In a nuclear reactor, heat is generated uniformly in the 5 -cm-diameter cylindrical uranium rods at a rate of \(2 \times 10^{8} \mathrm{~W} / \mathrm{m}^{3}\). If the length of the rods is \(1 \mathrm{~m}\), determine the rate of heat generation in each rod. Answer: \(393 \mathrm{~kW}\)

Short Answer

Expert verified
Answer: The rate of heat generation in each uranium rod is 393 kW.

Step by step solution

01

Calculate the volume of each rod

To find the rate of heat generation in each rod, we first need to calculate the volume of each rod. The rods have a cylindrical shape and we are given the diameter and the length. The formula for the volume of a cylinder is: \[V = \pi r^2 h\] where 'V' is the volume, 'r' is the radius, and 'h' is the height (length) of the cylinder. Since we have the diameter (5 cm) and length (1 m), we can find the radius by dividing the diameter by 2: \[r = \frac{d}{2} = \frac{5\mathrm{~cm}}{2} = 2.5\mathrm{~cm}\] Now, convert the radius and length to meters: \[r = 2.5\mathrm{~cm} \times \frac{1\mathrm{~m}}{100\mathrm{~cm}} = 0.025\mathrm{~m}\] \[h = 1\mathrm{~m}\] Now plug in the values for radius and height into the volume formula: \[V = \pi (0.025\mathrm{~m})^2 (1\mathrm{~m})\]
02

Calculate the volume

Now we have to calculate the actual volume of each cylindrical rod. Using the formula and the values we just found, we can find the volume: \[V = \pi (0.025\mathrm{~m})^2 (1\mathrm{~m}) = 0.001963\mathrm{~m}^3\]
03

Calculate the rate of heat generation

We are given the heat generation rate per cubic meter, which is \(2 \times 10^{8} \mathrm{~W} / \mathrm{m}^{3}\). To find the rate of heat generation in each rod, we just need to multiply the rate in \(\mathrm{W} / \mathrm{m}^{3}\) by the volume of the rod: \[\textit{Rate of heat generation} = 2 \times 10^{8} \mathrm{~W} / \mathrm{m}^{3} \times 0.001963\mathrm{~m}^3 = 393000\mathrm{~W}\]
04

Express the answer in kilowatts

Lastly, we need to express our answer in kilowatts. To do this, divide the watts by 1000: \[\textit{Rate of heat generation} = \frac{393000\mathrm{~W}}{1000} = 393\mathrm{~kW}\] Hence, the rate of heat generation in each uranium rod is 393 kW.

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Most popular questions from this chapter

Consider a large plane wall of thickness \(L=0.4 \mathrm{~m}\), thermal conductivity \(k=1.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=\) \(30 \mathrm{~m}^{2}\). The left side of the wall is maintained at a constant temperature of \(T_{1}=90^{\circ} \mathrm{C}\) while the right side loses heat by convection to the surrounding air at \(T_{\infty}=25^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=24 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming constant thermal conductivity and no heat generation in the wall, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the wall, \((b)\) obtain a relation for the variation of temperature in the wall by solving the differential equation, and \((c)\) evaluate the rate of heat transfer through the wall. Answer: (c) \(7389 \mathrm{~W}\)

A plane wall of thickness \(L\) is subjected to convection at both surfaces with ambient temperature \(T_{\infty 1}\) and heat transfer coefficient \(h_{1}\) at inner surface, and corresponding \(T_{\infty 2}\) and \(h_{2}\) values at the outer surface. Taking the positive direction of \(x\) to be from the inner surface to the outer surface, the correct expression for the convection boundary condition is (a) \(\left.k \frac{d T(0)}{d x}=h_{1}\left[T(0)-T_{\mathrm{o} 1}\right)\right]\) (b) \(\left.k \frac{d T(L)}{d x}=h_{2}\left[T(L)-T_{\infty 2}\right)\right]\) (c) \(\left.-k \frac{d T(0)}{d x}=h_{1}\left[T_{\infty 1}-T_{\infty 2}\right)\right]\) (d) \(\left.-k \frac{d T(L)}{d x}=h_{2}\left[T_{\infty 1}-T_{\infty 22}\right)\right]\) (e) None of them

Consider a small hot metal object of mass \(m\) and specific heat \(c\) that is initially at a temperature of \(T_{i}\). Now the object is allowed to cool in an environment at \(T_{\infty}\) by convection with a heat transfer coefficient of \(h\). The temperature of the metal object is observed to vary uniformly with time during cooling. Writing an energy balance on the entire metal object, derive the differential equation that describes the variation of temperature of the ball with time, \(T(t)\). Assume constant thermal conductivity and no heat generation in the object. Do not solve.

A spherical container, with an inner radius \(r_{1}=1 \mathrm{~m}\) and an outer radius \(r_{2}=1.05 \mathrm{~m}\), has its inner surface subjected to a uniform heat flux of \(\dot{q}_{1}=7 \mathrm{~kW} / \mathrm{m}^{2}\). The outer surface of the container has a temperature \(T_{2}=25^{\circ} \mathrm{C}\), and the container wall thermal conductivity is \(k=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). Show that the variation of temperature in the container wall can be expressed as \(T(r)=\left(\dot{q}_{1} r_{1}^{2} / k\right)\left(1 / r-1 / r_{2}\right)+T_{2}\) and determine the temperature of the inner surface of the container at \(r=r_{1}\).

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