13.72 An opaque, diffuse, gray (200 mm × 200 mm) plate with an emissivity of o.8 is placed over the opening of a furnace and is known to be at 400 K at a certain instant. The bottom of the furnace, having the same dimensions as the plate, is black and operates at 1000 K. The sidewalls of the furnace are well insulated. The top of the plate is exposed to ambient air with a convection coefficient of 25 W/m² . K and to large surroundings. The air and surroundings are each at 300 K.

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
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Chapter11: Heat Transfer By Radiation
Section: Chapter Questions
Problem 11.65P
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13.72 An opaque, diffuse, gray (200 mm x 200 mm) plate with an emissivity of o.8 is placed over the opening of a furnace
and is known to be at 400 K at a certain instant. The bottom of the furnace, having the same dimensions as the plate, is
black and operates at 1000 K. The sidewalls of the furnace are well insulated. The top of the plate is exposed to ambient air
with a convection coefficient of 25 W/m² . K and to large surroundings. The air and surroundings are each at 300 K.
Ty = 300 K
- T = 300 K
h = 25 W/m2 .K
sur
Air
Plate, 400 K, ɛ = 0.8
-Insulated sidewalls
200 mm
Furnace bottom,
1000 K
(a) Evaluate the net rate of radiative heat transfer to the bottom surface of the plate.
(b) If the plate has mass and specific heat of 2 kg and 900 J/kg · K, respectively, what will be the change in temperature of
the plate with time, dT „/ dt? Assume convection to the bottom surface of the plate to be negligible.
Transcribed Image Text:13.72 An opaque, diffuse, gray (200 mm x 200 mm) plate with an emissivity of o.8 is placed over the opening of a furnace and is known to be at 400 K at a certain instant. The bottom of the furnace, having the same dimensions as the plate, is black and operates at 1000 K. The sidewalls of the furnace are well insulated. The top of the plate is exposed to ambient air with a convection coefficient of 25 W/m² . K and to large surroundings. The air and surroundings are each at 300 K. Ty = 300 K - T = 300 K h = 25 W/m2 .K sur Air Plate, 400 K, ɛ = 0.8 -Insulated sidewalls 200 mm Furnace bottom, 1000 K (a) Evaluate the net rate of radiative heat transfer to the bottom surface of the plate. (b) If the plate has mass and specific heat of 2 kg and 900 J/kg · K, respectively, what will be the change in temperature of the plate with time, dT „/ dt? Assume convection to the bottom surface of the plate to be negligible.
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