TECHNICAL PAPERS: Forced Convection

Fluctuating Temperature Measurements on a Heated Cylinder Placed in a Cylinder Near-Wake

[+] Author and Article Information
Z. J. Wang, Y. Zhou, X. W. Wang, W. Jin

Department of Mechanical Engineering, The Hong Kong Polytechnic University, Hung Hom, Kowloon, Hong Kong

J. Heat Transfer 126(1), 62-69 (Mar 10, 2004) (8 pages) doi:10.1115/1.1643910 History: Received June 26, 2003; Revised November 19, 2003; Online March 10, 2004
Copyright © 2004 by ASME
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Grahic Jump Location
Fiber-optic Bragg grating sensing system (adapted from Kersey et al. 23; Ho et al. 26). TOF denotes a tunable optical filter, and LP and HP stand for low pass and high pass, respectively.
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Experimental arrangement
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Schematic of test cylinders
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Laser-induced fluorescence flow visualization in the water tunnel behind two inline cylinders: (a) L/d=5.20; (b) 2.50; and (c) 1.18. Re=450. Flow is left to right.
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Time histories of u (the hot wire was placed at x/d=2 and y/d=1.5) and θs at α=85 deg. Time t=0 is arbitrary; (a) L/d=5.20; (b) L/d=2.50; and (c) L/d=1.18. The same scales are used in (a), (b), and (c) for u and θs.
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Power spectral density function Eθs of the fluctuating surface temperature θs at α=85° and Eu of the streamwise fluctuating velocity u: (a) Eθs; and (b) Eu. The hot wire was located at x/d=2 and y/d=1.5. –, L/d=5.20; [[dashed_line]], L/d=2.50; -⋅⋅-⋅⋅-, L/d=1.18.
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Spectral coherences Cohθsu between the fluctuating surface temperature θs at α=85 deg and the streamwise fluctuating velocity u. The hot wire was located at x/d=2 and y/d=1.5. –, L/d=5.20; [[dashed_line]], L/d=2.50; -⋅⋅-⋅⋅-, L/d=1.18.
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Co-spectrum Coθsu between the fluctuating surface temperature θs at α=85 deg and the streamwise fluctuating velocity u. The hot wire was located at x/d=2 and y/d=1.5. —, L/d=5.20; [[dashed_line]], L/d=2.50; -⋅⋅-⋅⋅-, L/d=1.18.
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Circumferential distributions of θs/Θ and Nu (from Adachi et al. 33) on an isolated cylinder. ♦, θs/Θ measured using the FBG sensor; ⋄, θs/Θ measured using a type-K thermocouple; ○, Nu at Re=5000; •, Nu at Re=11000.
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Circumferential distributions of the local time-averaged surface temperature θs/Θ measured using the FBG sensor. ○, L/d=5.20; ▴, L/d=2.50; ▵, L/d=1.18.Re=9080.
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Influence of L/d on the global mean surface temperature Θ of the downstream cylinder
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Circumferential distribution of the rms value θs,rms/Θ of the fluctuating surface temperature θs.Re=9080. ♦, Isolated cylinder; ○, L/d=5.20; ▴, L/d=2.50; ▵, L/d=1.18.




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