Publications by authors named "Oliver Kaltenbrunner"

Recently, continuous downstream processing has become a topic of discussion and analysis at conferences while no industrial applications of continuous downstream processing for biopharmaceutical manufacturing have been reported. There is significant potential to increase the productivity of a Protein A capture step by converting the operation to simulated moving bed (SMB) mode. In this mode, shorter columns are operated at higher process flow and corresponding short residence times.

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Recombinant therapeutic proteins are heterogeneous due to chemical and physical modifications. Understanding the impact of these modifications on drug safety and efficacy is critical for optimal process development and for setting reasonable specification limits. In this study, we describe the development of an in vitro continuous flow dialysis system to evaluate potential in vivo behavior of thiol adducted species and incorrectly disulfide bonded species of therapeutic proteins.

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The demand for increased formulation concentrations for protein therapeutics puts a significant strain on already existing tangential flow filtration (TFF) systems that were constructed with lower protein concentration targets as part of their design criteria. TFF is commonly used to buffer exchange and concentrate the product to the appropriate drug substance concentration. Analyzing the ability of an existing TFF system to process under conditions outside its original design specifications can be challenging.

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Ceramic hydroxyapatite (CHT) is a multimodal chromatographic medium widely used in the pharmaceutical industry for the purification of biomolecules. CHT is a sintered form of hydroxyapatite crystals with moderate stability at acidic conditions. This moderate stability may lead to underperformance of CHT packed bed lifetime, especially under acidic conditions, which should be monitored by diagnostic tools to design optimal buffer systems for the step.

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In the production of a human therapeutic protein from inclusion bodies, product related impurities of very similar size and charge to the product are created as byproducts of the refold process. Their removal is usually challenging even when using chromatography with high performance resins and elution by shallow linear gradients. Additionally, performing this type of separation for commercial production adds increased complexity.

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