Hao Xiaolei, Horax Ronny, Qian Xianghong, Wheeler April, Shirataki Hironobu, Wickramasinghe S Ranil
Department of Biomedical Engineering, University of Arkansas, Fayetteville, Arkansas, USA.
Ralph E. Martin Department of Chemical Engineering, University of Arkansas, Fayetteville, Arkansas, USA.
Biotechnol Prog. 2025 Aug 4:e70059. doi: 10.1002/btpr.70059.
Efficient bioreactor clarification for harvesting virus particles is often challenging. Tangential flow filtration is attractive as it can be easily adapted for batch and perfusion operations. Here the feasibility of using reverse asymmetric hollow fiber membranes, where the more open support structure faces the feed stream, has been investigated for harvesting adeno associated virus serotype 2. The open support structure of these membranes stabilizes a secondary membrane consisting of rejected particulate matter. It is essential that the stabilized secondary membrane remains highly permeable. Flux stepping experiments were conducted in total recycle mode in order to determine the critical flux. The critical flux is the maximum stable flux. Higher fluxes lead to a rapid increase in transmembrane pressure under constant flux operation. The critical flux is shown to increase with increasing wall shear rate (feed flow rate). The reduction in turbidity of the permeate relative to the feed decreases with increasing wall shear rate. Harvesting adeno associated virus was conducted at a wall shear rate of 2000 s. The permeate flux was set at 15 Lm h. The feed was concentrated till the transmembrane pressure reached 3.5 kPa. Diafiltration then commenced using 3 diavolumes. While commencing diafiltration with a smaller feed volume will reduce diluent usage and dilution of the product, it is essential that the transmembrane pressure is not too high to create a compacted low permeability secondary membrane. Here the transmembrane pressure was almost constant at 3.5 kPa during diafiltration. Virus recovery was 94%.
高效的生物反应器澄清以收获病毒颗粒通常具有挑战性。切向流过滤很有吸引力,因为它可以很容易地适用于分批和灌注操作。本文研究了使用反向不对称中空纤维膜(其更开放的支撑结构面向进料流)收获腺相关病毒2型的可行性。这些膜的开放支撑结构稳定了由截留的颗粒物组成的二次膜。至关重要的是,稳定的二次膜要保持高渗透性。为了确定临界通量,在全循环模式下进行了通量步进实验。临界通量是最大稳定通量。在恒定通量操作下,更高的通量会导致跨膜压力迅速增加。结果表明,临界通量随壁面剪切速率(进料流速)的增加而增加。相对于进料,渗透液浊度的降低随壁面剪切速率的增加而减小。在壁面剪切速率为2000 s时进行腺相关病毒的收获。渗透通量设定为15 Lm h。将进料浓缩直至跨膜压力达到3.5 kPa。然后使用3倍稀释体积开始进行渗滤。虽然以较小的进料体积开始渗滤会减少稀释剂的使用和产物的稀释,但至关重要的是跨膜压力不能过高,以免形成压实的低渗透性二次膜。在这里,渗滤过程中跨膜压力几乎恒定在3.5 kPa。病毒回收率为94%。