During radiant heat treatment of a thin-film material, its shape, which may be hemispherical (a) or spherical (b), is maintained by a relatively low air pressure (as in the case of a rubber balloon). Irradiation on the film is due to emission from a radiant heater of area A h = 0.0052 m 2 , which emits diffusely with an intensity of I e , h = 169 , 000 W / m 2 · s r . (a) Obtain an expression for the irradiation on the film as a function of the zenith angle θ . (b) Based on the expressions derived in part (a), which shape provides the more uniform irradiation G and hence provides better quality control for the treatment process?
During radiant heat treatment of a thin-film material, its shape, which may be hemispherical (a) or spherical (b), is maintained by a relatively low air pressure (as in the case of a rubber balloon). Irradiation on the film is due to emission from a radiant heater of area A h = 0.0052 m 2 , which emits diffusely with an intensity of I e , h = 169 , 000 W / m 2 · s r . (a) Obtain an expression for the irradiation on the film as a function of the zenith angle θ . (b) Based on the expressions derived in part (a), which shape provides the more uniform irradiation G and hence provides better quality control for the treatment process?
Solution Summary: The author explains the expression for the irradiation on the film as a function of zenith angle theta and the equation for radiant heat leaving the surface.
During radiant heat treatment of a thin-film material, its shape, which may be hemispherical (a) or spherical (b), is maintained by a relatively low air pressure (as in the case of a rubber balloon). Irradiation on the film is due to emission from a radiant heater of area
A
h
=
0.0052
m
2
, which emits diffusely with an intensity of
I
e
,
h
=
169
,
000
W
/
m
2
·
s
r
.
(a) Obtain an expression for the irradiation on the film as a function of the zenith angle
θ
. (b) Based on the expressions derived in part (a), which shape provides the more uniform irradiation G and hence provides better quality control for the treatment process?
Two concentric spheres of diameter D1= 0.9 m and D2= 1.2 m are separated by an air space and have surface temperatures of T1= 400 K and T2= 300 K. (a) If the surfaces are black, what is the net rate of radiation exchange between the spheres, in W? q12= Enter your answer for part (a) in accordance to the question statement W (b) What is the net rate of radiation exchange between the surfaces if they are diffuse and gray with ε1= 0.5 and ε2= 0.05, in W? q12= Enter your answer for part (b) in accordance to the question statement W (c) What is the net rate of radiation exchange if D2 is increased to 20 m, with ε2= 0.05, ε1= 0.5, and D1= 0.9 m, in W? q12= Enter your answer for part (c) in accordance to the question statement W (d) What is the net rate of radiation exchange if the larger sphere behaves as a black body (ε2= 1.0) and with ε1= 0.5, D2= 20 m, and D1= 0.9 m, in W? q12= Enter your answer for part(d) in accordance to the question statement W
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Irradiation on a semi-transparent medium is at a
rate of 610 W/m2. If 160 W/m2 of the irradiation is
reflected from the medium and 130 W/m2 is
transmitted through the medium,
Determine the absorptivity of the medium.
The absorptivity of the medium is.
An uninsulated steam pipe passes through a room in which the air and walls are at 25°C. The tube's outer diameter is 70 mm and its surface temperature and emissivity are 200°C and 0.8, respectively. Determine the surface emissive power and the irradiation. If the coefficient associated with the natural convection of surface heat transfer to air is 15 W/m².K, what will be the heat transfer rate per unit length of pipe?
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