Photographs are presented for secondary flow patterns in a straight tube (x/d = 0 ∼ 70) downstream of a 180 deg bend (tube inside diameter d = 2.54 cm, radius of curvature Rc = 12.7 cm) and in an isothermally heated horizontal tube (tube inside diameter d = 2.54 cm, heated length l = 46.2 cm) with free convection effects. Each test section is preceded by a long entrance length with air as the flowing fluid. For curved pipes, the Dean number range is K = 99 to 384. At the exit of the 180 deg bend, the onset of centrifugal instability in the form of an additional pair of Dean vortices near the central outer wall occurs at a Dean number of about K = 100. The developing secondary flow patterns in the thermal entrance region of an isothermally heated horizontal tube are shown for the dimensionless axial distance z = 0.8 × 10−2 to 1.83 (Re = 3134 ∼ 14) for a range of constant wall temperatures Tw = 55 ∼ 65° C with entrance air temperature at about 25° C. The secondary flow patterns shown are useful for future comparisons with predictions from numerical solutions.
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Flow Visualization Studies on Secondary Flow Patterns in Straight Tubes Downstream of a 180 deg Bend and in Isothermally Heated Horizontal Tubes
K. C. Cheng,
K. C. Cheng
Department of Mechanical Engineering, University of Alberta, Edmonton, Alberta, Canada
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F. P. Yuen
F. P. Yuen
Department of Mechanical Engineering, University of Alberta, Edmonton, Alberta, Canada
Search for other works by this author on:
K. C. Cheng
Department of Mechanical Engineering, University of Alberta, Edmonton, Alberta, Canada
F. P. Yuen
Department of Mechanical Engineering, University of Alberta, Edmonton, Alberta, Canada
J. Heat Transfer. Feb 1987, 109(1): 49-54 (6 pages)
Published Online: February 1, 1987
Article history
Received:
April 24, 1984
Online:
October 20, 2009
Citation
Cheng, K. C., and Yuen, F. P. (February 1, 1987). "Flow Visualization Studies on Secondary Flow Patterns in Straight Tubes Downstream of a 180 deg Bend and in Isothermally Heated Horizontal Tubes." ASME. J. Heat Transfer. February 1987; 109(1): 49–54. https://doi.org/10.1115/1.3248066
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