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
  • [41] EXPERIMENTAL INVESTIGATION OF THE EFFECT OF A CONSTRICTION ON TURBULENT PIPE FLOW.
    Lissenburg, R.C.D.
    Hinze, J.O.
    Leydens, H.
    Technische Hogeschool Delft, Afdeling der Werktuigbouwkunde (Report) WTHD, 1974, (76):
  • [43] On unsteady boundary-layer separation in supersonic flow. Part 1. Upstream moving separation point
    Ruban, A. I.
    Araki, D.
    Yapalparvi, R.
    Gajjar, J. S. B.
    JOURNAL OF FLUID MECHANICS, 2011, 678 : 124 - 155
  • [44] Vertical two-phase flow. Part I: Flow regimes
    Chem Eng Res Des Trans Inst Chem Eng Pt A, A5 (612-619):
  • [45] Boundary-element analysis of planar drop deformation in confined flow. Part 1. Newtonian fluids
    Khayat, RE
    Luciani, A
    Utracki, LA
    ENGINEERING ANALYSIS WITH BOUNDARY ELEMENTS, 1997, 19 (04) : 279 - 289
  • [46] SIGNIFICANCE OF THE DIMENSIONLESS CONSTANT IN THE RATE EQUATION FOR SUPERPLASTIC FLOW.
    LANGDON, TERENCE G.
    1982, 13 (N 11): : 2059 - 2061
  • [47] NUMERICAL-ANALYSIS OF TRANSIENT FLOW-THROUGH A PIPE ORIFICE - (TIME CONSTANT FOR SETTLING FLOW)
    HAYASE, T
    CHENG, P
    HAYASHI, S
    JSME INTERNATIONAL JOURNAL SERIES B-FLUIDS AND THERMAL ENGINEERING, 1995, 38 (02): : 157 - 163
  • [48] FLOW REGIME IDENTIFICATION IN LARGE DIAMETER PIPE
    Sawant, Pravin
    Schelegel, Joshua
    Paranjape, Sidharth
    Ozar, Basar
    Hibiki, Takashi
    Ishii, Mamoru
    ICONE16: PROCEEDING OF THE 16TH INTERNATIONAL CONFERENCE ON NUCLEAR ENGINEERING - 2008, VOL 3, 2008, : 341 - 351
  • [49] VELOCITY FIELD OF THE FLOW AROUND A CIRCULAR CYLINDER STARTED IMPULSIVELY - 1. OUTER POTENTIAL FLOW.
    Nagata, Hiroshi
    Matsui, Tatsuya
    Yasuda, Haruo
    Bulletin of the JSME, 1980, 23 (179): : 687 - 695
  • [50] FLOW-INDUCED VIBRATIONS OF CIRCULAR CYLINDRICAL STRUCTURES - 1. STATIONARY FLUIDS AND PARALLEL FLOW.
    Chen, S.S.
    Shock and Vibration Digest, 1977, 9 (10): : 25 - 38