Heat Transfer from a Cylinder in Cross-Flow of Single and Multiphase Flows

In this paper, the average heat transfer characteristics
for a cross flow cylinder of 16 mm diameter in a vertical pipe has
been studied for single-phase flow (water/oil) and multicomponent
(non-boiling) flow (water-air, water-oil, oil-air and water-oil-air). The
cylinder is uniformly heated by electrical heater placed at the centre
of the element. The results show that the values of average heat
transfer coefficients for water are around four times the values for oil
flow. Introducing air as a second phase with water has very little
effect on heat transfer rate, while the heat transfer increased by 70%
in case of oil. For water–oil flow, the heat transfer coefficient values
are reflecting the percentage of water up to 50%, but increasing the
water more than 50% leads to a sharp increase in the heat transfer
coefficients to become close to the values of pure water. The
enhancement of heat transfer by mixing two phases may be attributed
to the changes in flow structure near to cylinder surface which lead to
thinner boundary layer and higher turbulence. For three-phase flow,
the heat transfer coefficients for all cases fall within the limit of
single-phase flow of water and oil and are very close to pure water
values. The net effect of the turbulence augmentation due to the
introduction of air and the attenuation due to the introduction of oil
leads to a thinner boundary layer of oil over the cylinder surface
covered by a mixture of water and air bubbles.

Authors:



References:
[1] Zukauskas, A. A., 1972, Heat transfer from tubes in cross-flow, Adv.
Heat Transfer 8, 93–160.
[2] Morgan, V. T., 1975, The overall convective heat transfer from smooth
circular cylinders, Adv. Heat Transfer 11. 199-264.
[3] Zukauskas, A. A., Ziugzda, J., 1985, Heat transfer of a cylinder in crossflow,
Hemisphere Publishing Corporation,
[4] Sanitjai, S., Goldstein, R.J., 2004a, Forced convection heat transfer from
a circular cylinder in cross-flow to air and liquids, Int. J. Heat Mass
Transfer 47, 4785-4794.
[5] Hoelscher, J. F., 1965, study of heat transfer from heated cylinder in
two-phase flow, water-air flow, MSc thesis, Air Force Institute of
Technology, Ohio.
[6] Takahara, E. W., 1966, Experimental study of heat transfer from a
heated circular cylinder in two-phase, water-air flow, MSc thesis, Air
Force Institute of Technology, Ohio.
[7] V. P. Bobkov, V. F. Sinyavskii, and N. K. Savanin, Effect of gas phase
on heat transfer in turbulent water flow in a model of compact triangular
rod bundle, Translated from Inzhenerno-Fizicheskie Zhurnal 44 (1972),
pp.362-367.
[8] Sanitjai, S., Goldstein, R.J., 2004b, Heat transfer from a circular cylinder
to mixtures of water and ethylene glycol, Int. J. Heat Mass Transfer 47,
4795-4805.
[9] Hu, Z., Yang Y., Zhou, F., 2005, Study on the heat transfer of cross flow
in vertical upward tubes, Journal of Zhejiang University Science 24,
1128-1131.
[10] Fand, R. M., 1965, Heat transfer by forced convection from a cylinder to
water in cross-flow. Int. J. Heat Mass Transfer 8, 995–1010.
[11] Whitaker, S., 1972, Forced convection heat transfer calculations for flow
in pipes, past flat plate, single cylinder, and for flow in packed beds and
tube bundles. AIChE Journal 18, 361–371.
[12] Theofanous T. G., Sullivan, J., 1982, Turbulence in two-phase dispersed
flows”, J. Fluid Mechanics 116, 343-362.
[13] Wang, S. K., Lee, S. J., Jones, O. C., Lahey, R.T., 1987, 3-D turbulence
structure and phase distribution measurements in bubbly two-phase
flows”, Int. J. Multiphase Flow 13, 327-343.
[14] Shawkat, M. E., Ching, C. Y., Shoukri, M., 2007, On the liquid
turbulence energy spectra in two-phase bubbly flow in a large diameter
vertical pipe, Int. J. Multiphase Flow 33, 300-316.
[15] Ghisalberti, L., Kondjoyan, A., 1999, Convective heat transfer
coefficients between air flow and a short cylinder. Effect of air velocity
and turbulence, effect of body shape, dimensions and position in the
flow, Journal of Food Engineering 42, 33-44.
[16] Liu T. J., Bankoff, S.G., 1993, Structure of air-water bubbly flow in
vertical pipe-II. void fraction, bubble velocity, and bubble size
distribution”, Int. J. Heat and Mass Transfer 36, 1061-1072.
[17] Zhao, D., Guo, L., Hu, X., Zhang, X., Wang, X, 2006, Experimental
study on local characteristics of oil-water dispersed flow in a vertical
pipe”, Int. J. Multiphase Flow 32, 1254-1268.
[18] Hamad, F. H., Dlir A., Ganesan, P. B., 2014, Study of kerosene-water
two-phase flow characteristics in vertical and inclined pipes, Can. J.
Chem Eng, 92, 905-917.
[19] Krepper, E., Beyer, M., Frank, T., Lucas, D., Prasser, H., 2009, CFD
modelling of polydispersed bubbly two-phase flow around an obstacle,
Nuclear Engineering and Design 239, 2372–2381.
[20] Habeeb, L. J., Al-Turaihi, R. S., 2013, Experimental study and CFD
simulation of two-phase flow around multi-shape obstacles in enlarging
channel, American Journal of Mechanical Engineering 1, 470-486
[21] Alagesan V., Sundaram, S., 2012, Two-phase experimental heat transfer
studies on a water-diesel system in a shell and tube heat exchanger 29,
275-283.