Vortical flow. Part 1. Flow through a constant-diameter pipe

被引:41
|
作者
Mattner, TW [1 ]
Joubert, PN [1 ]
Chong, MS [1 ]
机构
[1] Univ Melbourne, Dept Mech & Mfg Engn, Melbourne, Vic 3010, Australia
关键词
D O I
10.1017/S0022112002008741
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
This paper describes an exploration of the behaviour and properties of swirling flow through a constant-diameter pipe. The experiments reveal a complicated transition process as the swirl intensity Omega is increased at fixed pipe Reynolds number Re approximate to 4900. For Omega less than or equal to 1.09, the vortex was steady, laminar, axisymmetric, and developed slowly with streamwise distance. The upstream velocity profiles were similar to those commonly appearing in the literature in similar apparatus. Spiral vortex breakdown appeared in the test section for 1.09 less than or equal to Omega less than or equal to 1.31 and was associated with a localized transition from jet-like to wake-like mean axial velocity profiles. Further increase in Omega caused the breakdown to move upstream of the test section. Downstream, the core of the post-breakdown flow was unsteady and recovered toward jet-like profiles with streamwise distance. At Omega = 2.68, a global transition occurred in which the mean axial velocity profiles suddenly developed an annular axial velocity deficit. At the same time, disturbances began to appear in the outer flow. Further increase in Omega eventually led to an annulus of reversed axial flow and a completely unsteady vortex.
引用
收藏
页码:259 / 291
页数:33
相关论文
共 50 条
  • [21] OPTIMUM ECONOMIC PIPE DIAMETER FOR PUMPING HERSCHEL-BULKLEY FLUIDS IN LAMINAR FLOW.
    Garcia, Edgardo J.
    Steffe, James F.
    Journal of Food Process Engineering, 1986, 8 (02) : 117 - 136
  • [22] Effects of viscous dissipation on the heat transfer in forced pipe flow. Part 1: both hydrodynamically and thermally fully developed flow
    Aydin, O
    ENERGY CONVERSION AND MANAGEMENT, 2005, 46 (05) : 757 - 769
  • [23] MICROSCOPIC FLOW NEAR THE SURFACE OF TWO-DIMENSIONAL POROUS MEDIA. PART 1. AXIAL FLOW.
    Larson, R.E.
    Higdon, J.J.L.
    Journal of Fluid Mechanics, 1986, 166 : 449 - 472
  • [25] USE OF THE MICROCOMPUTER AS A SUPPLEMENT TO THE STUDY OF PIPE FLOW.
    Kaufman, Chris D.
    Janna, William S.
    CoED (Journal) (Computers in Education Division of ASEE), 1986, 6 (03): : 2 - 6
  • [26] ASPECTS OF THE EQUILIBRIUM PUFF IN TRANSITIONAL PIPE FLOW.
    Bandyopadhyay, Promode R.
    Journal of Fluid Mechanics, 1986, 163 : 439 - 458
  • [27] JET INJECTIONS FOR OPTIMUM MIXING IN PIPE FLOW.
    Fitzgerald, S.D.
    Holley, E.R.
    Research Report - University of Illinois at Urbana-Champaign, Water Resources Center, 1979, (144):
  • [28] CORRELATION MEASUREMENTS IN THE CORE OF A TURBULENT PIPE FLOW.
    Ko, N.W.M.
    Bullock, K.J.
    Smith, T.C.
    Engineering Journal of Singapore, 1982, 9 (01): : 11 - 21
  • [29] Edge states and slugs in cylindrical pipe flow.
    Duguet, Yoann
    Willis, A. P.
    Kerswell, R. R.
    MECANIQUE & INDUSTRIES, 2010, 11 (02): : 157 - 162
  • [30] ON THE WALL PRESSURE FIELD IN TURBULENT PIPE FLOW.
    Bull, M.K.
    Langeheineken, Th.
    Mitteilungen, Max-Planck-Institut fuer Stroemungsforschung und der Aerodynamischen Versuchsanstalt, 1981, (73):