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An experimental boiling water reactor is spherical in shape and operates with a water temperature of \(420 \mathrm{~K}\). The shell is made from nickel alloy steel \((k=21\) \(\mathrm{W} / \mathrm{m} \mathrm{K})\) and has an inside radius of \(0.7 \mathrm{~m}\) with a wall thickness of \(7 \mathrm{~cm}\). The reactor is surrounded by a layer of concrete \(20 \mathrm{~cm}\) thick. If the outside heat transfer coefficient is \(8 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\) and the ambient air is at \(300 \mathrm{~K}\), what are the temperatures of the internal and external surfaces of the concrete? Also, if the reactor operates at a power level of \(30 \mathrm{~kW}\), what fraction of the power generated is lost by heat transfer through the shell? The resistance to heat flow from the water to the shell can be taken to be negligible.

Short Answer

Expert verified
The temperatures of internal and external concrete surfaces depend on the calculations. The fraction of power lost is calculated by comparing heat loss through shell with reactor's total power output.

Step by step solution

01

Understand the Problem

We need to calculate the internal and external surface temperatures of the concrete. Additionally, determine the fraction of power lost through heat transfer. The given data includes: temperature of water inside the reactor core, the thermal conductivity of steel and concrete, shell and concrete thickness, outside heat transfer coefficient, and ambient temperature.
02

Identify Relevant Equations

Use the heat conduction equation for spherical shells \[ q = \frac{4 \pi k (T_{1} - T_{2})}{\frac{1}{r_{1}} - \frac{1}{r_{2}}} \]where \(q\) is the heat loss, \(k\) is conductivity, \(T_1\) and \(T_2\) are temperatures at inner and outer surfaces, and \(r_1\), \(r_2\) are inner and outer radii respectively. Use \[ q = UA(T_i - T_o) \]for the outer heat flux, where \(U\) is overall heat transfer coefficient, \(A\) is surface area.
03

Calculate Effective Conductivity for Concrete Layer

The conductivity for the concrete layer is typically around 1.4 W/mK. Given thickness is 20 cm, and the internal radius is 1.4 m. The effective thermal conductivity equation for a sphere helps determine how temperature changes across the layer.
04

Compute Heat Loss Through Nickel Alloy Steel Layer

With an inside radius of 0.7 m and thickness of 0.07 m, the outer radius becomes 0.77 m. Substitute these into the spherical shell conduction formula with values \(T_1 = 420\) K and find \(q\), the heat flow rate through the steel shell.
05

Calculate External Surface Temperature of Concrete

Now apply the heat conduction equation for the concrete layer using the external surface area and the ambient air temperature (300 K) as \(T_2\) with the heat flux calculated earlier. Solve for the internal surface temperature.
06

Determine Fraction of Power Lost

Compare calculated heat loss through the shell \(q\) with total reactor power output (30 kW). The fraction of power lost is \(\frac{q}{30000}\).

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Spherical Conduction
In the context of a boiling water reactor, spherical conduction plays a crucial role in understanding how heat is transferred through the reactor’s shell. When you have a spherical object, like this reactor, heat flows radially outward toward the environment. This is slightly different than conduction in flat surfaces. The mathematical equation for spherical conduction is given by:
\[q = \frac{4 \pi k (T_1 - T_2)}{\frac{1}{r_1} - \frac{1}{r_2}}\]
  • Here, \(q\) represents the rate of heat transfer.
  • \(k\) is the thermal conductivity of the material, which we'll discuss more shortly.
  • \(T_1\) and \(T_2\) are the temperatures at the inner and outer surfaces, respectively.
  • \(r_1\) and \(r_2\) refer to the inner and outer radii of the spherical shell.
This equation helps in calculating how efficiently heat transfers from the reactor core to the surrounding environment.
Thermal Conductivity
Thermal conductivity is a key property when discussing heat transfer. Thermal conductivity (\(k\)) indicates a material's ability to conduct heat. Higher values mean better heat conduction:
- Nickel alloy steel in the reactor shell has a thermal conductivity of about 21 W/mK. This implies it’s fairly good at conducting heat.- The concrete layer encasing the reactor, however, typically has a lower thermal conductivity, around 1.4 W/mK.The variation in conductivity affects how quickly heat is transferred from the reactor to its surroundings. The specific values for these materials are vital inputs in the equations used to calculate the temperatures at different points in the reactor's shell and concrete layer.
Boiling Water Reactor
A boiling water reactor (BWR) is a type of nuclear reactor where water surrounding the reactor core is not only used as a coolant but is also boiled to produce steam. This steam drives turbines to produce electricity. Key points about BWRs include:
  • In this type of reactor, the heat generated by nuclear fission in the core raises the temperature of the water up to boiling.
  • The hot water steam directly spins the turbine, a unique feature that distinguishes BWRs from other types like Pressurized Water Reactors (PWRs).
  • The internal temperature of the core, such as 420 K in the exercise, affects how heat conduction is managed through the various layers around it.
Understanding BWRs is essential to comprehend how energy is converted and transferred within the system, impacting structural components like the shell.
Heat Loss Calculation
Calculating heat loss is essential for assessing the efficiency of a reactor. Heat loss indicates how much of the generated power escapes from the system rather than being converted into usable energy.The exercise involves calculating:- **Internal and External Surface Temperatures**: Use the heat conduction and hyperbolic equations to find temperature distribution across shells.- **Heat Transfer Efficiency**: Determine how much of the 30 kW power output is lost through the shell.Finally, the fraction of power lost is calculated using:\[ \text{Fraction lost} = \frac{q}{30000} \]This fraction gives an idea of how much power is utilized versus wasted due to structural heat dissipation, helping to improve reactor efficiency through design adjustments.

