A scalable insect cell-based production process of the human recombinant BMX for in-vitro covalent ligand high-throughput screening.

Bone Marrow Tyrosine kinase in the chromosome X (BMX) is a TEC family kinase associated with numerous pathological pathways in cancer cells. Covalent inhibition of BMX activity holds promise as a therapeutic approach against cancer. To screen for potent and selective covalent BMX inhibitors, large quantities of highly pure BMX are normally required which is challenging with the currently available production and purification processes. Here, we developed a scalable production process for the human recombinant BMX (hrBMX) using the insect cell-baculovirus expression vector system. Comparable expression levels were obtained in small-scale shake flasks (13 mL) and in stirred-tank bioreactors (STB, 5 L). A two-step chromatographic-based process was implemented, reducing purification times by 75% when compared to traditional processes, while maintaining hrBMX stability. The final production yield was 24 mg of purified hrBMX per litter of cell culture, with a purity of > 99%. Product quality was assessed and confirmed through a series of biochemical and biophysical assays, including circular dichroism and dynamic light scattering. Overall, the platform herein developed was capable of generating 100 mg purified hrBMX from 5 L STB in just 34 days, thus having the potential to assist in-vitro covalent ligand high-throughput screening for BMX activity inhibition.

Establishing Suspension Cell Cultures for Improved Manufacturing of Oncolytic Adenovirus.

Recent clinical trials have shown the potential of oncolytic adenoviruses as a cancer immunotherapy. A successful transition of oncolytic adenovirus to clinical applications requires efficient and good manufacturing practice compatible production and purification bioprocesses. Suspension cultures are preferable for virus production as they can reduce process costs and increase product quality and consistency. This work describes the adaptation of the A549 cell line to suspension culture in serum-reduced medium validated by oncolytic adenovirus production in stirred tank bioreactor. Cell concentrations up to 3 × 106 cells mL-1 are obtained during the production process. At harvest 1.4 × 1010 infectious particles mL-1 and 6.9 ± 1.1 × 1010 viral genome mL-1 are obtained corresponding to a viral genome: infectious particles ratio of 5.2 (± 1.9): 1 confirming the virus quality. Overall, the suspension characteristics of these A549 cells support an easily scalable, less time-consuming, and more cost-effective process for expanded success in the use of oncolytic viruses for cancer therapy.

Structural and biophysical insights into the mode of covalent binding of rationally designed potent BMX inhibitors.

The bone marrow tyrosine kinase in chromosome X (BMX) is pursued as a drug target because of its role in various pathophysiological processes. We designed BMX covalent inhibitors with single-digit nanomolar potency with unexploited topological pharmacophore patterns. Importantly, we reveal the first X-ray crystal structure of covalently inhibited BMX at Cys496, which displays key interactions with Lys445, responsible for hampering ATP catalysis and the DFG-out-like motif, typical of an inactive conformation. Molecular dynamic simulations also showed this interaction for two ligand/BMX complexes. Kinome selectivity profiling showed that the most potent compound is the strongest binder, displays intracellular target engagement in BMX-transfected cells with two-digit nanomolar inhibitory potency, and leads to BMX degradation PC3 in cells. The new inhibitors displayed anti-proliferative effects in androgen-receptor positive prostate cancer cells that where further increased when combined with known inhibitors of related signaling pathways, such as PI3K, AKT and Androgen Receptor. We expect these findings to guide development of new selective BMX therapeutic approaches.

Production of oncolytic adenovirus and human mesenchymal stem cells in a single-use, Vertical-Wheel bioreactor system: Impact of bioreactor design on performance of microcarrier-based cell culture processes.

Anchorage-dependent cell cultures are used for the production of viruses, viral vectors, and vaccines, as well as for various cell therapies and tissue engineering applications. Most of these applications currently rely on planar technologies for the generation of biological products. However, as new cell therapy product candidates move from clinical trials towards potential commercialization, planar platforms have proven to be inadequate to meet large-scale manufacturing demand. Therefore, a new scalable platform for culturing anchorage-dependent cells at high cell volumetric concentrations is urgently needed. One promising solution is to grow cells on microcarriers suspended in single-use bioreactors. Toward this goal, a novel bioreactor system utilizing an innovative Vertical-Wheel™ technology was evaluated for its potential to support scalable cell culture process development. Two anchorage-dependent human cell types were used: human lung carcinoma cells (A549 cell line) and human bone marrow-derived mesenchymal stem cells (hMSC). Key hydrodynamic parameters such as power input, mixing time, Kolmogorov length scale, and shear stress were estimated. The performance of Vertical-Wheel bioreactors (PBS-VW) was then evaluated for A549 cell growth and oncolytic adenovirus type 5 production as well as for hMSC expansion. Regarding the first cell model, higher cell growth and number of infectious viruses per cell were achieved when compared with stirred tank (ST) bioreactors. For the hMSC model, although higher percentages of proliferative cells could be reached in the PBS-VW compared with ST bioreactors, no significant differences in the cell volumetric concentration and expansion factor were observed. Noteworthy, the hMSC population generated in the PBS-VW showed a significantly lower percentage of apoptotic cells as well as reduced levels of HLA-DR positive cells. Overall, these results showed that process transfer from ST bioreactor to PBS-VW, and scale-up was successfully carried out for two different microcarrier-based cell cultures. Ultimately, the data herein generated demonstrate the potential of Vertical-Wheel bioreactors as a new scalable biomanufacturing platform for microcarrier-based cell cultures of complex biopharmaceuticals.

