EXPERIMENTAL VALIDATION OF LMTD METHOD FOR MICROSCALE HEAT TRANSFER

The single phase fluid flow and heat transfer characteristic has been investigated experimentally. Experiments were conducted to cover transition zone for the Reynolds numbers ranging from 100 to 4800 by fused silica and stainless steel microtubes having diameters of 103-180 µm. The applicability of the Logarithmic Mean Temperature Difference (LMTD) method was revealed and an experimental method was developed to calculate the heat transfer coefficient. Moreover the scaling effects in micro scale such as axial conduction, viscous heating and entrance effects were discussed. The heat transfer coefficients were compared with data obtained by the correlations available in the literature in the study. The Nusselt numbers of microtube flows do not accord with the conventional results when the Reynolds number was lower than 1000. After that, the Nusselt number approaches the conventional theory prediction. On the aspect of fluid characteristics, the friction factor was well predicted with conventional theory and the conventional friction prediction was valid for water flow through microtube with a relative surface roughness less than about 4 %.

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  • [1] Kandlikar S.G., Heat Transfer and Fluid Flow in Minichannels and Microchannels (Second Edition), Chapter 3, Single-Phase Liquid Flow in Minichannels and Microchannels, Pages 103–174, 2014.
  • [2] Adams T M, Abdel-Khalik S I, Jeter S. M, Qureshi Z H. (1998) An experimental investigation of single-phase forced convection in microchannels. Int J Heat Mass Transfer; 41: (6–7) 851–857.
  • [3] Yu D, Warrington R, Barron R, Ameel T. (1995) An experimental investigation of fluid flow and heat transfer in microtubes. Proceedings of the ASME/JSME Thermal Engineering Conference, Vol. 1. American Society of Mechanical Engineers, pp. 523-530.
  • [4] Celata G P, Cumo M, Guglielmi M, Zummo G. (2002) Experimental investigation of hydraulic and single phase heat transfer in 0.130 µm capillary tube. MicroscaleThermophys Eng; 6: 85–97.
  • [5] Tso C P, Mahulikar S P, (1998) The use of Brinkman number for single phase forced convective heat transfer in microchannels. Int J Heat Mass Transf; 41: 1759-1769.
  • [6] Lelea D, Nishio S, Takano K. (2004) The experimental research on microtube heat transfer and fluid flow of distilled water. Int J Heat Mass Transfer; 47: 2817–2830.
  • [7] Celata G P, Morini G L, Marconi V, McPhail S J, Zummo G. (2006) Using viscous heating to determine the friction factor in microchannels – An experimental validation. Experimental Thermal and Fluid Science; 30: 725–731.
  • [8] Li Z, He Y L, Tang G H, Tao W Q. (2007) Experimental and numerical studies of liquid flow and heat transfer in microtubes. Int J Heat Mass Transfer; 50: 3447–3460.
  • [9] Zhigang L, Ning G, Chengwu Z, Xiaobao Z. (2009) Experimental study on flow and heat transfer in a 19.6 µm microtube. Experimental Heat Transfer; 22: 178-197.
  • [10] Parlak N, Gür M, Arı V, Küçük H, Engin T. (2010) Second law analysis of water flow through smooth microtubes under adiabatic conditions. Experimental Thermal and Fluid Science; 35: 60-67.