Category: <span>Biologics Production</span>

Classical filtration fouling models do not accurately predict fouling behaviors for sterilizing filtration applied to some bioprocess fluids, particularly when filters are operated in series. To overcome the limitations of these models, we extended a previously developed single-stage fouling model that combined blocking and adsorption mechanisms to dual filters operated in series. Our model demonstrates improvements in predicting bioprocess fluid filtration performance accuracy when applied to microfiltration membranes operated in series, from measured performance of each membrane filter operated individually. In addition, the model and developed method allows for rapid and efficient optimization of prefiltration to final filter area ratios. In redundant sterile filtration, two filters with the same pore size rating are operated in series to protect against an integrity failure of the primary sterilizing filter. Prefilters can also be used to protect final sterilizing-grade membrane filters from excessive fouling which in turn offer the benefits of reduced costs and filtration time…

Biologics Production

The baculovirus expression vector system (BEVS) has emerged as a powerful tool for the production of recombinant proteins used as therapeutics, reagents, and diagnostics. In order to maximize the system’s efficiency and thereby reduce costs, optimizing production parameters is imperative. A critical factor in optimization is the production of a high-quality baculovirus stock with a high-titer, pure clonal population of recombinant virus that is stable over time. Baculovirus stocks may contain alternate varieties of infectious virus due to cross-contamination, outgrowth of non-recombinant virus, and excision of inserts attributable to some recombinant virus production technologies. Since the advent of the BEVS, the “gold standard” for production of pure baculovirus stocks has been plaque purification. Briefly, plaque purification involves infecting a monolayer of cells with dilutions of virus before applying an agarose overlay to the monolayer. After a 5–7 day incubation, isolated plaques can be picked, virus eluted from the agarose plug, and amplified. The drawbacks of plaque purification are: (1) it is time and labor-intensive; (2) the results hinge greatly on the health of the cells and the cell density at infection; (3) identification and picking of isolated plaques is challenging; and (4) the integrity of the procedure is easily compromised by virus diffusion and mass flow of virus-containing liquid beneath the agarose overlay…

Biologics Production

There are approximately 400 vaccines in commercial manufacture targeted at 24 infectious diseases. Of these vaccines, about 300 are viral-based. It is estimated that 1400 vaccines are in development, half of which are viral-based (~ 640 viral vaccines, ~ 200 viral vectors, ~ 60 virus-like particles). Another 240 gene therapy products are in development that utilize the same viral-based technology. A live vector vaccine is one that uses a weakened or harmless microorganism to transport antigenic viral pieces into a cell in order to stimulate an immune response. Vectored vaccines show promise in reliably inducing potent cell-mediated immunity, which is essential for complex diseases such as AIDS, malaria, and cancer…

Biologics Production

The impact of individual and interactive behaviors of various fermentation process parameters on laccase and peroxidase-free tyrosinase production were investigated by isolated Streptomyces antibioticus RSP-T1. Six key bioprocess factors (medium pH, rpm, incubation time, sodium chloride concentration, complex nitrogen [yeast extract + peptone], and carbon source [maltose]) were selected based on using a one variable at a time methodology. All selected parameters had an impact at individual and interactive levels on tyrosinase production. Only 25% of the improved tyrosinase production was attributed to the optimized fermentation parameters selected. Regarding the nutritional parameters, the complex nitrogen/carbon source concentration (maltose and yeast extract + peptone) was found to have the most significance impact on overall tyrosinase enzyme production. Physiological growth factors (pH, rpm, and incubation time) played key roles at an interactive level. A maximum yield of 12.60 IU/mL tyrosinase production was achieved with optimized medium, adjusted to 7.5 pH, consisting of 0.75% maltose (w/v), 0.2% yeast extract (w/v), 0.2% peptone (w/v), and 1.25% sodium chloride (w/v) at 160 rpm in 24 hours. This study identified the optimum medium component concentrations for improved tyrosinase production by S. antibioticus RSP-T1. This strain requires complex nitrogen sources (yeast extract and peptone) for increased product yield. Overall, a greater than 250% increase in tyrosinase production was achieved using this optimization approach, as compared to conventional methods…

Biologics Production

Viral clearance studies are required for pharmaceuticals derived from human and/or animal sources such as recombinant proteins produced in eukaryotic cell lines, human blood products and vaccines, and even for some critical class III medical devices. It is mandatory to demonstrate that steps in the manufacturing process are capable of inactivating or removing potential viral contaminants. For this, a laboratory-scale (downscale) of the process step is developed and challenged with different model virus solutions. The viral concentrations are quantitatively determined in the feed material and the relevant product fraction. The ratio of both defines the reduction in virus and specifies the viral inactivation or viral removal capacity of the investigated process step…

