Tag: <span>process optimization</span>

The ability to scale a cell culture effectively and efficiently, from lab to manufacturing, is critical to maximizing productivity whilst minimizing the risk of run failures and delays that can cost millions of dollars per month. The task of scaling well, however, is still considered to be a challenge by many upstream scientists, and this can be an exercise in trial and error. Traditionally, scaling has most often been performed using arithmetic in a spreadsheet and/or simple ā€œback of an envelopeā€ calculations. For some, it may even come in the form of support from a team of data scientists using advanced analytical software. This dependency on what some consider to be complex mathematics or statistics has resulted in the common consideration of using just one scaling parameter at a time, one scale at a time.

However, it is difficult to determine easily or optimally, from the start, whether a process successfully transfers across scales based on only one process parameter, at one scale. In this article, we describe the benefits of using a risk-based approach to scaling, and the development of a software scaling tool known as BioPATĀ® Process Insights for predictive scale conversion across different bioreactor scales. BioPAT Process Insights can be used to consider multiple parameters and across multiple scales simultaneously, from the start of a scaling workflow. We briefly describe how it was used in a proof-of-concept scale-up study to allow a faster, more cost-effective process transfer from 250 mL to 2000 L. In summary, using BioPAT Process Insights, in conjunction with a bioreactor range that has comparable geometry and physical similarities across scales, has the potential to help biopharma manufacturing facilities reach 2000 L production-scale volumes with fewer process transfer steps, saving both time and money during scale-up of biologics and vaccines.

Manufacturing Risk Analysis and Management

When working on biotherapeutic process development, the analysis of spent cell culture media is often a daily practice during the optimization of bioreactor conditions and media composition. The introduction of parallel microbioreactor systems has decreased the complexity and costs of process development by allowing for concurrent studies of multiple bioreactor and media variables. However, the bioreactorsā€™ small volumes (typically less than 250 mL) limit the volume of media one can extract for daily sampling. We describe a means to analyze spent media with an integrated microchip capillary electrophoresis mass spectrometer (CE-MS) analyzer with minimal sample volume requirements and rapid analysis time. The platform was evaluated with a parallel microbioreactor system (ambrĀ® 250) culturing a Chinese hamster ovary (CHO) cell line stressed by varying levels of ammonia (NH3).

The spent media analysis identified net increases in the levels of the amino acids (AA) Ala, Arg, Asp, Glu, Gly, His, Ile, Leu, Lys, Phe, Thr, Trp, Tyr, and Val in all bioreactors, with Gly levels showing increases in excess of 8-fold initial levels in all bioreactors. Other media components either steadily decreased in concentration or were completely depleted by the end of culture. For example, Asn was depleted in all of the unstressed and 10 mM NH3-stressed bioreactors, but was approximately twice as high as the initial levels in the 30 mM NH3-stressed bioreactors at the end of the culture periods. Also, the 30 mM NH3-stressed condition may have caused either complete degradation or rapid consumption of choline, since it was no longer present starting at the t = 36 h sampling. Overall, the monitored media components were observed to have independent trajectories based on feeding and consumption by the cells, and depending on the stressed condition. The capability to have more frequent spent media analyses would allow for real-time observation of these process changes and associated control strategies.

Biologics Production

A rapid increase in the number of gene therapy trials and products has led to a comparable increase in the need for industrial production of viral gene therapy vectors such as lentiviral, adeno-associated, and adenoviral vectors. Current production systems are limited with respect to scalability and robustness. With our CAPĀ® and CAP-Tā„¢ cell lines, we have developed a novel system for high-density suspension culture, efficient and reproducible transfection, and highly efficient production of viral vectors. By upstream process optimization, we have obtained a robust and high-density fed-batch culture system which can be scaled in any current bioreactor format. A design-of-experiments approach has been employed to optimize transient production of lentiviral vectors with significantly higher titers than can be obtained with adherent HEK293T cells…

