Consider a cylindrical nuclear fuel rod of length L and diameter D that is encased in a concentric tube. Pressurized water flows through the annular region between the rod and the tube at a rate m ˙ , and the outer surface of the tube is well insulated. Heat generation occurs within the fuel rod, and the volumetric generation rate is known to vary sinusoidally with distance along the rod. That is, q ˙ ( x ) = q ˙ o sin ( π x / L ) , where q ˙ o ( W / m 3 ) is a constant. A uniform convection coefficient h may be assumed to exist between the surface of the rod and the water. (a) Obtain expressions for the local heat flux q ' ' ( x ) and the total heat transfer q from the fuel rod to the water. (b) Obtain an expression for the variation of the mean temperature T m ( x ) of the water with distance xalong the tube. (c) Obtain an expression for the variation of the rod surface temperature T s ( x ) with distance x along the tube. Develop an expression for the x -location at which this temperature is maximized.
Consider a cylindrical nuclear fuel rod of length L and diameter D that is encased in a concentric tube. Pressurized water flows through the annular region between the rod and the tube at a rate m ˙ , and the outer surface of the tube is well insulated. Heat generation occurs within the fuel rod, and the volumetric generation rate is known to vary sinusoidally with distance along the rod. That is, q ˙ ( x ) = q ˙ o sin ( π x / L ) , where q ˙ o ( W / m 3 ) is a constant. A uniform convection coefficient h may be assumed to exist between the surface of the rod and the water. (a) Obtain expressions for the local heat flux q ' ' ( x ) and the total heat transfer q from the fuel rod to the water. (b) Obtain an expression for the variation of the mean temperature T m ( x ) of the water with distance xalong the tube. (c) Obtain an expression for the variation of the rod surface temperature T s ( x ) with distance x along the tube. Develop an expression for the x -location at which this temperature is maximized.
Consider a cylindrical nuclear fuel rod of length L and diameter D that is encased in a concentric tube. Pressurized water flows through the annular region between the rod and the tube at a rate
m
˙
, and the outer surface of the tube is well insulated. Heat generation occurs within the fuel rod, and the volumetric generation rate is known to vary sinusoidally with distance along the rod. That is,
q
˙
(
x
)
=
q
˙
o
sin
(
π
x
/
L
)
,
where
q
˙
o
(
W
/
m
3
)
is a constant. A uniform convection coefficient h may be assumed to exist between the surface of the rod and the water.
(a) Obtain expressions for the local heat flux
q
'
'
(
x
)
and the total heat transfer q from the fuel rod to the water. (b) Obtain an expression for the variation of the mean temperature
T
m
(
x
)
of the water with distance xalong the tube. (c) Obtain an expression for the variation of the rod surface temperature
T
s
(
x
)
with distance x along the tube. Develop an expression for the x-location at which this temperature is maximized.
A liquid metal flows at a mass rate of 3 kg/s through a constant heat flux 5-cm-i.d tube in a nuclear reactor. The fluid at 473 K is to be heated with the tube wall 30 K above the fluid temperature. Determine the length of the tube required for a 1-K rise in bulk fluid temperature, using the following properties: p = 7.7 x 10^3 kg/m^3v = 8.0 x 10^-8 m^2/sCp = 130 J/(kg K)k = 12 W/mKPr = 0.011
Kaufman's correlation: Nu = 0,625.(Re.Pr)0,4
1. Water flows at the rate of 0.5 kg/s in a 2.5-cm-diameter tube having a length of 3 m. A constant heat flux is imposed at the tube wall so that the tube wall temperature is 40◦C higher than the water temperature. Calculate the heat transfer and estimate the temperature rise in the water. The water is pressurized so that boiling cannot occur.
You, a process design engineer, are tasked to build a powerplant that utilizes 1.5 metric tons of municipal
solid wastes (MSW) per hour. In an industrial boiler, MSW is burned to heat and pressurize 1 kg/s of
preheated water to high-pressure steam (44 atm, 450 °C).
The high-pressure steam, moving at a linear velocity of 70 m/s, is then used to drive a high-pressure
turbine. In a heat exchanger, the used steam from the outlet of high-P turbine at an intermediate pressure
(10 atm, 250 °C) is used to preheat the water that will be fed to the boiler. This water is pumped from an
underground reservoir at a low velocity (1 atm, 25 °C).
After preheating the water, the intermediate-pressure steam leaving the heat exchanger is then used to
drive a low-pressure turbine. Lastly, the steam from outlet of the low-P turbine leaves at a velocity of 10
m/s (at 1 atm and 100 °C) via an exhaust 10 m above the pump inlet.
The industrial boiler is insulated, but due to the high temperatures and the nature…
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