| Autor: |
Raihan MK; Department of Mechanical Engineering, Clemson University, Clemson, SC 29634-0921, USA. xcxuan@clemson.edu., Kim N; Department of Mechanical Engineering, Clemson University, Clemson, SC 29634-0921, USA. xcxuan@clemson.edu., Song Y; College of Marine Engineering, Dalian Maritime University, Dalian 116026, P. R. China. yongxin@dlmu.edu.cn., Xuan X; Department of Mechanical Engineering, Clemson University, Clemson, SC 29634-0921, USA. xcxuan@clemson.edu. |
| Abstrakt: |
Many engineering and natural phenomena involve the merging of two fluid streams through a T-junction. Previous studies of such merging flows have been focused primarily upon Newtonian fluids. We observed in our recent experiment with five different polymer solutions a direct change from an undisturbed to either a steady vortical or unsteady three-dimensional flow at the T-junction with increasing inertia. The transition state(s) in between these two types of merging flow patterns is, however, yet to be known. We present here a systematic experimental study of the merging flow of polyethylene oxide (PEO) solutions with varying polymer concentrations and molecular weights. Two new paths of flow development are identified with the increase of Reynolds number: one is the transition in very weakly viscoelastic fluids first to steady vortical flow and then to a juxtaposition state with an unsteady elastic eddy zone in the middle and a steady inertial vortex on each side, and the other is the transition in weakly viscoelastic fluids first to a steady vortical and/or a juxtaposition state and then to a fully unsteady flow. Interestingly, the threshold Reynolds number for the onset of elastic instabilities in the merging flow is not a monotonic function of the elasticity number, but instead follows a power-law dependence on the polymer concentration relative to its overlap value. Such a dependence turns out qualitatively consistent with the prediction of the McKinley-Pakdel criterion. |
