Compressible laminar motion with fluctuation in free stream temperature

1963 ◽  
Vol 11 (1) ◽  
pp. 104-108
Author(s):  
S. L. Soo
1968 ◽  
Vol 90 (1) ◽  
pp. 109-114 ◽  
Author(s):  
Ahmed R. Wazzan ◽  
T. Okamura ◽  
A. M. O. Smith

The theory of two-dimensional instability of laminar flow of water over solid surfaces is extended to include the effects of heat transfer. The equation that governs the stability of these flows to Tollmien-Schlichting disturbances is the Orr-Sommerfeld equation “modified” to include the effect of viscosity variation with temperature. Numerical solutions to this equation at high Reynolds numbers are obtained using a new method of integration. The method makes use of the Gram-Schmidt orthogonalization technique to obtain linearly independent solutions upon numerically integrating the “modified Orr-Sommerfeld” equation using single precision arithmetic. The method leads to satisfactory answers for Reynolds numbers as high as Rδ* = 100,000. The analysis is applied to the case of flow over both heated and cooled flat plates. The results indicate that heating and cooling of the wall have a large influence on the stability of boundary-layer flow in water. At a free-stream temperature of 60 deg F and wall temperatures of 60, 90, 120, 135, 150, 200, and 300deg F, the critical Reynolds numbers Rδ* are 520, 7200, 15200, 15600, 14800, 10250, and 4600, respectively. At a free-stream temperature of 200F and wall temperature of 60 deg F (cooled case), the critical Reynolds number is 151. Therefore, it is evident that a heated wall has a stabilizing effect, whereas a cooled wall has a destabilizing effect. These stability calculations show that heating increases the critical Reynolds number to a maximum value (Rδ* max = 15,700 at a temperature of TW = 130 deg F) but that further heating decreases the critical Reynolds number. In order to determine the influence of the viscosity derivatives upon the results, the critical Reynolds number for the heated case of T∞ = 40 and TW = 130 deg F was determined using (a) the Orr-Sommerfeld equation and (b) the present governing equation. The resulting critical Reynolds numbers are Rδ* = 140,000 and 16,200, respectively. Therefore, it is concluded that the terms pertaining to the first and second derivatives of the viscosity have a considerable destabilizing influence.


Author(s):  
X. J. Gu ◽  
D. R. Emerson

Abstract A high-order moment method is employed to study the effect of the wall temperature on gas flow past a stationary circular cylinder in terms of the size of the vortices behind the cylinder and the drag coefficient. When the wall temperature is lower than the free stream temperature, flow separation occurs at a lower Reynolds number and the vortex length is elongated with a corresponding reduction in the drag coefficient. Conversely, increasing the wall temperature above the free stream temperature delays the onset of flow separation and increases the drag coefficient.


1987 ◽  
Vol 109 (2) ◽  
pp. 75-78
Author(s):  
M. A. Abdrabboh ◽  
G. A. Karim

Clusters of preshaped oil sand spherical fragments were subjected to hot steady streams of air at low Reynolds number and constant stream temperature. A wide range of different combinations and arrangements of these fragments were employed involving up to twenty identical spherical samples that were either piled or set normal to the free stream of air and left exposed for various prescribed time periods at constant stream temperatures. The rates of mass loss due to fluid volatilization off these clusters during this exposure were then established experimentally and compared with the corresponding rates derived from the behavior of single spheres. This comparison showed, for the cases considered in this investigation, essentially no significant effect due to the interaction of the spherical samples with each other. The behavior of a single fragment can then form the basis for establishing the volatilization rate of the cluster. However, it was shown that the confinement of these clusters of fragments within a cylindrical tube placed axially along the heating stream produced appreciable effects on the rates of volatilization. The extent of the deviation from the single fragment model observed was then examined and a number of variables affecting it identified.


1959 ◽  
Vol 26 (2) ◽  
pp. 161-165
Author(s):  
E. M. Sparrow ◽  
J. L. Gregg

Abstract An analysis is made for laminar forced-convection heat transfer from a flat plate to a nonisothermal free stream. An exact solution of the boundary-layer energy equation is found for the situation of linearly varying free-stream temperature. Numerical calculations are carried out for Prandtl numbers in the range 0.01 ⩽ Pr ⩽ 50. Results are presented for the change in heat transfer due to the variation in free-stream temperature. This effect decreases with increasing Prandtl number.


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