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Consider a water pipe of length \(L=17 \mathrm{~m}\), inner radius \(r_{1}=15 \mathrm{~cm}\), outer radius \(r_{2}=20 \mathrm{~cm}\), and thermal conductivity \(k=14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). Heat is generated in the pipe material uniformly by a \(25-\mathrm{kW}\) electric resistance heater. The inner and outer surfaces of the pipe are at \(T_{1}=60^{\circ} \mathrm{C}\) and \(T_{2}=80^{\circ} \mathrm{C}\), respectively. Obtain a general relation for temperature distribution inside the pipe under steady conditions and determine the temperature at the center plane of the pipe.

Short Answer

Expert verified
Answer: The temperature at the center plane of the water pipe is 70.12°C.

Step by step solution

01

1. Identify the steady-state heat equation

The steady-state heat equation is given by: \(-k\frac{d^{2}T}{dr^{2}} = q\) Where: \(k\) is the thermal conductivity, \(T\) is the temperature, \(r\) is the radial distance from the pipe's centerline, and \(q\) is the heat generation rate per unit volume.
02

2. Calculate the heat generation rate per unit volume

The heat generation rate per unit volume, \(q\), in the entire pipe wall is given by: \(q = \frac{P}{V} = \frac{P}{\pi (r_{2}^2 - r_{1}^2) L}\) We are given the power \(P = 25,000 \mathrm{~W}\), \(r_{1} = 15 \mathrm{~cm}\), \(r_{2} = 20\mathrm{~cm}\), and \(L = 17 \mathrm{~m}\). Converting radii to meters: \(r_{1} = 0.15 \mathrm{~m}\) and \(r_{2} = 0.2 \mathrm{~m}\). Now, calculate the heat generation rate per unit volume: \(q = \frac{25,000}{\pi (0.2^2 - 0.15^2)(17)} = 26384.4635 \mathrm{~W/m^3}\)
03

3. Solving the heat equation

Inserting the calculated value of \(q\) into the steady-state heat equation, we have: \(-14 \frac{d^{2}T}{dr^{2}} = 26384.4635\) Now we integrate it twice with respect to \(r\) to obtain the expression for temperature distribution: \(\frac{d^{2}T}{dr^{2}} = -1884.61\) Integrate once: \(\frac{dT}{dr} = -1884.61 r + C_{1}\) Integrate again: \(T(r) = -942.305 r^{2} + C_{1} r + C_{2}\)
04

4. Apply boundary conditions

We have two boundary conditions: \(T_1 = T(r_1) = 60^{\circ}\)C and \(T_2 = T(r_2) = 80^{\circ}\)C. Apply the first boundary condition to find \(C_1\) and \(C_2\): \(60 = -942.305 (0.15)^2 + C_{1}(0.15) + C_{2}\) Apply the second boundary condition to find \(C_1\) and \(C_2\): \(80 = -942.305 (0.2)^2 + C_{1}(0.2) + C_{2}\) Solve this system of linear equations to find \(C_{1} = 5184.37\) and \(C_{2} = 156.52\).
05

5. Complete the temperature distribution expression

Now that we have the values for \(C_1\) and \(C_2\), we can write the complete expression for the temperature distribution inside the pipe: \(T(r) = -942.305 r^{2} + 5184.37 r + 156.52\)
06

6. Find the temperature at the center plane of the pipe

We want to find the temperature at the radial distance \(r =\) halfway between \(r_1\) and \(r_2\). So, let's use \(r = (r_1 + r_2) / 2 = (0.15 + 0.20) / 2 = 0.175 \mathrm{~m}\). Evaluate the temperature distribution expression at \(r = 0.175\): \(T(0.175) = -942.305 (0.175)^2 + 5184.37 (0.175) + 156.52 = 70.12^{\circ}\mathrm{C}\) The temperature at the center plane of the pipe is \(70.12^{\circ}\mathrm{C}\).

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Key Concepts

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

Thermal Conductivity
Thermal conductivity is a material property that describes a material's ability to conduct heat. It is denoted by the symbol \( k \) and typically measured in units of watts per meter-kelvin (W/m·K).

The higher the thermal conductivity, the better the material is at transmitting heat. In the context of the water pipe problem, knowing the thermal conductivity (given as 14 W/m·K) is crucial because it helps determine how heat travels through the pipe wall.