Biologics Production Cell & Gene Therapy

In general, yeasts offer advantages for recombinant protein expression because their intracellular environment is suitable for the correct folding of recombinant proteins and grow very high cell densities in defined fermentation media. Within the yeast kingdom, Pichia pastoris has been successfully used for expressing several recombinant proteins. The genome of this yeast contains two copies of the alcohol oxidase (AOX) gene, where the AOX1 promoter regulates 85% of the alcohol oxidase activity and drives the recombinant protein expression into the cell. One of the most successfully recombinant proteins expressed in Pichia pastoris is the hepatitis B surface antigen (HBsAg). The current manufacturing process of the active pharmaceutical ingredient (HBsAg) of the Cuban hepatitis B vaccine (HeberBiovacā„¢ HB) starts with the expression of the HBsAg in Pichia pastoris….

Biologics Production

Optimization of the key factors in a biopharmaceutical process is necessary to meet the continuous rise in the production demands. One of the key factors in the process addresses the diverse nutritional and growth requirements of the cell cultureā€”peptone supplementation. Peptones are low molecular weight protein digests, which provide nutrients such as amino acids, peptides, vitamins, and minerals to the culture medium. They are widely accepted as the supplements that enhance the performance of a chemically-defined cell culture medium, and have successfully been used for over thirty years…

Biologics Production

In todayā€™s biopharmaceutical pipeline, monoclonal antibodies are a predominant modality for a broad range of clinical indications, including inflammatory disorders, oncology, and infectious diseases. More than two dozen antibody-based products are commercially available. In 2004, six of the 12 new biopharmaceutics that gained approval in the United States and Europe were antibody-based products. Most antibody therapies require high doses over a long period of time, which requires large amounts of purified product per patient. Therefore, manufacturing capacity to meet the demands of antibody production is a real challenge. It is desirable to have highly productive and consistent manufacturing processes. In addition, speed to market is critical to deliver health benefits to patients quickly and to achieve business successā€¦

Biologics Production Manufacturing

The Vmax™ technique has been used extensively to estimate filter area requirements for normal flow filtration (NFF) processes in biopharmaceutical applications. The benefits that this technique presents over conventional flow decay methods are the speed of testing, reduced volume requirements for evaluation, and competitive testing of varying filter types/sizes ā€” all of which present an optimized filter screening strategy and preliminary estimate of optimized filter size requirements. Filter size or filtration area requirements derived using the Vmax technique consist of contributions from both capacity and flow-time aspects of the filtration process. This article examines the relative contributions of these terms to overall filter sizing vis-Ć -vis the ease of fluid filterabilityā€¦

Biologics Production Uncategorized

Biopharmaceutical manufacturers are constantly seeking new ways to lower production costs, while simultaneously increasing cost effectiveness without sacrificing quality. The U.S. biotech industry has grown from $8 billion in 1992 to $30 billion in 2002. As productivity in biopharmaceutical manufacturing has increased, pressures to contain costs have mounted in the healthcare industry, coupled with increased demands by investors, which results in increased cost containment pressures on the industry as a whole. Some biotechnology products need to be produced in large quantities (hundreds of kilograms per year) to meet both current and expected demand. This requires significant manufacturing capacity, and makes the types of incremental process improvements commonly sought in chemical pharmaceutical processing an attractive proposition for biopharmaceutical manufacturingā€¦

Manufacturing

One of the major aims of modern biotechnology companies that are producing recombinant therapeutic proteins is to focus on timeline reduction of critical cell line selection and process optimisation studies in order to minimise the time and financial constraints of early development products. This ā€œminimalist paradigmā€ of maximising early development throughput with minimal capital/operational outlays is a key driver for implementation of novel analytical technologies which can be applied at-line to process instrumentation. The large-scale production of recombinant therapeutics in the biopharmaceutical industry relies on in-process monitoring of product titre. Traditional titre determination methods, including enzyme-linked immunosorbent assay (ELISA) and protein A high performance liquid (immunoaffinity) chromatography (Protein A HPLC), are time consuming, and often reliant on analytical support from separate specialist teams/departments requiring detailed scientific knowledge and extensive training, with expensive capital outlay utilising large equipment…

Biologics Production