| Literature DB >> 32613033 |
Feihu Zhao1,2,3, Damien Lacroix4, Keita Ito1,2, Bert van Rietbergen1, Sandra Hofmann1,2.
Abstract
Bone tissue engineering (BTE) experiments in vitro have shown that fluid-induced wall shear stress (WSS) can stimulate cells to produce mineralized extracellular matrix (ECM). The application of WSS on seeded cells can be achieved through bioreactors that perfuse medium through porous scaffolds. In BTE experiments in vitro, commonly a constant flow rate is used. Previous studies have found that tissue growth within the scaffold will result in an increase of the WSS over time. To keep the WSS in a reported optimal range of 10-30 mPa, the applied external flow rate can be decreased over time. To investigate what reduction of the external flow rate during culturing is needed to keep the WSS in the optimal range, we here conducted a computational study, which simulated the formation of ECM, and in which we investigated the effect of constant fluid flow and different fluid flow reduction scenarios on the WSS. It was found that for both constant and reduced fluid flow scenarios, the WSS did not exceed a critical value, which was set to 60 mPa. However, the constant flow velocity resulted in a reduction of the cell/ECM surface being exposed to a WSS in the optimal range from 50% at the start of culture to 18.6% at day 21. Reducing the fluid flow over time could avoid much of this effect, leaving the WSS in the optimal range for 40.9% of the surface at 21 days. Therefore, for achieving more mineralized tissue, the conventional manner of loading the perfusion bioreactors (i.e. constant flow rate/velocity) should be changed to a decreasing flow over time in BTE experiments. This study provides an in silico tool for finding the best fluid flow reduction strategy.Entities:
Keywords: Extracellular matrix mineralization; In silico bone tissue engineering; Perfusion bioreactor; Wall shear stress
Year: 2020 PMID: 32613033 PMCID: PMC7315008 DOI: 10.1016/j.bonr.2020.100265
Source DB: PubMed Journal: Bone Rep ISSN: 2352-1872
Fig. 1Schematic illustration of homogenization of cell and ECM mixture.
Fig. 2Schematic illustration of parameter exchange between (a) diffusion process and (b) rheological property (i.e. dynamic viscosity) adaptation (ECM/cells growth) in an idealized porous domain.
Fig. 3(a) One quarter of the fluid domain in the bioreactor for CFD analysis: the up surface and bottom surface are defined as inlet and outlet, respectively; two side cutting surfaces are symmetric boundaries; the outer side surface and scaffold surfaces are defined as non-slip walls, (b) scaffold geometry with pore size and porosity equal in the three orthogonal directions.
Fig. 4Seven types of applied inlet fluid velocities (V), where type 1 (k1 = 0 mm/s day) is constant fluid velocity, types 2–7 have a decreasing velocity profile from day 1 to day 21.
Fig. 5(a) Simulated pore volume filling by homogenized ECM/cell at day 7, 14 and 21, the ECM/cell volume increases within 21 days, A-A is a zoomed-in top view that shows the cell/ECM growth within one unit scaffold, (b) increasing wall shear stress distribution at the interface between medium and ECM/cell at days 7, 14 and 21, the geometry is the fluid volume (counterpart of the cell/ECM volume within the pores).
Fig. 6Evolution of ECM/cell surface area fraction that undergoes the WSS of 10–30 mPa (for stimulating mineralization) under different loading conditions of the perfusion bioreactor.