Biologics Production

Viral clearance studies are required for pharmaceuticals derived from human and/or animal sources such as recombinant proteins produced in eukaryotic cell lines, human blood products and vaccines, and even for some critical class III medical devices. It is mandatory to demonstrate that steps in the manufacturing process are capable of inactivating or removing potential viral contaminants. For this, a laboratory-scale (downscale) of the process step is developed and challenged with different model virus solutions. The viral concentrations are quantitatively determined in the feed material and the relevant product fraction. The ratio of both defines the reduction in virus and specifies the viral inactivation or viral removal capacity of the investigated process step…

Biologics Production

Biosimilars, and related biopharmaceutical biobetters and biogenerics, are still relatively new, but are already starting to impact worldwide biopharmaceutical markets. Most discussions of biosimilars center on developed regions where markets are mature and manufacturing capabilities allow for the cost-efficient manufacture of these complex molecules. This article covers the development of these products outside the United States (US), European Union (EU), and other developed, generally rather affluent and high-technology economy-based countries. To start, we first offer some definitions…

Biologics Production

The expansion of stem cells, including mesenchymal stem cells (MSCs), has been successfully demonstrated using microcarrier-based small bioreactors such as spinner flasks. In this study, we explored a simple alternative for microcarrier-based MSC expansion using conventional shake flasks. This method relies on a new type of shaker with built-in CO2 gas control capability, the New Brunswick™ S41i incubator shaker. The expansion of adipose-derived mesenchymal stem cells (AdMSCs) was compared between shake and spinner flasks containing microcarriers. The AdMSCs were seeded at a density of 3 × 103 cells/cm2 in both setups, each containing 0.5 g of plastic microcarriers and 50 mL of stem cell growth medium. The cell culture experiments were conducted over 12 days with samples collected daily for cell growth, biochemistry, and metabolite analysis. The study revealed that AdMSCs cultured under shake flask conditions achieved excellent growth under 12-day batch-culture conditions. Finally, the AdMSCs expanded using the shake flask method retained high quality stem cell characteristics, as indicated by CD44 and CD90 stem cell marker assays, and the ability of these cells to differentiate into either adipocytes or osteocytes…

Biologics Production

The safety of biological products (biologics) derived from in vitro cultured cell lines of animal origin is dependent both on clinical studies to evaluate efficacy, and a matrix of controls throughout the manufacturing process to assure consistency, quality, and safety of the marketed product for human use. One major area of concern is virus safety. Through the combination of: (A) careful selection of raw materials; (B) testing of process intermediates; and (C) virus clearance evaluations of the individual steps in the manufacturing process; biologics manufacturers can demonstrate that their products are free from detectable adventitious and endogenous viruses. Comprehensive regulatory guidance suggests approaches for virus testing of biologics at early and later stages of clinical development and, although some countries have specific requirements, many of these approaches are harmonized worldwide. In general, regulatory authorities expect purification processes to include multiple steps with complementary, or orthogonal, methods for virus reduction including inactivation and separation or removal. Each step in the process may be more or less effective for reducing levels of different test viruses, and therefore selection of the appropriate panel of test viruses for the specific product is critical for viral clearance studies…

Biologics Production

Hybridoma cell lines are highly unpredictable and often, an unreliable source of important antibodies of national security interest. There is an urgent need to convert antibody production from these cell lines into robust, recombinant platforms that can reliably produce large quantities of antibody on demand, and abandon methods based on murine ascites production. This work describes the use of lentiviral vectors, Chinese hamster ovary (CHO)-K1 cells, and high-density perfusion cultures for antibody production. Cell line development was rapid, high insertion copy numbers were achievable, and the heavy/light chain ratios could be rapidly optimized. The mammalian cells provided an appropriate environment for IgG folding and obviated the difficult purification steps such as removal of endotoxins, refolding, or dealing with abnormal post-synthetic modifications common to other production systems. We found that even in the absence of an optimized cell line, in high-density cultures, routine productivities in the 1–5 g/L range were achieved. As expected, productivity was independent of the performance of the original hybridomas. We conclude that the lentiviral vector system can achieve high copy numbers of immunoglobulin genes with optimized heavy and light chain ratios to appropriately assemble and secrete the immunoglobulins, achieving high productivity. This observation suggests that substantial advances can be made by selecting and optimizing the cell line used for immunoglobulin production. The lentiviral vector-based method of antibody production offers substantial improvements over traditional murine ascites-based antibody production in terms of reliability, productivity, and cumulative cost—if the antibody need exceeds 1–3 grams within the shelf life of the product…

Biologics Production