chromatography should be developed to remove impurities and achieve a high recovery of rAAV. In the end, several chromatographic options are available to remove empty and defected capsids, so only functional viruses can be isolated. Here, the process of manufacturing and purification of rAAV has been designed using monolithic columns to achieve this important goal of preparing rAAV for the use in gene therapy.

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2021

by Nejc Pavlin, Blaž Bakalar, Janja Skok, Špela Kralj, Andreja Gramc Livk, and Aleš Štrancar

BioProcess International, October 2021

Abstract:

Plasmid DNA (pDNA) has become a crucial component in the production of next generation therapeutics such as messenger RNA (mRNA) and viral vectors.

As companies ramp up their production capabilities and move towards clinical applications, obtaining cGMP grade pDNA has become a production bottleneck, leading to lengthy production delays.

There is a growing market demand for solutions that can streamline the production of cGMP pDNA and help optimize down-stream processes (DSP) for better yields & purity.

The key step in this process is having quantifiably reliable analytics that give rapid results
for process optimization and scale-up, as well as production runs.

Establishing and expanding inhouse pDNA production platform in a quick and efficient manner will be a key differentiator between more and less successful next generation therapeutics projects.

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Pete Gagnon, Blaž Goričar, Sara Drmota Prebil, Hana Jug, Maja Leskovec, Aleš Štrancar

BioProcess J, 2021; 20

Abstract:

Separation of empty and full AAV8 capsids was achieved during their elution from a weak anion exchanger with an ascending pH gradient at low conductivity. Experimental data suggest elution was mediated by loss of positive charge from the exchanger. The method produced a full capsid peak with fewer empty capsids than elution of a strong anion exchanger with a salt gradient. Elution of the weak exchanger by sodium chloride gradients or by pH gradients in the presence of sodium chloride gave inferior separation performance. Pre-elution of empty capsids with a pH step allowed full capsids to be eluted by salt without compromising separation. Loading at intermediate pH prevented empty capsid binding and enabled step elution of full capsids in a physiological buffer environment.

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Nerea Zabaleta, Wenlong Dai, Urja Bhatt, Cécile Hérate, Pauline Maisonnasse, Jessica A. Chichester, Julio Sanmiguel, Reynette Estelien, Kristofer T. Michalson, Cheikh Diop, Dawid Maciorowski, Nathalie Dereuddre Bosquet, Mariangela Cavarelli, Anne-Sophie Gallouët, Thibaut Naninck, Nidhal Kahlaoui, Julien Lemaitre, Wenbin Qi, Elissa Hudspeth, Allison Cucalon, Cecilia D. Dyer, M. Betina Pampena, James J. Knox, Regina C. LaRocque, Richelle C. Charles, Dan Li, Maya Kim, Abigail Sheridan, Nadia Storm, Rebecca I. Johnson, Jared Feldman, Blake M. Hauser, Vanessa Contreras, Romain Marlin, Raphaël Ho Tsong Fang, Catherine Chapon, Sylvie van der Werf, Eric Zinn, Aisling Ryan, Dione T. Kobayashi, Ruchi Chauhan, Marion McGlynn, Edward T. Ryan, Aaron G. Schmidt, Brian Price, Anna Honko, Anthony Griffiths, Sam Yaghmour, Robert Hodge, Michael R. Betts, Mason W. Freeman, James M. Wilson, Roger Le Grand, Luk H. Vandenberghe

Cell Host & Microbe, Volume 29, Issue 9, 2021, Pages 1437-1453

Abstract:

The SARS-CoV-2 pandemic has affected more than 185 million people worldwide resulting in over 4 million deaths. To contain the pandemic, there is a continued need for safe vaccines that provide durable protection at low and scalable doses and can be deployed easily. Here, AAVCOVID-1, an adeno-associated viral (AAV), spike-gene-based vaccine candidate demonstrates potent immunogenicity in mouse and non-human primates following a single injection and confers complete protection from SARS-CoV-2 challenge in macaques. The AAVCOVID vector has no relevant pre-existing immunity in humans and does not elicit cross-reactivity to common AAVs used in gene therapy. Vector genome persistence and expression wanes following injection. The single low-dose requirement, high-yield manufacturability, and 1-month stability for storage at room temperature may make this technology well suited to support effective immunization campaigns for emerging pathogens on a global scale.

