Consider the composite wall of Problem 3.13 under conditions for which the inside air is still characterized by T ∞ , i = 20 ° C and h i = 30 W/m 2 ⋅ K . However, use the more realistic conditions for which the outside air is characterized by a diurnal (time) varying temperature of the form T ∞ , 0 ( K ) = 273 + 5 sin ( 2 π 24 t ) 0 ≤ t ≤ 12 h T ∞ , o ( K ) = 273 + 11 sin ( 2 π 24 t ) 12 ≤ t ≤ 24 h with h o = 60 W/m 2 ⋅ K . Assuming quasi-steady conditions for which changes in energy storage within the wall may be neglected, estimate the daily heat loss through the wall if its total surface area is 200 m 2 .
Consider the composite wall of Problem 3.13 under conditions for which the inside air is still characterized by T ∞ , i = 20 ° C and h i = 30 W/m 2 ⋅ K . However, use the more realistic conditions for which the outside air is characterized by a diurnal (time) varying temperature of the form T ∞ , 0 ( K ) = 273 + 5 sin ( 2 π 24 t ) 0 ≤ t ≤ 12 h T ∞ , o ( K ) = 273 + 11 sin ( 2 π 24 t ) 12 ≤ t ≤ 24 h with h o = 60 W/m 2 ⋅ K . Assuming quasi-steady conditions for which changes in energy storage within the wall may be neglected, estimate the daily heat loss through the wall if its total surface area is 200 m 2 .
Solution Summary: The author calculates the daily heat loss through the wall. The temperature of inside air is T_infty,i=20°C, the heat transfer coefficient inside room is
Consider the composite wall of Problem 3.13 under conditions for which the inside air is still characterized by
T
∞
,
i
=
20
°
C
and
h
i
=
30
W/m
2
⋅
K
.
However, use the more realistic conditions for which the outside air is characterized by a diurnal (time) varying temperature of the form
T
∞
,
0
(
K
)
=
273
+
5
sin
(
2
π
24
t
)
0
≤
t
≤
12
h
T
∞
,
o
(
K
)
=
273
+
11
sin
(
2
π
24
t
)
12
≤
t
≤
24
h
with
h
o
=
60
W/m
2
⋅
K
.
Assuming quasi-steady conditions for which changes in energy storage within the wall may be neglected, estimate the daily heat loss through the wall if its total surface area is
200
m
2
.
=
Consider a large plane wall of thickness L=0.3 m, thermal conductivity k = 2.5 W/m.K,
and surface area A = 12 m². The left side of the wall at x=0 is subjected to a net heat
flux of ɖo = 700 W/m² while the temperature at that surface is measured to be T₁ =
80°C. Assuming constant thermal conductivity and no heat generation in the wall, (a)
express the differential equation and the boundary equations for steady one-
dimensional heat conduction through the wall, (b) obtain a relation for the variation of
the temperature in the wall by solving the differential equation, and (c) evaluate the
temperature of the right surface of the wall at x=L.
Ti
до
L
X
How long should it take to boil an egg? Model the egg as a sphere with radius of 2.3 cm that has properties similar to water with a density of = 1000 kg/m3 and thermal conductivity of k = 0.606 Watts/(mC) and specific heat of c = 4182 J/(kg C). Suppose that an egg is fully cooked when the temperature at the center reaches 70 C. Initially the egg is taken out of the fridge at 4 C and placed in the boiling water at 100 C. Since the egg shell is very thin assume that it quickly reaches a temperature of 100 C. The protein in the egg effectively immobilizes the water so the heat conduction is purely conduction (no convection). Plot the temperature of the egg over time and use the data tooltip in MATLAB to make your conclusion on the time it takes to cook the egg in minutes.
4x
F2
# 3
E
4,
F3
54
$
R
F4
Ac = 1m²
▬
H
DII
x= 1 m
(4) Consider a wall (as shown above) of thickness L-1 m and thermal conductivity k-1 W/m-K. The left
(x=0) and the right (x=1 m) surfaces of the wall are subject to convection with a convectional heat
transfer coefficient h= 1 W/m²K and an ambient temperature T. 1 K. There is no heat generation inside
the wall. You may assume 1-D heat transfer, steady state condition, and neglect any thermal contact
resistance. Find T(x).
%
To,1 = 1 K
h₁ = 1 W/m²K
5
Q Search
F5
T
T₁
A
6
x=0
F6
à = 0 W/m³
k= 1W/mK
L=1m
Y
994
F7
&
7
T₂
U
Ton2 = 1 K
h₂ = 1 W/m²K1
PrtScn
F8
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0
PgUp
F11
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