WALL FREE SHEAR FLOW
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This study uses laser-induced fluorescence technique to visualize the turbulent flow of an axisymmetric water jet. The fractal dimension of the scalar interface in turbulent flows is measured and interpreted.
WALL FREE SHEAR FLOW
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WALL FREE SHEAR FLOW Turbulent flows free of solid boundaries Irrotational JET y x Turbulent Two-dimensional image of an axisymmetric water jet, obtained by the laser-induced fluorescence technique. (From R. R. Prasad and K. R. Sreenivasan, Measurement and interpretation of fractal dimension of the scalar interface in turbulent flows, Phys. Fluids A, 2:792–807, 1990)
WAKE http://www.ifh.uni-karlsruhe.de/science/envflu/
x Laser-Induced Fluorescence (LIF) VISUALIZATION OF AN AXISYMMETRIC TURBULENT JET, C. Fukushima and J. Westerweel, Technical University of Delft, The Netherlands
Turbulent Kinetic Energy (q2) Balance in a Jet x Laser-Induced Fluorescence (LIF) VISUALIZATION OF AN AXISYMMETRIC TURBULENT JET, C. Fukushima and J. Westerweel, Technical University of Delft, The Netherlands
q2 <v2 > <u2 > y m2/s2 <w2 > x -<uv> y
Turbulent Kinetic Energy (q2) Balance in a Jet x No local accelerations No viscous transport Part of the shear production = 0 No buoyancy production Laser-Induced Fluorescence (LIF) VISUALIZATION OF AN AXISYMMETRIC TURBULENT JET, C. Fukushima and J. Westerweel, Technical University of Delft, The Netherlands
Gain y m2/s3 x y Loss
WALL-BOUNDED SHEAR FLOW 0.99U0 http://www.symscape.com/node/447 Nominal limit of boundary layer U0 Viscous sublayer For fully developed, bounded turbulent flow (not changing in x): viscous Reynolds
Function of z only Function of x only Stress distribution is then LINEAR z CONSTANTS! centerline or surface
in boundary layer over flat plate (no press grad): stress is now a function of x and z z z edge of boundary layer
Near the wall – Different Layers z ū (x) Only involve mass dimension u(x,z) Should appear together in nondimensional groups Friction Velocity http://furtech.typepad.com/
This relates 4 variables involving the dimensions of length and time According to the PI THEOREM, this relationship has 4 variables and 2 dimensions Then, only two (4 – 2) non-dimensional groups can result: Law of the Wall Z+ is a distance nondimensionalized by the viscous scale Inner part of the wall layer, right next to the wall, is called the viscous sublayer– dominated by viscous effects
z (m) = z+ν/u* viscous sublayer buffer layer logarithmic layer
outer layer Velocity defect law Equating and multiplying times z/u* logarithmic layer Karman constant = 0.41 buffer layer viscous sublayer Law of the wall
Karman constant = 0.41 Integrating: From experiments: Velocity distributions for the Overlap layer, Inertialsublayer, Logarithmic layer Logarithmic velocity distribution near a boundary can also be derived from dimensional analysis
can only depend on z, and the only relevant velocity scale is u*
Data from Ponce de Leon Inlet Florida FloridaIntracoastal Waterway