A copper sheet of thickness 2 L = 2 mm has an initial temperature of T i = 118 ° C . It is suddenly quenched in liquid water, resulting in boiling at its two surfaces. For boiling, Newton's law of cooling is expressed as q n = h ( T s − T sat ) , where T s is the solid surface temperature and T sat is the saturation temperature of the fluid (in this case T sat = 100 ° C) . The convection heat transfer coefficient may be expressed as h = 1010 W/m 2 ⋅ K 3 ( T − T sat ) 2 . Determine the time needed for the sheet to reach a temperature of T = 102 ° C . Plot the copper temperature versus time for 0 ≤ t ≤ 0.5 s . On the same graph, plot the copper temperature history assuming the heat transfer coefficient is constant. evaluated at the average copper temperature T ¯ = 100 ° C . Assume lumped capacitance behavior.
A copper sheet of thickness 2 L = 2 mm has an initial temperature of T i = 118 ° C . It is suddenly quenched in liquid water, resulting in boiling at its two surfaces. For boiling, Newton's law of cooling is expressed as q n = h ( T s − T sat ) , where T s is the solid surface temperature and T sat is the saturation temperature of the fluid (in this case T sat = 100 ° C) . The convection heat transfer coefficient may be expressed as h = 1010 W/m 2 ⋅ K 3 ( T − T sat ) 2 . Determine the time needed for the sheet to reach a temperature of T = 102 ° C . Plot the copper temperature versus time for 0 ≤ t ≤ 0.5 s . On the same graph, plot the copper temperature history assuming the heat transfer coefficient is constant. evaluated at the average copper temperature T ¯ = 100 ° C . Assume lumped capacitance behavior.
Solution Summary: The author calculates the time required for the sheet to require at temperature 102°C.
A copper sheet of thickness
2
L
=
2
mm
has an initial temperature of
T
i
=
118
°
C
.
It is suddenly quenched in liquid water, resulting in boiling at its two surfaces. For boiling, Newton's law of cooling is expressed as
q
n
=
h
(
T
s
−
T
sat
)
,
where
T
s
is the solid surface temperature and
T
sat
is the saturation temperature of the fluid (in this case
T
sat
=
100
°
C)
.
The convection heat transfer coefficient may be expressed as
h
=
1010
W/m
2
⋅
K
3
(
T
−
T
sat
)
2
.
Determine the time needed for the sheet to reach a temperature of
T
=
102
°
C
.
Plot the copper temperature versus time for
0
≤
t
≤
0.5
s
.
On the same graph, plot the copper temperature history assuming the heat transfer coefficient is constant. evaluated at the average copper temperature
T
¯
=
100
°
C
.
Assume lumped capacitance behavior.
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