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.
Water enters a tube at 29°C with a flow rate of 460 kg/h. The rate of heat transfer from the tube wall to the fluid is given as qs′(W/m)=ax, where the coefficient a is 25 W/m2 and x(m) is the axial distance from the tube entrance.
(a) Beginning with a properly defined differential control volume in the tube, derive an expression for the temperature distribution Tm(x) of the water.
(b) What is the outlet temperature of the water for a heated section 31 m long?
(c) Sketch the mean fluid temperature, Tm(x), and the tube wall temperature, Ts(x), as a function of distance along the tube for fully developed and developing flow conditions.
(d) What value of a uniform wall heat flux, qs″ (instead of qs′=ax), would provide the same fluid outlet temperature as that determined in part 8.13b? For this type of heating, sketch the temperature distributions requested in part 8.13c.
2. Consider water is to be heated in a tube equipped with electric resistance heater on its surface.
The power rating of the heater and inner surface temperature are to be determined? Properties
of tube and water are given below;
Tube length L= 7 m, Tube Diameter of Tube D= 2cm, Surface heat flux is constant,
water inlet/outlet Temp. Tinlet= 12 °C, Toutlet= 70°C
For water q= 992.1 kg/m³ , V=0.008 m³/min, k=0.631 W/m°C, y= 0.658 10- m²/s,
4179 j/kg °C, Pr= 4.32
Cp=
steam exits the turbine of a steam power plant at 105 F and is to be condensed in a large condenser by cooling water flowing through copper pipes (k = 223 Btu/h-ft-F) of inner diameter 0.5 in. and outer diameter 0.7 in. at an average temperature of 70 F. The heat transfer of vaporization of water at 100F is 1037 Btu/lbm. The heat transfer coefficient are 1500 Btu/h-ft-F on the steam side and 35 Btu/h-ft-F on the water side. Determine the length of the tube required to condense steam at arate of 130 lbm/h.
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