Question

In: Physics

Air at 15°C flows at 9 m/s parallel to a thin flat plate measuring 260 mm...

Air at 15°C flows at 9 m/s parallel to a thin flat plate measuring 260 mm × 390 mm. The direction of flow is parallel to the 260-mm edges. The surface of the plate is at a uniform temperature of 85°C. The plate is in a large chamber with walls at a temperature of 22°C. The emissivity of the plate’s surfaces is 0·75. (a) Determine the rate of convective heat transfer from one side of the plate to air. [16] (b) Determine the rate of radiant heat transfer from one side of the plate the chamber walls. [4] (c) In the configuration described above, consider two values of freestream air speed: 9 m/s and 100 m/s. Sketch a graph showing the variation of local heat flux q'' (x) as a function of distance x along the plate from the leading edge for each value of speed, showing the two curves on a single set of axes. It is not necessary to calculate values for q'' (x) but you should determine the correct shape of each curve. Briefly explain the reasons for differences between the curves.

Solutions

Expert Solution


Related Solutions

A thin plate is suspended in air at 1 atm. with T_infinite= 15°C. Air flows on...
A thin plate is suspended in air at 1 atm. with T_infinite= 15°C. Air flows on both sides of the plate where the bottom side absorbs a uniform radiative heat flux of 1542 W/m2. The plate is oriented parallel to the flow and the length along the flow direction is 60 cm. Consider the plate is negligibly thin and the width of the plate (perpendicular to the flow) is large, so that the problem can be considered as a 2D...
Glycerin flows parallel to a flat plate measuring 2 ft by 2 ft with a velocity...
Glycerin flows parallel to a flat plate measuring 2 ft by 2 ft with a velocity of 10 fps. Determine values for the mean convective heat-transfer coefficient and the associated drag force imposed on the plate for glycerin temperatures of 30, 50, and 80F. What heat flux will result, in each case, if the plate temperature is 50F above that of the glycerin?
Air flows over a 4 meter long flat plate at a velocity of 8 m/s. Using...
Air flows over a 4 meter long flat plate at a velocity of 8 m/s. Using a spreadsheet, calculate the boundary layer thickness and wall shear stress at 0.1 meter intervals along the plate. Do not plot the wall shear stress at x=0. Use a transition Reynolds number of 5 x 10^5 . (You will need to calculate Rex at each location to determine if the laminar or turbulent correlations should be used.) Generate a spreadsheet table that includes columns...
A thin, flat plate that is 0.2 m × 0.2 m on a side is oriented...
A thin, flat plate that is 0.2 m × 0.2 m on a side is oriented parallel to an atmospheric airstream having a velocity of 40 m/s. The air is at a temperature of ∞T∞= 20ºC, while the plate is maintained at Ts= 120ºC. The air flows over the top and bottom surfaces of the plate, and measurement of the drag force reveals a value of 0.075 N. What is the rate of heat transfer from both sides of the...
A liquid flows tangentially past a flat plate of dimensions total length of 4 m (parallel...
A liquid flows tangentially past a flat plate of dimensions total length of 4 m (parallel to the flow direction) and width of 1.5 m. fluid velocity is 1 m/s (length wise). What is the skin friction drag (shear force) on both sides of the plate? liquid density = 1000 kg/m3, dynamic viscosity = 2 x 10-2 N*s/m2.
Air at 1 atm and 27 degree C flows across a flat plate at a velocity...
Air at 1 atm and 27 degree C flows across a flat plate at a velocity of 14 m/s. Find the distance from the leading edge where transition to turbulent flow begins and the local heat-transfer coefficient at this point if the temperature of the plate is 77 degree C.
Forced convection A thin plate is suspended in air at 1 atm. with T? = 15°C....
Forced convection A thin plate is suspended in air at 1 atm. with T? = 15°C. Air flows on both sides of the plate where the bottom side absorbs a uniform radiative heat flux of 1542 W/m2. The plate is oriented parallel to the flow and the length along the flow direction is 60 cm. Consider the plate is negligibly thin and the width of the plate (perpendicular to the flow) is large, so that the problem can be considered...
Consider a flat plate with parallel airflow (top and bottom) characterized by u∞ 5 m/s, T∞...
Consider a flat plate with parallel airflow (top and bottom) characterized by u∞ 5 m/s, T∞ 20°C. Determine the average convection heat transfer coefficient, convective heat transfer rate, and drag force associated with an 2.8-m-long, 2.8-m wide flat plate with a surface temperature of 50°C. Assume the critical Reynolds number is 5x105. Determine the average convection heat transfer coefficient, in W/m2·K. Determine the convective heat transfer rate, in W. Determine the drag force, in N.
Sketch a 5 kg thin flat uniform homogeneous square plate of side 600 mm, with a...
Sketch a 5 kg thin flat uniform homogeneous square plate of side 600 mm, with a circular opening of radius 100 mm. Determine the area and the mass moments of inertia about the center of mass.
Air at 10°C and I atm flows over a flat plate (30 cm x100 cm) at...
Air at 10°C and I atm flows over a flat plate (30 cm x100 cm) at 20 m/s. The plate is maintained at 70°C. (a) calculate the boundary layer thikness at distances of 30 cm and 100 cm, (b) calculate the heat transfer from first 30 cm and from whole the plate.
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT