Challenges and solutions to manufacturing of low viscosity, ultra-high concentration IgG1 drug products: From late downstream process to final fill finish processing.

Vaibhav D Deokar, Alok Sharma, Volety Mallikarjun Subrahmanyam
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Abstract

Challenges in manufacturing of high concentration antibody formulations have seldom been discussed. These are observed mainly form late downstream operations where antibody gets concentrated to its final strength, to final fill finish processing and containerization of the product. Present paper summarizes challenges typically observed in manufacturing and processing of high concentration antibody products and provides turnkey solutions to these typical challenges in order to have their consistent and robust manufacturing process. IgG1 has been used as model protein for studying the challenges and providing solutions to them. The late downstream challenges like increased viscosity limiting further concentration can be resolved by used of viscosity modifying agents in the formulation. Replacement of conventionally used 'A' screen membranes with 'D' screen or using single pass TFF can further provide advantage in targeting higher concentrations for same protein with lesser shear and aggregation. Using 0.5μm/0.2μm asymmetric or bilayered membrane instead of conventional 0.2μm membrane resulted in better flux while filtration of high concentration IgG1 formulation. In process holding time during filling operation was optimized to be <60min based on the nozzle drying time for high concentration IgG1 formulation. Appropriate control strategy of replacing filling nozzles and performing periodic fill weight check was proposed for fill finish process of high concentration IgG1 formulation.

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生产低粘度、超高浓度 IgG1 药物产品所面临的挑战和解决方案:从后期下游工艺到最终灌装加工。
人们很少讨论高浓度抗体制剂生产过程中面临的挑战。这些挑战主要体现在抗体浓缩到最终强度的后期下游操作,以及产品的最终灌装加工和装箱。本文总结了在生产和加工高浓度抗体产品过程中通常会遇到的挑战,并针对这些典型挑战提供了全套解决方案,以确保生产过程的一致性和稳健性。IgG1 被用作研究这些挑战并提供解决方案的模型蛋白。通过在配方中使用粘度调节剂,可以解决粘度增加限制进一步浓缩等后期下游难题。用 "D "型滤网代替传统的 "A "型滤网膜或使用单程 TFF 可以进一步提高相同蛋白质的浓度,减少剪切和聚集。使用 0.5μm/0.2μm 不对称膜或双层膜代替传统的 0.2μm 膜,在过滤高浓度 IgG1 制剂时可获得更好的通量。灌装操作过程中的保温时间优化为
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CiteScore
1.90
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发文量
34
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