Asymptotic methods are employed to derive the leading-order equations which govern the fluid dynamics of timedependent, incompressible, planar liquid sheets at low Reynolds numbers using as small parameter the slendemess ratio. Analytical and numerical solutions of relevance to both steady film cast
Line fountain behavior at low-Reynolds number
β Scribed by N. Srinarayana; N. Williamson; S.W. Armfield; Wenxian Lin
- Publisher
- Elsevier Science
- Year
- 2010
- Tongue
- English
- Weight
- 773 KB
- Volume
- 53
- Category
- Article
- ISSN
- 0017-9310
No coin nor oath required. For personal study only.
β¦ Synopsis
In this paper, we present line fountain behavior at low-Reynolds numbers obtained by experiments. The experiments are conducted over the range of Reynolds number 2:1 K Re K 127 and Froude number 0:4 K Fr K 42. It is observed that the fountain behavior can be categorized broadly into four regimes: the steady; flapping; laminar mixing; and jet-type mixing behavior, at full development. The critical Froude number for transition from a steady to unsteady flow varies with the Reynolds number. For Re J 60, the transition is independent of Re and is well described by the Fr $ 1:0 line. Over the range 10 < Re K 50, the transition can be approximated by a constant FrRe 2=3 line. For Re K 10, there is a higher dependency on the Reynolds number with a very sharp increase in the critical Froude number and it is hypothesized that the demarcation line follows Fr $ Re Γn , where n % 2-4. The fountain exhibits flapping behavior in the range 13Re Γ2=3 K Fr K 37Re Γ2=3 . These observed fountain behaviors are mapped on to a Re-Fr plot. In addition, the observed, non-dimensionalised fountain height z m is found to be in reasonable agreement with previous results on laminar line fountains. In particular, the experimental results confirm the scaling z m $ FrRe Γ1=2 in the steady regime which was obtained previously by scaling analysis.
π SIMILAR VOLUMES
## Abstract Results are presented for the flow past a stationary square cylinder at zero incidence for Reynolds number, __Re__ β©½ 150. A stabilized finiteβelement formulation is employed to discretize the equations of incompressible fluid flow in twoβdimensions. For the first time, values of the lam