An experimental nuclear core simulation apparatus consists of a long thin-walled metallic tube of diameter D and length L , which is electrically heated to produce the sinusoidal heat flux distribution q s " ( x ) = q o " sin ( π x L ) where x is the distance measured from the tube inlet. Fluid at an inlet temperature T m , i flows through the tube at a rate of m ˙ . Assuming the flow is turbulent and fully developed over the entire length of the tube, develop expressions for: (a) the total rate of heat transfer, q , from the tube to the fluid; (b) the fluid outlet temperature, T m , o ; (e) the axial distribution of the wall temperature, T s ( x ) : and (d) the magnitude and position of the highest wall temperature. (e) Consider a 40-mm-diameter tube of 4-m length with a sinusoidal heat flux distribution for which q o " = 10 , 000 W / m 2 . Fluid passing through the tube has a flow rate of 0 .025 kg/s , a specific heat of 4180 J/kg ⋅ K , an entrance temperature of 25 ° C , and a convection coefficient of 1000 W/m 2 ⋅ K . Plot the mean fluid and surface temperatures as a function of distance along the tube. Identify important features of the distributions. Explore the effect of ± 25 % changes in the convection coefficient and the heat flux on the distributions.
An experimental nuclear core simulation apparatus consists of a long thin-walled metallic tube of diameter D and length L , which is electrically heated to produce the sinusoidal heat flux distribution q s " ( x ) = q o " sin ( π x L ) where x is the distance measured from the tube inlet. Fluid at an inlet temperature T m , i flows through the tube at a rate of m ˙ . Assuming the flow is turbulent and fully developed over the entire length of the tube, develop expressions for: (a) the total rate of heat transfer, q , from the tube to the fluid; (b) the fluid outlet temperature, T m , o ; (e) the axial distribution of the wall temperature, T s ( x ) : and (d) the magnitude and position of the highest wall temperature. (e) Consider a 40-mm-diameter tube of 4-m length with a sinusoidal heat flux distribution for which q o " = 10 , 000 W / m 2 . Fluid passing through the tube has a flow rate of 0 .025 kg/s , a specific heat of 4180 J/kg ⋅ K , an entrance temperature of 25 ° C , and a convection coefficient of 1000 W/m 2 ⋅ K . Plot the mean fluid and surface temperatures as a function of distance along the tube. Identify important features of the distributions. Explore the effect of ± 25 % changes in the convection coefficient and the heat flux on the distributions.
Solution Summary: The author explains the expression for total rate of heat transfer from tube to fluid.
An experimental nuclear core simulation apparatus consists of a long thin-walled metallic tube of diameter D and length L, which is electrically heated to produce the sinusoidal heat flux distribution
q
s
"
(
x
)
=
q
o
"
sin
(
π
x
L
)
where x is the distance measured from the tube inlet. Fluid at an inlet temperature
T
m
,
i
flows through the tube at a rate of
m
˙
. Assuming the flow is turbulent and fully developed over the entire length of the tube, develop expressions for: (a) the total rate of heat transfer, q, from the tube to the fluid; (b) the fluid outlet temperature,
T
m
,
o
; (e) the axial distribution of the wall temperature,
T
s
(
x
)
: and (d) the magnitude and position of the highest wall temperature. (e) Consider a 40-mm-diameter tube of 4-m length with a sinusoidal heat flux distribution for which
q
o
"
=
10
,
000
W
/
m
2
. Fluid passing through the tube has a flow rate of
0
.025 kg/s
, a specific heat of
4180 J/kg
⋅
K
, an entrance temperature of
25
°
C
, and a convection coefficient of
1000 W/m
2
⋅
K
. Plot the mean fluid and surface temperatures as a function of distance along the tube. Identify important features of the distributions. Explore the effect of
±
25
%
changes in the convection coefficient and the heat flux on the distributions.
Water flows at a rate of 0.1 kg/s in a tube with a diameter of 250 mm. The tube is heated uniformly at a rate of 135 kW/m2. Find the wall temperature at a location where Tsat = 180 C and x = 25%. [Ans.: Ts = 188 C]
1. Heated air at 1 atm and 35°C is to be transported in a 150-m-long circular plastic duct at a
rate of 0.35 m³/s (Fig. 1). If the head loss in the pipe is not to exceed 20 m, using the
Colebrook equation and consulting with the FE Reference Handbook and appropriate
table(s) for equations and properties. Write a Matlab code to determine the
i.
ii.
iii.
iv.
minimum diameter of the duct,
the friction factor,
average flow velocity and
Reynolds number of the flow
0.35 m³/s
air
D
-150 m
Fig 1
Water flows at a rate of 0.1 kg/s in a tube with a diameter of 250 mm. The tube is heated uniformly at a rate of 135 kW/m2. Find the wall temperature at a location where Tsat = 180 C and x = 25%. [Ans.: Ts = 188 C]
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