Water at 20°C and a flow rate of 0 .1 kg/s enters a heated, thin-walled tube with a diameter of 15 mm and length of 2 m. The wall heat flux provided by the heating elements depends on the wall temperature according to the relation q s " ( x ) = q s , o " [ 1 + α ( T s − T ref ) ] where q s " = 10 4 W / m 2 , α = 0.2 K − 1 , T r e f = 20 ° C , and T s , is the wall temperature in °C. Assume fully developed flow and thermal conditions with a convection coefficient of 3000 W / m 2 ⋅ K . (a) Beginning with a properly defined differential control volume in the tube, derive expressions for the variation of the water, T m ( x ) , and the wall, T s ( x ) ,temperatures as a function of distance from the tube inlet. (b) Using a numerical integration scheme, calculate and plot the temperature distributions, T m ( x ) and T s ( x ) on the same graph. Identify and comment on the main features of the distributions. Hint: The IHT integral function D E R ( T m , x ) can be used to perform the integration along the length of the tube. (c) Calculate the total rate of heat transfer to the water.
Water at 20°C and a flow rate of 0 .1 kg/s enters a heated, thin-walled tube with a diameter of 15 mm and length of 2 m. The wall heat flux provided by the heating elements depends on the wall temperature according to the relation q s " ( x ) = q s , o " [ 1 + α ( T s − T ref ) ] where q s " = 10 4 W / m 2 , α = 0.2 K − 1 , T r e f = 20 ° C , and T s , is the wall temperature in °C. Assume fully developed flow and thermal conditions with a convection coefficient of 3000 W / m 2 ⋅ K . (a) Beginning with a properly defined differential control volume in the tube, derive expressions for the variation of the water, T m ( x ) , and the wall, T s ( x ) ,temperatures as a function of distance from the tube inlet. (b) Using a numerical integration scheme, calculate and plot the temperature distributions, T m ( x ) and T s ( x ) on the same graph. Identify and comment on the main features of the distributions. Hint: The IHT integral function D E R ( T m , x ) can be used to perform the integration along the length of the tube. (c) Calculate the total rate of heat transfer to the water.
Solution Summary: The author explains the expressions for the variations of the water and the wall, as a function of distance from the tube inlet.
Water at 20°C and a flow rate of
0
.1 kg/s
enters a heated, thin-walled tube with a diameter of 15 mm and length of 2 m. The wall heat flux provided by the heating elements depends on the wall temperature according to the relation
q
s
"
(
x
)
=
q
s
,
o
"
[
1
+
α
(
T
s
−
T
ref
)
]
where
q
s
"
=
10
4
W
/
m
2
,
α
=
0.2
K
−
1
,
T
r
e
f
=
20
°
C
, and
T
s
, is the wall temperature in °C. Assume fully developed flow and thermal conditions with a convection coefficient of
3000
W
/
m
2
⋅
K
.
(a) Beginning with a properly defined differential control volume in the tube, derive expressions for the variation of the water,
T
m
(
x
)
, and the wall,
T
s
(
x
)
,temperatures as a function of distance from the tube inlet. (b) Using a numerical integration scheme, calculate and plot the temperature distributions,
T
m
(
x
)
and
T
s
(
x
)
on the same graph. Identify and comment on the main features of the distributions. Hint: The IHT integral function
D
E
R
(
T
m
,
x
)
can be used to perform the integration along the length of the tube. (c) Calculate the total rate of heat transfer to the water.
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The tension in the belt is 46 lb. Determine the moment of the force F1 about the pin at A. Determine the moment of the force F2 about the pin at A.
1. Describe each of the tolerances in the following drawing:
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