Consider a thin,
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Fundamentals of Heat and Mass Transfer
- Experimental measurements of the convection heat transfer coefficient for a square bar in cross flow yielded the following values: Assume that the functional form of the Nusselt number is Nu = C*Rem*Prn, where C, m, and n are constants. Also, assume that air temperature does not change in the following problem.A. What will be the convection heat transfer coefficient for a similar bar with L = 1 m when V = 15 m/s?B. What will be the convection heat transfer coefficient for a similar bar with L = 1 m when V = 30 m/s?arrow_forwardIn elementary mechanical fluidarrow_forwardProblem 1. A smooth plate with length L = 3.0 m and width 6 = 0.90 m moves through still air at STP at a velocity of U = 4.5 m/s that is aligned with L. Calculate the following for a boundary layer that stays laminar and for one that trips to turbulent at the leading edge: (a) boundary layer disturbance thickness, &, at x = 0.5, 1.0, 1.5, 2.0, 2.5, and 3.0 m from the leading edge of the plate, (b) wall shear stress, Tw, at those x- locations, and (c) friction drag, FD,f, on one side of plate. (d) Calculate percent decrease in drag for laminar versus turbulent boundary layer.arrow_forward
- 6- A uniform free stream of air at 0.8 m/s flows over a flat plate (4 m long x 1 m wide). Assuming the boundary layer to be laminar on the plate and the velocity profile is: Find the ratio of the drag force on the front half portion to the drag U. 2 force on the rear half portion of the plate. (p = 1.2 kg/m; v = 1.51x10 m²/s) [2.42]arrow_forwardProblem 9. Assume that we want to model a recirculating flow happens at the downstream of a step as shown in the following sketch. (a) Specify the position of reattachment point and the appropriate distance of the outflow boundary layer, as a function of step height, h. (b) Determine all of the required boundary conditions for turbulent parameters (k and D) in each boundary. (c) Which turbulence model do you suggest to solve this problem? h ?arrow_forwardQuestion 9 Consider the flow of water over a flat plate. In a different experiment consider the flow of air over a flat plate. In both cases the flow is steady, the boundary layers that are formed are laminar and the gravitational acceleration can be neglected. In both cases the velocity far from the plates is the same (v.) and the temperature is also the same (80 °F). For the same distance x from the leading edge, in which boundary layer will the friction coefficient be higher? (a) The friction coefficient is the same for both cases. (b) In water. (c) In air. (d) It depends on the velocity profile that is assumed inside the boundary layer.arrow_forward
- Help me step by steparrow_forwardTwo large fixed parallel planes are 12 mm apart. The space between the surfaces Example is filled with oil of viscosity 0.972 N.s/m². A flat thin plate 0.25 m² area moves through the oil at a velocity of 0.3 m/s. Calculate the drag force: (1) When the plate is equidistant from both the planes, and (ii) When the thin plate is at a distance of 4 mm from one of the plane surfaces. Fixed parallel plane 6 mm Plate 0.3 m/s F 6 mm 12 mmarrow_forwardAir flows over a flat plate with a velocity u = 13 m/s and temperature T. = 25 °C. The plate surface area and temperature are A = 2 x 2 m and T, =125 °C, respectively. a- Determine the critical length X (length of the laminar region). b- Determine the rate of heat transfer in the laminar region. %3D C- Determine the total rate of heat transfer from the entire plate (mixed boundary layer). Use the following properties of air H = 2.08 x 10 N.s/m, p = 0.887 kg/m, k = 0.0325 W/m.K, Pr = 0.705 %3D rinar @111arrow_forward
- Problem 1. For uniform flow over a flat plate, a useful approximation for the x-component of velocity in an incompressible laminar boundary layer is a parabolic variation from the velocity at the surface, u (y = 0) = 0 due to no-slip condition, to the free-stream velocity at the edge of the boundary layer, u (y = 8) = U. The equation for the profile is given by u/U = 2 (y/d) – (y/8)², where d = cx 1/2 and c is a constant - (a) Show that the simplest expression for the y-component of velocity is (b) Plot u/U and v/U versus y/d at x = separate graphs. 2 *=4[4(9)²¯ +(9)*] = 0.50 m where = 5.0 mm. Use the x-axis for velocity and plot on (c) Find the maximum value for v/U at this location and discuss its magnitude compared to u/U. АУ u(x, y) Uarrow_forward2. Air at 40 °C moves over a long flat plate with a uniform free stream velocity of U = 900 m/s. Assume the boundary layer formed above the surface of the plate starts at the tip of the leading edge and the velocity profile inside the boundary layer has power-law form as Re, <107 8 10' < Re, <10* 7 - (). for u Sxarrow_forward6- A uniform free stream of air at 0.8 m/s flows over a flat plate (4 m long x 1 m wide). Assuming the boundary layer to be laminar on the plate and the velocity profile is: и Find the ratio of the drag force on the front half portion to the drag %3D U force on the rear half portion of the plate. (p = 1.2 kg/m ; v= 1.51×10* m³/s) [2.42]arrow_forwardarrow_back_iosSEE MORE QUESTIONSarrow_forward_ios
- Principles of Heat Transfer (Activate Learning wi...Mechanical EngineeringISBN:9781305387102Author:Kreith, Frank; Manglik, Raj M.Publisher:Cengage Learning