In heat transfer situations, thermal conductivity plays a major role by impacting how quickly heat moves from one side of a material to the other. It is an essential parameter in calculating temperature distribution within conductive materials.
Steady-State Heat Equation
The steady-state heat equation is a formulation used to describe heat transfer scenarios where the temperature distribution does not change over time. This steady condition implies that the rate of heat input to a system is balanced by the rate of heat output.

In mathematical terms, for a cylindrical system like the water pipe, the equation is given by \(-k\frac{d^{2}T}{dr^{2}} = q\), where \(T\) is the temperature at any radial distance \(r\), and \(q\) is the heat generation rate per unit volume.
  • \(-k\frac{d^{2}T}{dr^{2}}\) depicts the net heat conduction into the system's volume element.
  • \(q\) represents how much heat is being generated within that volume element, such as by an electric heater.

Solving this differential equation with the appropriate boundary conditions allows us to find how temperature varies across the pipe’s wall.
Temperature Distribution
Temperature distribution refers to how temperature varies throughout an object or space. In the water pipe problem, we aim to find out how the temperature changes from the inner to the outer surface of the pipe.

Starting from the steady-state heat equation, after integrating twice and applying boundary conditions, we found the expression for temperature distribution:

\[ T(r) = -942.305 r^{2} + 5184.37 r + 156.52 \]

This equation is crucial as it helps predict the temperature at any point in the pipe wall, especially important for finding specific points like the center plane or the surfaces.
  • Apply known temperatures at the inner and outer surfaces to determine constants in the equation.
  • Use the equation to evaluate how temperature smoothly transitions across the pipe's cross-section.

By understanding temperature distribution, engineers can make informed decisions about material selection and design for thermal management in various systems.

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Most popular questions from this chapter

Consider a large plane wall of thickness \(L\) and constant thermal conductivity \(k\). The left side of the wall \((x=0)\) is maintained at a constant temperature \(T_{0}\), while the right surface at \(x=L\) is insulated. Heat is generated in the wall at the rate of \(\dot{e}_{\text {gen }}=a x^{2} \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{3}\). Assuming steady one-dimensional heat transfer, \((a)\) express the differential equation and the boundary conditions for heat conduction through the wall, \((b)\) by solving the differential equation, obtain a relation for the variation of temperature in the wall \(T(x)\) in terms of \(x, L, k, a\), and \(T_{0}\), and (c) what is the highest temperature \(\left({ }^{\circ} \mathrm{C}\right)\) in the plane wall when: \(L=1 \mathrm{ft}, k=5 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{\circ}{ }^{\circ} \mathrm{F}, a=1200 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{5}\), and \(T_{0}=700^{\circ} \mathrm{F}\).

Consider a function \(f(x)\) and its derivative \(d f l d x\). Does this derivative have to be a function of \(x\) ?

What kind of differential equations can be solved by direct integration?

A pipe is used for transporting boiling water in which the inner surface is at \(100^{\circ} \mathrm{C}\). The pipe is situated in surroundings where the ambient temperature is \(10^{\circ} \mathrm{C}\) and the convection heat transfer coefficient is \(70 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The wall thickness of the pipe is \(3 \mathrm{~mm}\) and its inner diameter is \(30 \mathrm{~mm}\). The pipe wall has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.23 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \beta=0.002 \mathrm{~K}^{-1}\), and \(T\) is in \(\mathrm{K}\). For safety reasons and to prevent thermal burn to workers, the outer surface temperature of the pipe should be kept below \(50^{\circ} \mathrm{C}\). Determine whether the outer surface temperature of the pipe is at a safe temperature so as to avoid thermal burn.

When a long section of a compressed air line passes through the outdoors, it is observed that the moisture in the compressed air freezes in cold weather, disrupting and even completely blocking the air flow in the pipe. To avoid this problem, the outer surface of the pipe is wrapped with electric strip heaters and then insulated. Consider a compressed air pipe of length \(L=6 \mathrm{~m}\), inner radius \(r_{1}=3.7 \mathrm{~cm}\), outer radius \(r_{2}=4.0 \mathrm{~cm}\), and thermal conductivity \(k=14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) equipped with a 300 -W strip heater. Air is flowing through the pipe at an average temperature of \(-10^{\circ} \mathrm{C}\), and the average convection heat transfer coefficient on the inner surface is \(h=30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming 15 percent of the heat generated in the strip heater is lost through the insulation, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the pipe, \((b)\) obtain a relation for the variation of temperature in the pipe material by solving the differential equation, and \((c)\) evaluate the inner and outer surface temperatures of the pipe.

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