1 Turbulence Measurements in: Natural Convection Boundary Layer Swirling Jet by Abolfazl Shiri Thesis Supervisor William K. George Abolfazl SHIRI Feb. 19th, 2010 2 Turbulence Measurements in: Natural Convection Boundary Layer Swirling Jet Why we did these two experiments? • They were both turbulent flows and we aimed to measure the turbulence parameters. • There is a lack of reliable experimental data in both flows. • The velocity measurement method in both experiments was laser Doppler anemometry. • Both have axisymmetric nature which simplifies the three-dimensionality of the flow. • Doing a related experimental study while designing and installing the other experimental facility. Abolfazl SHIRI Feb. 19th, 2010 3 Swirling Jet Experiment • What is a jet flow? Jet flow represent a class of free shear flows that evolve in the absence of walls. Free Shear Flows Wakes Abolfazl SHIRI Jets Plumes Shear Layer Flows Feb. 19th, 2010 4 Anatomy of the Jet Flow Regions: • Potential core ( X/D ~ 1 ) • Mixing layer • Developing flow ( X/D ~ 20 ) • Self-preserving flow • Characteristic velocity scale • Characteristic jet width Uc(x) δ1/2(x) Asymptotic behaviour of flow at self-preserving region: U ( x, r ) r f( ) U c ( x) 1/ 2 Abolfazl SHIRI Feb. 19th, 2010 5 Entrainment Jet mass flow • Self-preserved region: When the mass entrained by the turbulence overwhelms the added mass at the source of jet. • Main application of jet flows in industry for mixing due to entrainment. • Laboratory jets can’t be categorized as universal self-similar, point-source of momentum jets. • Virtual origin (x0) and jet growth rate (dδ/dx) are the parameters characterizing the initial condition. • Azimuthal velocity component (swirl) modifies the initial condition. Abolfazl SHIRI Feb. 19th, 2010 6 Swirling Jet Flow • Two cases of low and moderate swirl (S = 0.15 & 0.25) were compared with a non-swirling jet. • Geometry of the nozzle and the velocity profile at the nozzle changes the initial condition. • How the additional swirl effects the nozzle velocity profile? Abolfazl SHIRI Not a top-hat anymore! Feb. 19th, 2010 7 Jet Facility • 1 inch jet nozzle diameter • Six injectors for tangential flow derived by different blower • 3.5m X 3.5m X 10m enclosure • Solid-body rotation for tangential velocity distribution • Reynolds number at nozzle: 40,000 • Same facility which used in Hussein, Capp & George 1994 for axisymmetric jets study. • Brought from university of Buffalo by George and modified to add the swirl components. Abolfazl SHIRI Feb. 19th, 2010 8 Summary of the Swirling Jet Experiment • The far swirling jet is self-similar (like the non-swirling jet). • For S < 0.2, the effect of initial swirl is negligible. • There is no considerable effect of swirl on growth rate, consistent with the theory. • The change in the virtual origin of these jets are slight (consistent with the relatively low swirl number) • U c 1/12 x 1 Wmax 1/ 22 x 2 • The role of each term (production, advection, diffusion and dissipation) is similar in both swirling and non-swirling jet. Abolfazl SHIRI Feb. 19th, 2010 9 Natural Convection Experiment Heat Transfer Modes Conduction Very Slow Process Forced Convection Convection + Natural Convection • Natural convection flows are among the least well undersood. No need for a medium to tranferthere the heat Radiation • Although they are the most commonly occuring method of convective heat transfer, is a lack of controlled and reliable experimental studies because of the difficulties. Abolfazl SHIRI Feb. 19th, 2010 10 Natural Convection Applications Natural-draft cooling tower Heat-sink Abolfazl SHIRI Reactor heat exchanger Radiator Feb. 19th, 2010 11 Some Definitions GrL g Ts T L3 2 Buoyancy forces Viscous forces GrL GrL Natural Natural 1 1 convection can Re 2 convection Re 2L L be neglected dominates Ra L GrL Pr For vertical surface, transition to turbulence at RaL 109 For a wall at T=70 C in air, transition starts at L 0.6 m Abolfazl SHIRI Feb. 19th, 2010 12 Theory of the NCBL Turbulent natural convection boundary layer flow next to a cylindrical surface: • Axisymmetric flow: homogeneous in tangential direction. • Newtonian, Incompressible flow. • Temperature gradient in the flow cause the density, viscosity and other thermodynamics properties variation. • Buoyancy as the source of momentum. To simplify the momentum and energy B.L. equation separation equations of the flow Inner layer → Viscous and conduction terms are dominating Outer layer → Viscous and conduction terms are negligible → For an acceptable seperation between the scales we need a really big Grashof number flow... This was primary reason for the large experimetal facility at Chalmers. Abolfazl SHIRI Feb. 19th, 2010 13 Experimental Rig Previous experiments: • Most of the experiments were carried out next to a vertical flat plate: Tsuji & Nagano (1988) • Measurements on vertical cylinder by Persson & Karlsson (1996) were problematic: – Low Grashof number – Boundary conditions were not controlled. New experimental facility was built to modify the rig used by Persson & Karlsson Abolfazl SHIRI Feb. 19th, 2010 14 Experimental Rig Schematic Abolfazl SHIRI Feb. 19th, 2010 15 Measurement Methods Velocity measurement: Laser Doppler Anemometry (LDA) Thermocouple Temperature measurement: mean temperature Cold-wire thermometry instantaneous temperature Abolfazl SHIRI Feb. 19th, 2010 16 Temperature Measurement Errors • Prongs temperature gradient. • Wall temperature measurement errors. • Calibration uncertainities. • Temperature measurement errors in very low velocity fluids. Abolfazl SHIRI Feb. 19th, 2010 17 Summary of the NCBL Experiment • The experiments were carried out in three different heights: 1.5m, 3m and 4m corresponding to the Rayleigh numbers: Ra = 1.0 × 1010 , 7 × 1010 and 1.7 × 1011 respectively. • Simultaneous two components velocity and temperature measured across boundary layer in turbulent region. • Temperature measurement methods were not suitable for this flow, but lack of any other alternative method with the necessary accuracy forced us to use them, considering the short comings. • A comprehensive theoritical foundation was established for future investigations. Abolfazl SHIRI Feb. 19th, 2010 18 In Memory of Professor Rolf Karlsson (1945 – 2005) Abolfazl SHIRI Feb. 19th, 2010