In this study, the AAVCOVID candidates were produced at larger scale via standard AAV production processes by Novartis Gene Therapies, following their stablished protocol with only minimal modifications to adjust to the AAVrh32.33 technology. Briefly, AC1 and AC3 were produced via three plasmid transfection. After cell lysis and lysate clarification, tangential flow filtration (TFF) was conducted to achieve volume reduction. The TFF retentate was next enriched for AAV particles on a cation exchange chromatography column (Sartorius BIA Separations). The eluate was concentrated, and buffer exchanged through an additional TFF step, before CsCl ultracentrifugation to separate genome containing versus empty AAV particles. Finally, formulation was achieved through TFF before bulk drug substance was filtered.

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Urh Černigoj, Jana Vidič, Ana Ferjančič, Urša Sinur, Klemen Božič, Nina Mencin, Anže Martinčič Celjar, Pete Gagnon, Aleš Štrancar

Electrophoresis, September 2021. https://doi.org/10.1002/elps.202100210

Abstract:

Elution of strong and weak anion exchangers with sodium chloride gradients is commonly employed for analysis of sample mixtures containing different isomers of plasmid DNA. Gradient elution of a weak anion exchanger (diethylaminoethyl, DEAE) in the presence of guanidine hydrochloride (Gdn) roughly doubles resolution between open-circular (oc) and supercoiled (sc) isomers. It also improves resolution among sc, linear, and multimeric/aggregated forms. Sharper elution peaks with less tailing increase sensitivity about 30%. However, elution with an exclusively-Gdn gradient to 900 mM causes more than 10% loss of plasmid. Elution with a sodium chloride gradient while maintaining Gdn at a level concentration of 300 mM achieves close to 100% recovery of sc plasmid while maintaining the separation improvements achieved by exclusively-Gdn elution. Corresponding improvements in separation performance are not observed on a strong (quaternary amine) anion exchanger. Other chaotropic salts do not produce a favorable result on either exchanger, nor does the inclusion of surfactants or EDTA. Selectivity of the DEAE-Gdn method is orthogonal to electrophoresis, but with better quantification than agarose electrophoresis, better quantitative accuracy than capillary electrophoresis, and resolution approaching capillary electrophoresis.

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Rafael G. Ferreira, Neal F. Gordon, Rick Stock, Demetri Petrides

Processes 2021, 9(8), 1430

Abstract:

The COVID-19 pandemic has motivated the rapid development of numerous vaccines that have proven effective against SARS-CoV-2. Several of these successful vaccines are based on the adenoviral vector platform. The mass manufacturing of these vaccines poses great challenges, especially in the context of a pandemic where extremely large quantities must be produced quickly at an affordable cost. In this work, two baseline processes for the production of a COVID-19 adenoviral vector vaccine, B1 and P1, were designed, simulated and economically evaluated with the aid of the software SuperPro Designer.

In the purification process the retentate from the ultrafiltration step was subjected to anion-exchange chromatography (AEX), operating in capture mode, to remove protein and DNA impurities. A strong anion-exchange column with a monolithic structure (CIMmultus QA from Sartorius BIA Separations) is used in this step due to its high binding capacity for VPs.

Both processes were sized to produce 400 M/yr vaccine doses. The media and facility-dependent expenses were found to be the main contributors to the operating cost. The results indicate that adenoviral vector vaccines can be practically manufactured at large scale and low cost.

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Pete Gagnon, Maja Leskovec, Sara Drmota Prebil, Rok Žigon, Maja Štokelj, Andrej Raspor, Sebastijan Peljhan, Ales Štrancar

Journal of Chromatography A, 2021

Abstract:

Separation of empty and full adeno-associated virus capsids by multimodal metal affinity chromatography was investigated using a positively charged metal affinity ligand. A subpopulation of empty capsids eluted first, followed by full capsids, and later by more empty capsids and debris. Empty and full capsid composition of chromatography fractions was evaluated by cesium chloride density gradient centrifugation followed by stratigraphic flow analysis of the centrifuge tube contents, monitored by intrinsic fluorescence. Columns charged with barium, calcium, magnesium, zinc, manganese, and ferric ions gave similar results with respect to capsid separation. Charging with cupric ions maintained resolution between early-eluting empty capsids and full capsids but caused them to elute at lower conductivity. Empty and full capsids were fractionated with Tris-borate gradients, sodium chloride gradients, and magnesium chloride gradients. Recovery of full serotype 9 capsids was 100% with complete elimination of empty capsids. All metal ions bound contaminant subsets that required sodium hydroxide for removal. Columns charged with ferric iron and manganese bound more contaminants than all other metals. Columns charged with calcium, magnesium, barium, and copper bound the least. Contaminant binding on zinc-charged columns was intermediate between the two groups.

