Oncolytic viruses (OVs) are a class of cancer therapy that is currently undergoing clinical trials on its way to full regulatory approval. At present, the downstream processing of OVs relies on a combination of chromatography and membrane-based processes to remove process-related (e.g. host-cell proteins and nucleic acids) and product-related impurities (e.g. aggregated virus particles). This thesis explores various methods that can potentially be used to address the challenges associated with downstream processing during the production of OVs. To this end, the Rhabdoviral vector, which is currently undergoing clinical trials (phase I/II) for use in treating advanced or metastatic solid tumors, was selected as a promising oncolytic virus.
One potential improvement in the downstream process that was investigated was the use of monolithic column chromatography for Rhabdovirus purification. Two monolithic anion-exchange columns (2 and 6 µm pore size) and one hydrophobic interaction column (6 µm pore size) were used to examine how column pore size affects virus recovery and contaminant removal. This investigation ultimately inspired the development of a purification process based on monolithic hydrophobic interaction column chromatography. Furthermore, this work is also the first to investigate how additives, namely glycerol, impact the hydrophobic interaction chromatography of virus particles. The developed process could be readily implemented for the scaled-up purification of the Rhabdoviral vector.
Another challenge associated with the downstream processing of OVs is membrane fouling, which is characterized by a dramatic rise in transmembrane pressure (TMP) and low virus recovery. Indeed, membrane fouling poses a significant challenge, as some recent studies have reported that it can result in viral vector titer losses of over 80%. One critical use of membranes in downstream processing is for the sterile filtration of OVs, which is a required final step that is conducted right before vialing and involves passing the virus particles through a validated sterile filter. One of the main objectives of this thesis was to develop a fundamental understanding of the sterile filtration process and to optimize it in order to achieve higher throughput and lower losses, which are both essential to the large-scale production of OVs. To this end, a dead-end sterile filtration setup was designed, and various commercially available filters were evaluated to examine how membrane morphology affects fouling and product recovery. The results of these tests showed that double-layered composite filters enabled higher virus recovery and filtration capacity compared to single-layered sterile filters.
Another cause of membrane fouling is the aggregation of virus particles, which is mediated by various interactions in the solution. To study this, the above-described setup was re-designed to create an effective procedure that utilizes minimal volumes of virus solution, while also enabling the rapid assessment of microscale filtration performance and a comprehensive understanding of virus-virus and virus-membrane interactions. This setup was used to study how different additives, including various proteins (bovine serum albumin and α-lactalbumin) and polymers (polyethylene glycol and polyvinylpyrrolidone), affect the microfiltration of the Rhabdoviral vector and, consequently, the TMP profile. Furthermore, the correlation between the membrane fouling rate (via TMP profiles) and virus recovery was also investigated. This investigation revealed that proteins significantly increase virus transmission and that polymers are incapable of mimicking the effects of the proteins.
To explain this phenomenon, a theory based on the biophysical structure of proteins, mainly heterogenicity in charge distribution, was proposed. Moreover, membrane surface modification tests were conducted using bovine serum albumin, with the results indicating that this approach has considerable potential for enhancing virus transmission. Due to the similarities between the test setup and actual downstream processing unit operations, the results from this part of the thesis could be easily and accurately applied to process optimization. / Thesis / Candidate in Philosophy / There is considerable interest in the development of oncolytic viruses for cancer immunotherapy. Indeed, at the time of this thesis’ writing, a Canadian team of researchers is conducting the world’s first clinical trial using a combination of two viruses to kill cancer cells and stimulate an immune response. The process of manufacturing oncolytic viruses is generally divided into two major steps: upstream processing and downstream processing. While upstream processing focuses on virus propagation, downstream processing aims at removing process-related and product-related impurities. However, research into downstream process design and optimization has largely been neglected in favour of a focus on upstream processing, aimed at increasing bioreactor yields and achieving high viral titers. Consequently, downstream processing has become the main bottleneck in virus manufacturing processes, accounting for as much as 70% production costs. This thesis aims to identify and develop a fundamental understanding of the main challenges associated with the downstream processing of oncolytic viruses and to investigate methods for addressing them. Specifically, the present work focuses on the purification and final sterile filtration steps in the manufacturing of oncolytic Rhabdoviral vectors.
| Identifer | oai:union.ndltd.org:mcmaster.ca/oai:macsphere.mcmaster.ca:11375/27403 |
| Date | January 2019 |
| Creators | Shoaebargh, Shabnam |
| Contributors | Latulippe, David R., Chemical Engineering |
| Source Sets | McMaster University |
| Language | en_US |
| Detected Language | English |
| Type | Thesis |
Page generated in 0.008 seconds