Heat Transfer Studies and Applications by Salim Newaz Kazi

By Salim Newaz Kazi

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J. Acoust. Soc. Am. 2004;(115): 2873-2886. [5] Marquardt ED, Radebaugh R. Compact high effectiveness parallel plate heat ex‐ changers. In Ross Jr. RG, editor. Cryocoolers 12. G. Ross Jr. : Kluwer Academic/ Plenum Publishers; 2003. 507-516. [6] Nellis GF. A heat exchanger model that includes axial conduction, parasitic heat loads, and property variations. ; 2003. 523-538. [7] Radebaugh R. Microscale heat transfer at low temperatures. In Kakaç S, Vasiliev LL, Bayazitoğlu Y, Yener Y, editors. : Springer Netherlands 93-124.

Fluid Mech. 1976; 76(4): 801-817. [22] Wang CY. Drag due to a striated boundary in slow Couette flow. Phys. Fluids. 1978; 21: 697-698. [23] Orszag SA, Kells LC. Transition to turbulence in plane Poiseuille and plane Couette flow. J. Fluid Mech. 1980; 96(1): 159-205. [24] Richardson S. On the no-slip boundary condition. Journal of Fluid Mechanics. 1973; 59(04): 707-719. 31 32 Heat Transfer Studies and Applications [25] Luccini P, Manzo F, Pozzi A. Resistance of a grooved surface to parallel flow and cross-flow.

3. Effect of interaction on Nus Figure 9 shows the distributions of the span-averaged values of Nus at Re = 600 and 1800 for different values of c. The value of Nus for plain fin without VGs is also shown in the figure for comparison. The span-averaged values of Nus are obviously enhanced by the longitudinal vortices generated by the VGs mounted in the channel. In the entrance of the channel, the fluid flows in at a uniform velocity, the boundary layer starts to develop, and the value of Nus gets the largest value.

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