Numerical Analysis of Impact of Relative Humidity on Crossflow Heat Exchangers with Staggered Configuration at Maximum Operating Temperature

Authors

  • Arshan Ahmed Department of Mechanical Engineering, NUST College of Electrical and Mechanical Engineering, National University of Sciences and Technology, Islamabad, Pakistan.
  • Atta ul Mannan Hashmi Department of Mechanical Engineering, NUST College of Electrical and Mechanical Engineering, National University of Sciences and Technology, Islamabad, Pakistan.
  • Fahad Rafi Butt Research Associate, Digital Pakistan Lab, NUST College of Electrical and Mechanical Engineering, National University of Sciences and Technology, Islamabad, Pakistan.
  • Shahbaz Ghani Department of Mechanical Engineering, NUST College of Electrical and Mechanical Engineering, National University of Sciences and Technology, Islamabad, Pakistan
  • Imran Akhtar Department of Mechanical Engineering, NUST College of Electrical and Mechanical Department of Mechanical Engineering, NUST College of Electrical and Mechanical Engineering, National University of Sciences and Technology, Islamabad, Pakistan

Keywords:

Heat transfer, relative humidity, Nusselt number, Prandtl number, Reynolds number

Abstract

Heat exchangers are employed in numerous applications of industry, automotive and air conditioning systems. The efficacy of heat exchangers depends upon various factors e.g., Reynolds number (Re) of the fluids, geometry of heat exchanging surfaces, and the Prandtl number of the cooling air. In this paper, the working of a crossflow heat exchanger with elliptical tubes is simulated numerically for 5000 < Re < 20000 at its maximum operating temperature of 323K. The tubes were arranged in a staggered way. The radical investigations were done at one-of-a-kind relative humidity ranges within the cooling air ranging from 0% to 80%. The relative humidity was modeled in the shape of mass fractions of water vapors in the air. The thermos-physical properties of dry and moist air were employed for the analysis. The impact of this changing of relative humidity on forced convection heat transfer of heat exchangers is examined in the form of percentage change in Nusselt number. With the increase in moisture content in the air, the Nusselt number was observed increased up to 4.5%. The paper provides a tool to analyze the Nusselt number of the elliptical-shaped heat exchanger while operating in moist atmospheric conditions.

Full Text

References

H. Suyi and P. Shizhou, “Convection and heat transfer of elliptical tubes” “Heat Mass Transfer” 1995, vol. 30, no. 6, pp. 411–415.

C. R. Iskra and C. J. Simonson, “Effect of humidity on the convective mass transfer coefficient in a rectangular duct” “Saudi Medical Journal” 2012, vol. 33, pp. 3–8.

E. Reynoso-jardón, G. Urquiza, O. Tenango-pirin, and Y. Mariaca-beltrán, “Numerical study of a cross flow heat exchanger varying the transverse and longitudinal space to increase heat transfer” “International Journal of Combinatorial Optimization Problems and Informatics” 2020, vol. 11, pp. 106–114.

S. A. E. Sayed Ahmed, E. Z. Ibrahiem, O. M. Mesalhy, and M. A. Abdelatief, “Heat transfer characteristics of staggered wing-shaped tubes bundle at different angles of attack,” “Heat Mass Transfer” 2014, vol. 50, no. 8, pp. 1091–1102.

T. Kanthimathi, P. Bhramara, and G. N. S. Ram, “Numerical analysis on the effect of heat Transfer rate by varying the tube arrays in a cross-flow heat exchanger” “International Journal of Scientific & Engineering Research” 2016, vol. 7, no. 6, pp. 13–16.

N. El Gharbi, A. Kheiri, M. El Ganaoui, and R. Blanchard, “Numerical optimization of heat exchangers with circular and non-circular shapes” “Case Studies in Thermal Engineering” 2015, vol. 6, pp. 194–203.

M. Still, H. Venzke, F. Durst, and A. Melling, “Influence of humidity on the convective heat transfer from small cylinders” “Experiments in Fluids” 1998, vol. 24, no. 2, pp. 141–150.

D. Uguru-okorie and I. Ikpotokin, “Experimental comparison of staggered and in-line tube- bank thermal performance” “International Journal of Mechanical Engineering and Technology” 2018, vol. 9, pp. 1061–1070.

J. Zhang, A. Gupta, and J. Baker, “Effect of relative humidity on the prediction of natural convection heat transfer coefficients” “Heat Transfer Engineering” 2007, vol. 28, no. 4, pp. 335– 342.

B. Prasad, A. Tawfek, and V. Rao, “Heat transfer from aero foils in cross-flow” “International Communications in Heat and Mass Transfer” 1992, vol. 19, no. 6, pp. 879– 890.

P. T. Tsilingiris, “Thermo-physical and transport properties of humid air at temperature range between 0 and 100°C” “Energy Conservation and Management” 2008, vol. 49, no. 5, pp. 1098–1110.

Water moisture content of humid air calculator, http://www.quadco.engineering.com/en/know-how/cfd-calculate-water-fraction-humid-air. html.

ANSYS Inc, “ANSYS Fluent® User’s Guide” 2013, Release 15.

L. M. Smith and W. C. Reynolds, “On the Yakhot-Orszag renormalization group method for deriving turbulence statistics and models,” “Physics of Fluids A: Fluid Dynamics” 1992, vol. 4, no. 2, pp. 364–390.

Importance of mesh independence study & why you should care, https://www. maxshear.com/training/importance-of-mesh-independence-study-amp-why-you-should-doit.

F. P. Incropera, D. P. Dewitt, T. L. Bergman, and A. S. Lavine, “Fundamentals of heat and mass transfer” “John Willey & Sons” 2006, ed. 6th, p. 370.

A. Zukauskas, “Heat Transfer from tubes in crossflow” “Advances in Heat Transfer” 1972, vol. 8, pp. 93–160.

Downloads

Published

2022-01-14

How to Cite

Ahmed, A., Hashmi, A. ul M. ., Butt, F. R., Ghani, S., & Akhtar, I. (2022). Numerical Analysis of Impact of Relative Humidity on Crossflow Heat Exchangers with Staggered Configuration at Maximum Operating Temperature. International Journal of Innovations in Science & Technology, 3(4), 84–95. Retrieved from https://journal.50sea.com/index.php/IJIST/article/view/117