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Michael Winkler, Mikhail Goldfarb, Shaojie Weng, Jeff Smith, Susan Wexelblat, John Li, Alejandro Becerra, Sandra Bezemer, Kevin Sleijpen, Aleš Štrancar, Sara Primec, Romina Zabar, April Schubert, Akunna Iheanacho, and David Cetlin

BioProcess International, April 2021

Abstract

Over the past decade, adenoassociated virus (AAV) vectors have become established as leading gene-delivery vehicles. In 2017, the pipeline for gene therapies included 351 drugs in clinical trials and 316 in preclinical development. As those candidates advance, significant efforts are being made in process development and manufacturing for viral vectors, with the overall goal of reducing process impurities while maintaining the highest possible process yield.

Sartorius BIA Separations has developed and commercialized CIMmultus QA monoliths, which have been cited in several AAV downstream processes for their ability to separate empty and full virus particles effectively. Monolithic supports represent a unique type of stationary phase for liquid chromatography, bioconversion, and solid-phase synthesis. Aside from increased processing speed, monolithic flow-through pores (channels) also provide easy access for large molecules, which supports both purification and depletion of nanoparticles such as plasmid DNA (pDNA) molecules and AAV particles.

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Sebastijan Peljhan, Maja Štokelj, Sara Drmota Prebil, Pete Gagnon and Aleš Štrancar

Cell & Gene Therapy Insights, March 2021

Abstract:

Ultracentrifugation (UC) is a well-known technique for fractionating adeno-associated virus (AAV) capsids according to their density, which is mainly a function of their encapsidated DNA mass. Empty capsids represent the lowest density subpopulation. Full capsids represent the highest density subpopulation, sometimes accompanied by partially full capsids of intermediate density. Fractions can be collected after sedimentation for analysis but the practice is laborious and discourages application of multiple monitoring techniques that might provide deeper insights into sample composition. Anion exchange chromatography (AEC) also achieves fractionation of empty and full capsids for many AAV serotypes. The degree of separation varies among serotypes and does not correlate strictly with UC. This is not surprising since separation by AEC is highly influenced by capsid surface charge, which is independent of the amount of DNA packaged within the capsids. Chromatography methods however present a significant analytical advantage in the ease of monitoring the column effluent, including with multiple detectors. UV absorbance at 260 nm and 280 nm permits estimation of empty and full capsid proportions in any given peak. Intrinsic fluorescence enables estimation of relative areas of empty capsid peaks and full capsid peaks. Light scattering does the same and permits the further determination of capsid size and mass. In this report, we merge UC with an HPLC monitoring array to simultaneously analyze dual wavelength UV, intrinsic fluorescence, and light scattering through cesium chloride density gradient strata. Limitations of each monitoring method are discussed. UC results are compared with chromatography profiles to highlight distinction between separation methods. Practical application of results for final product characterization is considered, along with potential to support development of better purification processes.

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Pete Gagnon, Maja Leskovec, Blaz Goricar, and Aleš Štrancar

BPI, December 17, 2020

Abstract:

With its first licensed therapeutic now marketed worldwide, adeno-associated virus (AAV) has become a preferred vector for gene therapy. However, unlocking its full potential still poses challenges, many of which are associated with purification. The first involves the transition from upstream to downstream processes. AAV-bearing lysates are laden with debris that foul filtration media and limit or prevent concentration. Another challenge involves reduction of soluble host-cell DNA, which is complicated by its strong association with nucleoproteins. A third involves elimination of empty capsids. Currently, ultracentrifugation meets that need, but scale-up issues make chromatographic alternatives attractive. A fourth challenge involves the need for rapid, accurate, and revealing analytical results to guide process development, support validation, document control, and enable reproducibility of manufacturing processes. The following article shares experimental data showing how those challenges can be addressed to advance the evolution of gene therapy with AAV.

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