首页> 外文会议>Conference on single-use technologies II: bridging polymer science to biotechnology applications >EXPERIMENTAL DESIGN AND SMALL-SCALE MODEL FOR HIGH-PERFORMING PERFUSION MEDIA AND PROCESSES SCALABLE TO 50 L BIOREACTORS
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EXPERIMENTAL DESIGN AND SMALL-SCALE MODEL FOR HIGH-PERFORMING PERFUSION MEDIA AND PROCESSES SCALABLE TO 50 L BIOREACTORS

机译:高性能灌注介质的实验设计和小规模模型以及可扩展至50 L生物反应器的过程

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Cell culture perfusion processes are considered optimal for a truly integrated continuous biomanufacturing pipeline. The nutrient-rich but balanced media should be designed to support very low cell-specific perfusion rates (CSPR) that minimize media consumption but maximize viable cell days and productivities. Optimized processes at low CSPR drastically reduce equipment costs, lab space, and product dilution. Finally, operating at very low CSPR enables running mammalian cell bioprocesses as true chemostat cultures in the future. We demonstrate a general workflow to develop high-performing perfusion media using small-scale models and transferred the process to 50 L scale at CSPR of 20 pL/c/d. Recombinant CHO cells were evaluated at small scale in shaking tubes. Cells were grown in HyClone™ ActiPro or CDM4NS0 basal media, and optimal spike concentrations of HyClone Cell Boost™ supplements were determined using a DoE-supported workflow. The identified high-performing perfusion medium was applied to ReadyToProcess WAVE™ 25 and XDR-50 bioreactor runs. Different strategies were tested to find the critical minimum CSPR and maximum supported viable cell density (VCD). The obtained product profile was compared between scales, as determined by glycan-, charge-, and size-variant distribution. Scale-down models were leveraged to define high-performing media and applied to bioreactor runs at constant volumetric perfusion rate, VCD, or CSPR. CSPR values as low as 10 pL/c/d at 2 × 10~8 c/mL were achieved. These results make high-density perfusion processes suitable for inoculum preparation (N-1) or high cell density cryopreservation. The developed perfusion processes supported steady-state production at constant 5 × 10~7 c/mL by applying a continuous cell bleed and were scaled to 50 L.
机译:对于真正整合的连续生物制造流水线,细胞培养灌注过程被认为是最佳的。营养丰富但平衡的培养基应设计为支持极低的细胞特异性灌注速率(CSPR),以最大程度地减少培养基消耗,但最大化可行的细胞天数和生产率。以低CSPR进行优化的工艺可以大大降低设备成本,实验室空间和产品稀释度。最后,在非常低的CSPR下运行可以使哺乳动物细胞的生物过程在未来成为真正的化学恒温器培养物。我们演示了使用小规模模型开发高性能灌注培养基的一般工作流程,并将该过程以20 pL / c / d的CSPR转移至50 L规模。在摇管中以小规模评估重组CHO细胞。细胞在HyClone™ActiPro或CDM4NS0基础培养基中生长,并使用DoE支持的工作流程确定HyClone Cell Boost™补充剂的最佳峰浓度。将鉴定出的高性能灌注培养基应用于ReadyToProcess WAVE™25和XDR-50生物反应器。测试了不同的策略,以找到关键的最小CSPR和最大支持的活细胞密度(VCD)。比较所获得的产品概况,在不同规模之间进行比较,如聚糖分布,电荷分布和尺寸变化分布所确定的。利用按比例缩小的模型来定义高性能培养基,并以恒定的体积灌注率,VCD或CSPR应用于生物反应器运行。在2×10〜8 c / mL下获得的CSPR值低至10 pL / c / d。这些结果使高密度灌注过程适合接种物制备(N-1)或高细胞密度冷冻保存。所开发的灌注过程通过施加连续的细胞抽血,支持以恒定的5×10〜7 c / mL进行稳态生产,并放大至50L。

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