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Most popular questions from this chapter

In a laboratory experiment, a long, \(2 \mathrm{~cm}\)-diameter, cylinder of fissionable material is encased in a \(1 \mathrm{~cm}\)-thick graphite shell. The unit is immersed in a coolant at 330 \(\mathrm{K}\), and the convective heat transfer coefficient on the graphite surface is estimated to be \(1000 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\). If heat is generated uniformly within the fissionable material at a rate of \(100 \mathrm{MW} / \mathrm{m}^{3}\), determine the temperature at the center-line of the cylinder. Allow for an interfacial conductance between the material and the graphite shell of \(3000 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\). and take the thermal conductivities of the material and graphite as \(4.1 \mathrm{~W} / \mathrm{m} \mathrm{K}\) and \(50 \mathrm{~W} / \mathrm{m} \mathrm{K}\), respectively.

Determine the allowable current in a 10 gage \((2.59 \mathrm{~mm}\) diameter) copper wire that is insulated with a \(1 \mathrm{~cm}-\mathrm{O} . \mathrm{D}\). layer of rubber. The outside heat transfer coefficient is \(20 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\), and the ambient air is at \(310 \mathrm{~K}\). The allowable maximum temperature of the rubber is \(380 \mathrm{~K}\). Take \(k=0.15 \mathrm{~W} / \mathrm{m} \mathrm{K}\) for the rubber and an electrical resistancethe rubber and an electrical resistance of \(0.00328 \Omega / \mathrm{m}\) for the copper wire.

An explosive is to be stored in large slabs of thickness \(2 L\) clad on both sides with a protective sheath. The rate at which heat is generated within the explosive is temperature-dependent and can be approximated by the linear relation \(\dot{Q}_{v}^{\prime \prime \prime}=a+b\left(T-T_{e}\right)\), where \(T_{e}\) is the prevailing ambient air temperature. If the overall heat transfer coefficient between the slab surface and the ambient air is \(U\), show that the condition for an explosion is \(L=(k / b)^{1 / 2} \tan ^{-1}\left[U /(k b)^{1 / 2}\right]\). Determine the slab thickness if \(k=0.9 \mathrm{~W} / \mathrm{m} \mathrm{K}, U=0.20 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}, a=60 \mathrm{~W} / \mathrm{m}^{3}\), \(b=6.0 \mathrm{~W} / \mathrm{m}^{3} \mathrm{~K}\).

In order to prevent fogging, the \(3 \mathrm{~mm}\)-thick rear window of an automobile has a transparent film electrical heater bonded to the inside of the glass. During a test, \(200 \mathrm{~W}\) are dissipated in a \(0.567 \mathrm{~m}^{2}\) area of window when the inside and outside air temperatures are \(22^{\circ} \mathrm{C}\) and \(1^{\circ} \mathrm{C}\), and the inside and outside heat transfer coefficients are \(9 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\) and \(22 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\), respectively. Determine the temperature of the inside surface of the window.

A test technique for measuring the thermal conductivity of copper-nickel alloys is based on the measurement of the tip temperature of pin fins made from the alloys. The standard fin dimensions are a diameter of \(5 \mathrm{~mm}\) and a length of \(20 \mathrm{~cm}\). The test fin and a reference brass fin \((k=111 \mathrm{~W} / \mathrm{m} \mathrm{K})\) are mounted on a copper base plate in a wind tunnel. The test data include \(T_{B}=100^{\circ} \mathrm{C}, T_{e}=20^{\circ} \mathrm{C}\), and tip temperatures of \(64.2^{\circ} \mathrm{C}\) and \(49.7^{\circ} \mathrm{C}\) for the brass and test alloy fins, respectively. (i) Determine the conductivity of the test alloy. (ii) If the conductivity should be known to \(\pm 1.0 \mathrm{~W} / \mathrm{m} \mathrm{K}\), how accurately should the tip temperatures be measured?

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