An opaque, diffuse, gray ( 200 mm× 200 mm ) plate with an emissivity of 0.8 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/m 2 ⋅ K and to large surroundings. The air and surroundings are each at 300 K. (a) Evaluate the net radiative heat transfer lo 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, d T p / d t ? Assume convection to the bottom surface of the plate to be negligible. (c) Extending the analysis of part (b), generate a plot of the change in temperature of the plate with time, d T p / d t , as a function of the plate temperature for 350 ≤ T p ≤ 900 K and all other conditions remaining the same. What is the steady-state temperature of the plate?
An opaque, diffuse, gray ( 200 mm× 200 mm ) plate with an emissivity of 0.8 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/m 2 ⋅ K and to large surroundings. The air and surroundings are each at 300 K. (a) Evaluate the net radiative heat transfer lo 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, d T p / d t ? Assume convection to the bottom surface of the plate to be negligible. (c) Extending the analysis of part (b), generate a plot of the change in temperature of the plate with time, d T p / d t , as a function of the plate temperature for 350 ≤ T p ≤ 900 K and all other conditions remaining the same. What is the steady-state temperature of the plate?
Solution Summary: The author explains the net radiative heat transfer to the bottom surface of the plate.
An opaque, diffuse, gray
(
200
mm×
200
mm
)
plate with an emissivity of 0.8 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/m
2
⋅
K
and to large surroundings. The air and surroundings are each at 300 K.
(a) Evaluate the net radiative heat transfer lo 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,
d
T
p
/
d
t
? Assume convection to the bottom surface of the plate to be negligible. (c) Extending the analysis of part (b), generate a plot of the change in temperature of the plate with time,
d
T
p
/
d
t
, as a function of the plate temperature for
350
≤
T
p
≤
900
K
and all other conditions remaining the same. What is the steady-state temperature of the plate?
Please Please use MATLAB with codes and graph. Recreate the following four Figures of the textbook using MATLAB and the appropriate parameters. Comment on your observations for each Figure. List all of the parameters that you have used. The figure is attached below.
Please only step 6 (last time I asked it was cut off at that point)
Please Please use a MATLAB with codes and grap. Recreate the following four Figures of the textbook using MATLAB and the appropriate parameters. Comment on your observations for each Figure. List all of the parameters that you have used. The figure attached below.
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