Air flows in a cylindrical duct of diameter D = 6 in. At section ①, the turbulent boundary layer is of thickness δ 1 = 0.4 in. and the velocity in the inviscid central core is U 1 = 80 ft/s. Further downstream, at section ②, the boundary layer is of thickness δ 2 = 1.2 in. The velocity profile in the boundary layer is approximated well by the 1 7 -power expression. Find the velocity, U 2 , in the inviscid central core at the second section, and the pressure drop between the two sections. Does the magnitude of the pressure drop indicate that we are justified in approximating the flow between sections ① and ② as one with zero pressure gradient? Estimate the length of duct between sections ① and ②. Estimate the distance downstream from section ① at which the boundary layer thickness is δ = 0.6 in. Assume standard air.
Air flows in a cylindrical duct of diameter D = 6 in. At section ①, the turbulent boundary layer is of thickness δ 1 = 0.4 in. and the velocity in the inviscid central core is U 1 = 80 ft/s. Further downstream, at section ②, the boundary layer is of thickness δ 2 = 1.2 in. The velocity profile in the boundary layer is approximated well by the 1 7 -power expression. Find the velocity, U 2 , in the inviscid central core at the second section, and the pressure drop between the two sections. Does the magnitude of the pressure drop indicate that we are justified in approximating the flow between sections ① and ② as one with zero pressure gradient? Estimate the length of duct between sections ① and ②. Estimate the distance downstream from section ① at which the boundary layer thickness is δ = 0.6 in. Assume standard air.
Air flows in a cylindrical duct of diameter D = 6 in. At section ①, the turbulent boundary layer is of thickness δ1 = 0.4 in. and the velocity in the inviscid central core is U1 = 80 ft/s. Further downstream, at section ②, the boundary layer is of thickness δ2 = 1.2 in. The velocity profile in the boundary layer is approximated well by the
1
7
-power expression. Find the velocity, U2, in the inviscid central core at the second section, and the pressure drop between the two sections. Does the magnitude of the pressure drop indicate that we are justified in approximating the flow between sections ① and ② as one with zero pressure gradient? Estimate the length of duct between sections ① and ②. Estimate the distance downstream from section ① at which the boundary layer thickness is δ = 0.6 in. Assume standard air.
The wing of a tactical support aircraft is approximately rectangular with a wingspan (the length
perpendicular to the flow direction) of 16.5 m and a chord (the length parallel to the flow
direction) of 2.75 m. The airplane is flying at standard sea level with a velocity of 250 ms¯¹.
Assume the wing is approximated by a flat plate. Assume incompressible flow. Use μ =
1.789 x 10-5 kg/ms
(a) If the flow is considered to be completely laminar, calculate the boundary layer
thickness at the trailing edge and the total skin friction drag.
Air at 15°C forms a boundary layer near a solid wall. The velocity distribution
in the boundary layer is given by: u/U = 1- exp (-2y/8), where U 35 m/sec.
and 8 = 0.8 cm. Find the shear stress at wall (y 0).
A two-dimensional diverging duct is being designed to diffuse the high-speed air exiting a wind tunnel. The x-axis is the centerline of the duct (it is symmetric about the x-axis), and the top and bottom walls are to be curved in such a way that the axial wind speed u decreases approximately linearly from u1 = 300 m/s at section 1 to u2 = 100 m/s at section 2 . Meanwhile, the air density ? is to increase approximately linearly from ?1 = 0.85 kg/m3 at section 1 to ?2 = 1.2 kg/m3 at section 2. The diverging duct is 2.0 m long and is 1.60 m high at section 1 (only the upper half is sketched in Fig. P9–36; the halfheight at section 1 is 0.80 m). (a) Predict the y-component of velocity, ?(x, y), in the duct. (b) Plot the approximate shape of the duct, ignoring friction on the walls. (c) What should be the half-height of the duct at section 2?
Chapter 9 Solutions
Fox and McDonald's Introduction to Fluid Mechanics
Heating Ventilating and Air Conditioning: Analysis and Design
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