Nandy S, Tarbell J M
Department of Chemical Engineering, Pennsylvania State University, University Park 16802.
Biorheology. 1987;24(5):483-500. doi: 10.3233/bir-1987-24506.
Wall shear stress has been measured by flush-mounted hot film anemometry distal to an Ionescu-Shiley tri-leaflet valve under pulsatile flow conditions. Both Newtonian (aqueous glycerol) and non-Newtonian (aqueous polyacrylamide) blood analog fluids were investigated. Significant differences in the axial distribution of wall shear stress between the two fluids are apparent in flows having nearly identical Reynolds numbers. The Newtonian fluid exhibits a (peak) wall shear rate which is maximized near the valve seat (30 mm) and then decays to a fully developed flow value (by 106 mm). In contrast, the shear rate of the non-Newtonian fluid at 30 mm is less than half that of the Newtonian fluid and at 106 mm is more than twice that of the Newtonian fluid. It is suggested that non-Newtonian rheology influences valve flow patterns either through alterations in valve opening associated with low shear separation zones behind valve leaflets, or because of variations in the rate of jet spreading. More detailed studies are required to clarify the mechanisms. The Newtonian wall shear stresses for this valve are low. The highest value observed anywhere in the aortic chamber was 2.85 N/m2 at a peak Reynolds number of 3694.
在脉动流条件下,已通过安装在Ionescu-Shiley三叶瓣瓣膜远端的嵌入式热膜风速仪测量了壁面剪应力。研究了牛顿流体(甘油水溶液)和非牛顿流体(聚丙烯酰胺水溶液)这两种血液模拟流体。在雷诺数几乎相同的流动中,两种流体之间壁面剪应力的轴向分布存在明显差异。牛顿流体呈现出一个(峰值)壁面剪切速率,该速率在阀座附近(30毫米处)达到最大值,然后衰减至充分发展流动的值(在106毫米处)。相比之下,非牛顿流体在30毫米处的剪切速率不到牛顿流体的一半,而在106毫米处则是牛顿流体的两倍多。有人认为,非牛顿流变学通过与瓣膜小叶后方低剪切分离区相关的瓣膜开口变化,或者由于射流扩散速率的变化,影响瓣膜流动模式。需要更详细的研究来阐明其机制。该瓣膜的牛顿壁面剪应力较低。在主动脉腔内观察到的最高值为2.85 N/m²,峰值雷诺数为3694。