Human amniocyte-derived cells are a promising cell host for adenoviral vector production under serum-free conditions.

Recombinant adenovirus vectors (AdVs) have been used for the development of vaccines, as gene therapy vectors and for protein production. Currently, the production of clinical grade batches of recombinant E1-deleted adenovirus type 5 vectors is performed using human-derived HEK293 or PER.C6(®) cell lines. In this work we describe the generation of a new human amniocyte-derived cell line named 1G3 and show that it can be used as a very promising cell host for AdV production in serum-free conditions, allowing for production in high cell density cultures and avoiding the typical cell density effect observed for HEK293. By design, this cell line makes the generation of replication-competent adenovirus during production of E1-deleted AdVs very unlikely. The impact of the culture system (static versus agitated) and AdV infection parameters such as multiplicity of infection, time of harvesting and cell concentration at infection were evaluated and compared with HEK293. Using stirred tanks bioreactors, it was possible to grow 1G3 cells to cell densities of up to 9 × 10(6) cells/mL using serum-free media. Moreover, without a medium exchange step at infection, a three-fold increase in AdV volumetric titers was obtained, as no cell density effect was observed at CCI 3. Overall, our results clearly demonstrate the potential of the human amniocyte-derived newly established cell line 1G3 for AdV production in a serum-free scalable process, paving the way for further process improvements based on fed-batch or perfusion strategies.

Exploring continuous and integrated strategies for the up- and downstream processing of human mesenchymal stem cells.

The integration of up- and downstream unit operations can result in the elimination of hold steps, thus decreasing the footprint, and ultimately can create robust closed system operations. This type of design is desirable for the bioprocess of human mesenchymal stem cells (hMSC), where high numbers of pure cells, at low volumes, need to be delivered for therapy applications. This study reports a proof of concept of the integration of a continuous perfusion culture in bioreactors with a tangential flow filtration (TFF) system for the concentration and washing of hMSC. Moreover, we have also explored a continuous alternative for concentrating hMSC. Results show that expanding cells in a continuous perfusion operation mode provided a higher expansion ratio, and led to a shift in cells' metabolism. TFF operated either in continuous or discontinuous allowed to concentrate cells, with high cell recovery (>80%) and viability (>95%); furthermore, continuous TFF permitted to operate longer with higher cell concentrations. Continuous diafiltration led to higher protein clearance (98%) with lower cell death, when comparing to discontinuous diafiltration. Overall, an integrated process allowed for a shorter process time, recovering 70% of viable hMSC (>95%), with no changes in terms of morphology, immunophenotype, proliferation capacity and multipotent differentiation potential.

Scalable production of adenovirus vectors.

Recombinant adenoviruses (AdV) are highly efficient at gene transfer for a broad spectrum of cell types and species. They became one of the vectors of choice for gene delivery and expression of foreign proteins in gene therapy and vaccination purposes. To meet the need of significant amounts of adenoviral vectors for preclinical and possibly clinical uses, scalable and reproducible production processes are required.In this chapter, we review processes used for scalable production of two types of first generation (E1-deleted) adenoviral vectors (Human and Canine) using stirred tank bioreactors. The production of adenovirus vectors using either suspension (HEK 293) or anchorage-dependent cells (MDCK-E1) are described to exemplify scalable production processes with different cell-culture types. The downstream processes will be covered in the next chapter.

Carbon monoxide modulates apoptosis by reinforcing oxidative metabolism in astrocytes: role of Bcl-2.

Modulation of cerebral cell metabolism for improving the outcome of hypoxia-ischemia and reperfusion is a strategy yet to be explored. Because carbon monoxide (CO) is known to prevent cerebral cell death; herein the role of CO in the modulation of astrocytic metabolism, in particular, at the level of mitochondria was investigated. Low concentrations of CO partially inhibited oxidative stress-induced apoptosis in astrocytes, by preventing caspase-3 activation, mitochondrial potential depolarization, and plasmatic membrane permeability. CO exposure enhanced intracellular ATP generation, which was accompanied by an increase on specific oxygen consumption, a decrease on lactate production, and a reduction of glucose use, indicating an improvement of oxidative phosphorylation. Accordingly, CO increased cytochrome c oxidase (COX) enzymatic specific activity and stimulated mitochondrial biogenesis. In astrocytes, COX interacts with Bcl-2, which was verified by immunoprecipitation; this interaction is superior after 24 h of CO treatment. Furthermore, CO enhanced Bcl-2 expression in astrocytes. By silencing Bcl-2 expression with siRNA transfection, CO effects in astrocytes were prevented, namely: (i) inhibition of apoptosis, (ii) increase on ATP generation, (iii) stimulation of COX activity, and (iv) mitochondrial biogenesis. Thus, Bcl-2 expression is crucial for CO modulation of oxidative metabolism and for conferring cytoprotection. In conclusion, CO protects astrocytes against oxidative stress-induced apoptosis by improving metabolism functioning, particularly mitochondrial oxidative phosphorylation.

