Heat transfer distributions are presented for a rectangular duct with two opposite wide walls arranged with V-shaped ribs pointing upstream or downstream relative to the main¯ow direction. The rectangular duct has an aspect ratio of 1/8. The parallel V-shaped circular ribs are arranged staggered on the two wide walls. The rib height-to-hydraulic diameter ratio is 0.06, with an attack angle of 60°. The pitch-to-height ratio equals 10. The tested Reynolds numbers range from 1000 to 6000. The test surface is sprayed with black paint and then liquid crystal, and a steady state method is adopted to obtain the temperature distribution between adjacent ribs. The secondary¯ow caused by the angled ribs creates different spanwise variation of the heat transfer coef®cient on the rib-roughened wall for different V-rib orientations. Interaction between heat transfer and secondary¯ow is analyzed. In the streamwise direction, the temperature distribution shows a sawtooth behavior between a pair of adjacent ribs. Local Nusselt numbers are presented between a pair of adjacent ribs, and based on these the average Nusselt numbers are calculated to investigate the augmentation of heat transfer by the presence of the V-shaped ribs.
IntroductionPeriodic ribs are frequently employed in heat exchangers to enhance the heat transfer process. The heat transfer distribution and enhancement caused by parallel ribs has been investigated [1]. V-shaped ribs originated from the concept that angled ribs can act as longitudinal vortex generator and provide heat transfer augmentation. It is then assumed that V-shaped ribs can principally double the high heat transfer region and provide even higher heat transfer coef®cients (see, e.g., [2]). Because the¯ow ®eld is disturbed by the presence of the ribs and the orientation of the V-shaped ribs will induce different types of secondarȳ ow, and the local heat transfer distributions are also different.Han et al. used thermocouples to investigate the heat transfer of a square duct with 45 and 60°V-shaped ribs, and the ribs could point in the main¯ow direction or in the opposite direction [3]. The ribbed walls were in-line and the Reynolds number covered the range of 15 000± 90 000. The V-shaped ribs directed opposite to the main ow provided the highest heat transfer enhancement. Taslim et al. employed liquid crystal thermography to study the heat transfer enhancement caused by V-shaped ribs on two opposite walls of a square duct [2]. The 45°angled ribs were arranged with a ®xed pitch-to-height ratio of 10. In the whole Reynolds number range of 5000±30 000, for the blockage ratio (e/D h ) of 0.083, it was revealed that V-shaped ribs pointing downstream produced the highest heat transfer enhancement. These results contradict those of [3]. In another investigation, Ekkad and Han measured the heat transfer of a two-pass square duct with 60°V-ribs using liquid crystal thermography. The Reynolds numbers were from 6000 to 60 000 [4]. The Nusselt number ratio distributions for the ®rst pass with V-ribs pointing in...