Open Access Open Access  Restricted Access Subscription Access

Heat Transfer and Fluid Flow Characteristics of Rib- Groove Roughened Solar Air Heater Ducts


Affiliations
1 Dept. of Mech. Engg,, Shri. G.S. Instt. of Technol. & Sc., Indore, India
2 Rajiv Gandhi Technical Univ., Bhopal, M.P.
 

The performance of solar air heater is considerably low due to the low value of convective heat transfer coefficient between the flowing air and the absorber plate. This is due to the formation of thin viscous sub-layer at the surface of the absorber plate. Artificial roughness is used to break the laminar viscous sub-layer formed on the absorber plate for increasing the level of turbulence to enhance the heat transfer. In the present work artificial roughness in the form of integral wedge shaped rib with and without groove has been employed on one of the heated broad wall of the rectangular duct to enhance the heat transfer. The wedge angle (Φ) was varied from 10 ° to 25° for relative roughness pitch (p/e) was kept as 8 and relative roughness height (e/D) was maintained as 0.033. The aspect ratio of the rectangular duct was maintained as 8. The Nusselt number and friction factor of the artificially roughened ducts were determined experimentally and the corresponding values were compared with that of smooth duct for the range of Reynolds number 3000-20000. The maximum enhancement in heat transfer was observed for the artificial roughness of wedge angle 15°. At the optimum angle of 15° a groove was incorporated. It was observed that wedge-groove roughened surface shows more enhancement in heat transfer compared to only rib roughened surface. The investigation revealed that Nusselt number increases 1.5-3 times of the smooth duct while the friction factor increases two to three folds that of the smooth duct in the range of operating parameters. The uncertainties in the measurements due to various instruments for the Reynolds number, Nusselt number and friction factor lies in the range of ± 3.8%, ± 3.54%, and ± 7.6%, respectively.

Keywords

Nusselt Number, Reynolds Number, Friction Factor, Solar Heater, Dryer
User

  • ASHRAE standards (1977) Methods of testing to determine the performance of solar air heater, 93-97.
  • Bhagoria JL, Saini JS and Solanki SC (2002) Heat transfer coefficient and friction factor correlation for rectangular solar air heater duct having transverse wedge shaped rib roughness on the absorber plate. J. Renewable Energy. 25, 341-369.
  • Duffie JA and Beckman WA (1980) Solar engineering of thermal processes. Wiely, New York.
  • Han JC, Glicksman LR and Rohsenow WM (1978) An investigation of heat transfer and friction for rib roughened surfaces. Trans. ASME J. Heat Transfer. 78, 1143-1156.
  • Hassan Ridouane EI and Campo A (2008) Heat transfer enhancement of air flowing across groovedchannels: joint effects of channel height and groove depth. ASME J. Heat transfer. 130./ 021901-1 to 7.
  • Jaurker AR, Saini JS and Gandhi BK (2006) Heat transfer coefficient and friction characteristics of rectangular solar air heater duct using rib-grooved artificial roughness. Intl.J. Solar Energy. 80, 895-907.
  • Kline SJ and Mc Clintock A (1953) The description of uncertainties in a single sample experiments. Mech. Engg. 75, 3-8.
  • Layek A, Saini JS andSolanki SC (2007) Heat transfer coefficient and friction characteristics of rectangular solar air heater duct using rib-grooved artificial roughness. Intl. J. Heat & Mass Transfer. 50,4845-4854.
  • Lewis MJ (1975) Optimizing the thermo hydraulic performance of rough surface. Intl. J. Heat & Mass Transfer. 18, 1243 -1248.
  • Prasad BN and Saini JS (1988) Effect of artificial roughness on heat transfer and friction factor in a solar air heater. Solar Energy. 41 (6), 555–560.
  • Prasad SB, Saini JS and Singh Krishna M (2009) Investigation of heat transfer and friction characteristics of packed bed solar air heater using wire mesh as packing material. Intl. J. Solar energy. 83, 773–783.
  • Tauscher R and Mayinger F (1995) Enhancement of heat transfer in plate heat exchanger by turbulence promoters. Proc. International Conf. on Compact Heat Exchanger for the Process Industries, Snowbird, Begell House, Inc., N.Y., USA.
  • Webb RL, Eckert ERG and Goldstein RJ (1971) Heat transfer and friction in tubes with repeated rib roughness. Intl. J. Heat & Mass Transfer. 14, 601-617.
  • Williams F, Pirie MAM and Warburton C (1970) Heat transfer from surfaces roughened by ribs. ASME Symp. Volume: Augmentation of Convective Heat & Mass Transfer.
  • Zang YM, Gu WZ and Han JC (1994) Heat transfer and friction in rectangular channel with ribbed or ribbed-grooved walls. ASME J. Heat Transfer. 116, 58-65.

Abstract Views: 450

PDF Views: 106




  • Heat Transfer and Fluid Flow Characteristics of Rib- Groove Roughened Solar Air Heater Ducts

Abstract Views: 450  |  PDF Views: 106

Authors

C. B. Pawar
Dept. of Mech. Engg,, Shri. G.S. Instt. of Technol. & Sc., Indore, India
K. R. Aharwal
Dept. of Mech. Engg,, Shri. G.S. Instt. of Technol. & Sc., Indore, India
Alok Chaube
Rajiv Gandhi Technical Univ., Bhopal, M.P.

Abstract


The performance of solar air heater is considerably low due to the low value of convective heat transfer coefficient between the flowing air and the absorber plate. This is due to the formation of thin viscous sub-layer at the surface of the absorber plate. Artificial roughness is used to break the laminar viscous sub-layer formed on the absorber plate for increasing the level of turbulence to enhance the heat transfer. In the present work artificial roughness in the form of integral wedge shaped rib with and without groove has been employed on one of the heated broad wall of the rectangular duct to enhance the heat transfer. The wedge angle (Φ) was varied from 10 ° to 25° for relative roughness pitch (p/e) was kept as 8 and relative roughness height (e/D) was maintained as 0.033. The aspect ratio of the rectangular duct was maintained as 8. The Nusselt number and friction factor of the artificially roughened ducts were determined experimentally and the corresponding values were compared with that of smooth duct for the range of Reynolds number 3000-20000. The maximum enhancement in heat transfer was observed for the artificial roughness of wedge angle 15°. At the optimum angle of 15° a groove was incorporated. It was observed that wedge-groove roughened surface shows more enhancement in heat transfer compared to only rib roughened surface. The investigation revealed that Nusselt number increases 1.5-3 times of the smooth duct while the friction factor increases two to three folds that of the smooth duct in the range of operating parameters. The uncertainties in the measurements due to various instruments for the Reynolds number, Nusselt number and friction factor lies in the range of ± 3.8%, ± 3.54%, and ± 7.6%, respectively.

Keywords


Nusselt Number, Reynolds Number, Friction Factor, Solar Heater, Dryer

References





DOI: https://doi.org/10.17485/ijst%2F2009%2Fv2i11%2F29537