Metabolic alterations induced by ischemia in primary cultures of astrocytes: merging 13C NMR spectroscopy and metabolic flux analysis.

Disruption of brain energy metabolism is the hallmark of cerebral ischemia, a major cause of death worldwide. Astrocytes play a key role in the regulation of brain metabolism and their vulnerability to ischemia has been described. Aiming to quantify the effects of an ischemic insult in astrocytic metabolism, primary cultures of astrocytes were subjected to 5 h of oxygen and glucose deprivation in a bioreactor. Flux distributions, before and after ischemia, were estimated by metabolic flux analysis using isotopic information and the consumption/secretion rates of relevant extracellular metabolites as constraints. During ischemia and early recovery, 30% of cell death was observed; several metabolic alterations were also identified reflecting a metabolic response by the surviving cells. In the early recovery ( approximately 10 h), astrocytes up-regulated glucose utilization by 30% and increased the pentose phosphate pathway and tricarboxylic acid cycle fluxes by three and twofold, respectively. Additionally, a two to fivefold enhancement in branched-chain amino acids catabolism suggested the importance of anaplerotic molecules to the fast recovery of the energetic state, which was corroborated by measured cellular ATP levels. Glycolytic metabolism was predominant in the late recovery. In summary, this work demonstrates that changes in fluxes of key metabolic pathways are implicated in the recovery from ischemia in astrocytes.

Integrating human stem cell expansion and neuronal differentiation in bioreactors.

BACKGROUND: Human stem cells are cellular resources with outstanding potential for cell therapy. However, for the fulfillment of this application, major challenges remain to be met. Of paramount importance is the development of robust systems for in vitro stem cell expansion and differentiation. In this work, we successfully developed an efficient scalable bioprocess for the fast production of human neurons. RESULTS: The expansion of undifferentiated human embryonal carcinoma stem cells (NTera2/cl.D1 cell line) as 3D-aggregates was firstly optimized in spinner vessel. The media exchange operation mode with an inoculum concentration of 4 x 10(5) cell/mL was the most efficient strategy tested, with a 4.6-fold increase in cell concentration achieved in 5 days. These results were validated in a bioreactor where similar profile and metabolic performance were obtained. Furthermore, characterization of the expanded population by immunofluorescence microscopy and flow cytometry showed that NT2 cells maintained their stem cell characteristics along the bioreactor culture time.Finally, the neuronal differentiation step was integrated in the bioreactor process, by addition of retinoic acid when cells were in the middle of the exponential phase. Neurosphere composition was monitored and neuronal differentiation efficiency evaluated along the culture time. The results show that, for bioreactor cultures, we were able to increase significantly the neuronal differentiation efficiency by 10-fold while reducing drastically, by 30%, the time required for the differentiation process. CONCLUSION: The culture systems developed herein are robust and represent one-step-forward towards the development of integrated bioprocesses, bridging stem cell expansion and differentiation in fully controlled bioreactors.

Towards purification of adenoviral vectors based on membrane technology.

Given increasing applications of recombinant adenoviruses for gene therapy and vaccination, there is a need for highly robust and fast purification platforms for their large scale manufacture. Traditional chromatographic methods using resins as matrices have several limitations such as high-pressure drops and slow processing rates due to pore diffusion and channelling of the feed through the bed. In contrast, membrane adsorbers offer the advantage of fast, gentle, and effective isolation. Furthermore, membranes are easy to use, no column packing is needed and, when used as disposables, no cleaning validation is necessary, representing a substantial advantage to meet cGMP requirements. In this work, a strategy for purification of adenovirus vectors from cell-culture bulks fully based on membrane devices is presented. Ultrafiltration membranes with molecular weight cutoffs of 300, 500, and 750 kDa were tested for the concentration of cell-culture supernatant after an initial clarification step. The results show that the use of ultrafiltration/diafiltration membranes not only concentrates the virus but also leads to the removal of 90% of host cell DNA and proteins in the retentate. Two membrane adsorbers (Sartobind Q and Sartobind anion direct) were evaluated for adenovirus vectors capture and purification. To define the best operating conditions, the effect of pH, conductivity, and recirculation of load bulk on the recovery yield of infectious adenoviruses were evaluated. Sartobind anion direct allows for higher recovery yields (up to 62%) of infectious adenoviruses than Sartobind Q; identical ratios between total and infectious adenoviruses (TP/IP) were achieved for both membrane adsorbers. The overall recovery yield of the process is approximately 52%; this work credits membrane technology as an alternative for the concentration and purification of adenoviruses and as a promising solution for downstream processing of other viral vectors.