David B, Doré E, Jaffrin M Y, Legallais C
Université de Technologie de Compiègne, Laboratoire de Biomécanique et Génie Biomedical, Compiègne, France.
Int J Artif Organs. 2004 Apr;27(4):284-93. doi: 10.1177/039139880402700404.
Fluidized bed bioreactor with alginate beads may be an alternative to hollow fiber cartridge to host hepatocytes for bioartificial liver purposes. After the bioreactor design and the characterization of fluid mechanics, the present study was aimed at analyzing bi-directional mass transfers of calibrated species between external fluid and empty beads. Static (batch) and dynamic (fluidized bed bioreactor) experimental conditions were analyzed. A simple modelling approach permitted the definition of mass transfer coefficients. The motion of beads within the bioreactor clearly enhanced mass transfer kinetics, but did not alter the amount exchanged. The shear enhanced diffusion coefficient for VitB12 was 20 times higher in the fluidized bed bioreactor than under batch conditions, proving the efficiency of such a device.
带有藻酸盐珠的流化床生物反应器可能是用于生物人工肝目的、承载肝细胞的中空纤维盒的替代方案。在完成生物反应器设计和流体力学特性表征后,本研究旨在分析校准物质在外部流体与空珠之间的双向传质。分析了静态(间歇式)和动态(流化床生物反应器)实验条件。一种简单的建模方法可定义传质系数。生物反应器内珠的运动明显增强了传质动力学,但未改变交换量。在流化床生物反应器中,维生素B12的剪切增强扩散系数比间歇条件下高20倍,证明了这种装置的效率。