The 50-mm peephole of a large furnace operating at 450 ∘ C is covered with a material having τ = 0.8 and ρ = 0 for irradiation originating from the furnace. The material has an emissivity of 0.8 and is opaque to irradiation from a source at room temperature. The outer surface of the cover is exposed to surroundings and ambient air at 27 ∘ C with a convection heat transfer coefficient of 50 W / m 2 ⋅ k . Assuming that convection effects on the inner surface of the cover are negligible, calculate the heat loss by the furnace and the temperature of the cover
The 50-mm peephole of a large furnace operating at 450 ∘ C is covered with a material having τ = 0.8 and ρ = 0 for irradiation originating from the furnace. The material has an emissivity of 0.8 and is opaque to irradiation from a source at room temperature. The outer surface of the cover is exposed to surroundings and ambient air at 27 ∘ C with a convection heat transfer coefficient of 50 W / m 2 ⋅ k . Assuming that convection effects on the inner surface of the cover are negligible, calculate the heat loss by the furnace and the temperature of the cover
Solution Summary: The author explains the heat loss by the furnace, the temperature of the cover, and the convection heat transfer coefficient.
The 50-mm peephole of a large furnace operating at
450
∘
C
is covered with a material having
τ
=
0.8
and
ρ
=
0
for irradiation originating from the furnace. The material has an emissivity of 0.8 and is opaque to irradiation from a source at room temperature. The outer surface of the cover is exposed to surroundings and ambient air at
27
∘
C
with a convection heat transfer coefficient of
50
W
/
m
2
⋅
k
. Assuming that convection effects on the inner surface of the cover are negligible, calculate the heat loss by the furnace and the temperature of the cover
A horizontal plate is experiencing uniform irradiation on the both upper and lower surfaces. The ambient air temperature surrounding the plate is 290 K with a convection heat transfer coefficient of 30 W/m2·K. Both upper and lower surfaces of the plate have a radiosity of 4000 W/m2, and the plate temperature is maintained uniformly at 390 K. If the plate is not opaque and has an absorptivity of 0.527, determine the irradiation and emissivity of the plate.
A furnace has the shape of a cylinder and has R = H = 2m as its dimensions. The temperatures on the base, top, and side surfaces of the furnace are kept constant at 500, 700, and 1200 K accordingly. All three surfaces are black. Determine the net rate of radiation heat transfer from or to the top surface when the system is operating at a steady state.
You can neglect radiation at the bottom of the plate; the bottom side of the plate has water flowing underneath it. Often, when dealing with liquids (rather than gases), one can neglect radiation because heat transfer due to convection is so much larger (liquids tend to have higher convection coefficient values than gases).
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