Contribution in Unsteady Flow of Power-Law Fluids

AIAA Journal ◽  
1973 ◽  
Vol 11 (2) ◽  
pp. 238-239 ◽  
Author(s):  
SREEDHAN ROY
1993 ◽  
Vol 115 (2) ◽  
pp. 330-333 ◽  
Author(s):  
Ali J. Chamkha

Equations governing flow of a particulate suspension exhibiting finite volume fraction in non-Newtonian power-law fluids are developed and applied to the problem of unsteady flow past an infinite porous flat plate with suction. Numerical results for small volume fraction for the displacement thicknesses for both phases and the skin-friction coefficient for the fluid phase are obtained using an implicit finite difference scheme and presented graphically to elucidate interesting features of the solutions.


AIAA Journal ◽  
1972 ◽  
Vol 10 (5) ◽  
pp. 689-691 ◽  
Author(s):  
TOMMY Y.W. CHEN ◽  
DAVID E. WOLLERSHEIM

2009 ◽  
Vol 64 (12) ◽  
pp. 2978-2999 ◽  
Author(s):  
Vijaya K. Patnana ◽  
Ram P. Bharti ◽  
Raj P. Chhabra

AIAA Journal ◽  
1973 ◽  
Vol 11 (11) ◽  
pp. 1588-1588
Author(s):  
I. S. HABIB ◽  
T. Y. NA

2017 ◽  
Vol 20 (12) ◽  
pp. 1071-1086 ◽  
Author(s):  
Ming-Qing Kui ◽  
Xiao-Hua Tan ◽  
Xiao-Ping Li ◽  
Jianchao Cai

Author(s):  
Jaspinder Kaur ◽  
Roderick Melnik ◽  
Anurag Kumar Tiwari

Abstract In this present work, forced convection heat transfer from a heated blunt-headed cylinder in power-law fluids has been investigated numerically over the range of parameters, namely, Reynolds number (Re): 1–40, Prandtl number (Pr): 10–100 and power-law index (n): 0.3–1.8. The results are expressed in terms of local parameters, like streamline, isotherm, pressure coefficient, and local Nusselt number and global parameters, like wake length, drag coefficient, and average Nusselt number. The length of the recirculation zone on the rear side of the cylinder increases with the increasing value of Re and n. The effect of the total drag coefficient acting on the cylinder is seen to be higher at the low value of Re and its effect significant in shear-thinning fluids (n < 1). On the heat transfer aspect, the rate of heat transfer in fluids is increased by increasing the value of Re and Pr. The effect of heat transfer is enhanced in shear-thinning fluids up to ∼ 40% and it impedes it’s to ∼20% shear-thickening fluids. In the end, the numerical results of the total drag coefficient and average Nusselt number (in terms of J H −factor) have been correlated by simple expression to estimate the intermediate value for the new application.


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