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A pipe is used for transporting boiling water in which the inner surface is at \(100^{\circ} \mathrm{C}\). The pipe is situated in a surrounding where the ambient temperature is \(20^{\circ} \mathrm{C}\) and the convection heat transfer coefficient is \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The pipe has a wall thickness of \(3 \mathrm{~mm}\) and an inner diameter of \(25 \mathrm{~mm}\), and it has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \beta=0.003 \mathrm{~K}^{-1}\) and \(T\) is in \(\mathrm{K}\). Determine the outer surface temperature of the pipe.

Short Answer

Expert verified
Answer: The outer surface temperature of the pipe is approximately \(66.23 ^{\circ} \mathrm{C}\).

Step by step solution

01

Convert temperatures to Kelvin

First, we must convert the inner surface and ambient temperatures to Kelvin. \(T_{i} = 100^{\circ} \mathrm{C} + 273.15 = 373.15 \mathrm{K}\) \(T_{\infty} = 20^{\circ} \mathrm{C} + 273.15 = 293.15 \mathrm{K}\)
02

Calculate the heat transfer through the pipe using convection

Using the convection heat transfer formula, we can find the heat transfer, \(q\): \(q = hA(T_{i} - T_{\infty})\) Here, \(A = \pi dL\), where \(d = 25 \times 10^{-3} \mathrm{m}\) is the pipe's inner diameter and \(L\) is the length of the pipe. \(q = 50 \cdot \pi(25 \times 10^{-3})L (373.15 - 293.15)\)
03

Calculate the thermal conductivity at the average temperature

First, we need to find the average temperature between the inner surface and ambient temperatures: \(T_{avg} = \frac{T_{i} + T_{\infty}}{2} = 333.15 \mathrm{K}\) Now, we can calculate the thermal conductivity, \(k(T)\), at the average temperature: \(k(T_{avg}) = k_{0}(1 + \beta T_{avg}) = 1.5(1 + 0.003 \cdot 333.15)\)
04

Calculate the heat transfer through the pipe using conduction

Using the conduction heat transfer formula, we can find the heat transfer, \(q\): \(q = kA\frac{T_{i} - T_{o}}{t}\)
05

Equate the convection and conduction heat transfer equations and solve for the outer surface temperature

Now we set the convection and conduction heat transfer equations equal to each other and solve for \(T_{o}\): \(50 \cdot \pi(25 \times 10^{-3})L (373.15 - 293.15) = 1.5(1 + 0.003 \cdot 333.15) \cdot \pi(25 \times 10^{-3})L \frac{T_{i} - T_{o}}{3 \times 10^{-3}}\) Solve for \(T_{o}\): \(T_{o} = T_{i} - \frac{50(373.15 - 293.15)}{1.5(1 + 0.003 \cdot 333.15) \cdot \frac{1}{3 \times 10^{-3}}} = 339.38 \mathrm{K}\)
06

Convert the outer surface temperature back to Celsius

Our final step is to convert \(T_{o}\) back to Celsius: \(T_{o} = 339.38 \mathrm{K} - 273.15 = 66.23 ^{\circ} \mathrm{C}\) The outer surface temperature of the pipe is approximately \(66.23 ^{\circ} \mathrm{C}\).

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Key Concepts

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

Convection Heat Transfer
Convection heat transfer is a process where heat is transferred between a solid surface and a liquid or gas. This happens through the motion of the fluid or gas against the surface. The movement enhances the heat exchange rate, making it a crucial mode of heat transfer.
This transfer is quantified by the convection heat transfer coefficient, denoted as \( h \). This coefficient varies depending on the fluid properties, the surface area involved, and the temperature difference between the surface and the surrounding fluid.
In the context of the pipe example, the ambient air at 20°C cools the pipe's outer surface through convection. The formula used to calculate this transfer is:
\[ q = hA(T_i - T_{\infty}) \]
where:
  • \( q \) is the heat transfer rate
  • \( h \) is the convection heat transfer coefficient
  • \( A \) is the surface area through which heat is being transferred
  • \( T_i \) and \( T_{\infty} \) are the temperatures of the inner surface of the pipe and the ambient air, respectively
This equation underscores the importance of temperature differences in driving the rate of heat transfer through convection.
Conduction Heat Transfer
Conduction heat transfer involves the movement of heat within a solid or between solids in direct contact. It is a molecular process, where heat is transferred through collisions and diffusion of molecules inside the material.
This type of heat transfer is characterized by the material's thickness and thermal conductivity. In the case of the pipe, conduction takes place through the pipe's wall.
The basic formula to describe conduction heat transfer is:
\[ q = kA\frac{(T_i - T_o)}{t} \]
where:
  • \( q \) is the rate of heat transfer
  • \( k \) is thermal conductivity of the material
  • \( A \) is the cross-sectional area
  • \( T_i \) and \( T_o \) are the temperatures of the inner and outer surfaces of the pipe, respectively
  • \( t \) is the thickness of the pipe wall
Solving the exercise, the conduction equation helps establish a connection between the thermal energy lost from the inner surface to the outer surface, allowing us to calculate parameters like the outer surface temperature.
Thermal Conductivity
Thermal conductivity is a property of a material that indicates its ability to conduct heat. This property varies based on the material's structure, temperature, and other factors.
In the given exercise, the thermal conductivity of the pipe's material is not constant. It changes with temperature according to the formula:
\[ k(T) = k_0(1 + \beta T) \]
Where:
  • \( k_0 \) is the base thermal conductivity at a reference temperature
  • \( \beta \) is the coefficient that represents how thermal conductivity changes with temperature
  • \( T \) is the temperature in Kelvin
Calculating the average thermal conductivity is crucial as it influences how effectively the pipe material can conduct heat from the inner to the outer surface. In the solution, the knowledge of variable thermal conductivity, which depends on temperature, allows for a more accurate calculation of heat transmission through the pipe material.

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Most popular questions from this chapter

The heat conduction equation in a medium is given in its simplest form as $$ \frac{1}{r} \frac{d}{d r}\left(r k \frac{d T}{d r}\right)+\dot{e}_{\text {gen }}=0 $$ Select the wrong statement below. (a) The medium is of cylindrical shape. (b) The thermal conductivity of the medium is constant. (c) Heat transfer through the medium is steady. (d) There is heat generation within the medium. (e) Heat conduction through the medium is one-dimensional.

A spherical container of inner radius \(r_{1}=2 \mathrm{~m}\), outer radius \(r_{2}=2.1 \mathrm{~m}\), and thermal conductivity \(k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is filled with iced water at \(0^{\circ} \mathrm{C}\). The container is gaining heat by convection from the surrounding air at \(T_{\infty}=25^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=18 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming the inner surface temperature of the container to be \(0^{\circ} \mathrm{C},(a)\) express the differential equation and the boundary conditions for steady one- dimensional heat conduction through the container, \((b)\) obtain a relation for the variation of temperature in the container by solving the differential equation, and \((c)\) evaluate the rate of heat gain to the iced water.

Consider a large plane wall of thickness \(L=0.3 \mathrm{~m}\), thermal conductivity \(k=2.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=\) \(12 \mathrm{~m}^{2}\). The left side of the wall at \(x=0\) is subjected to a net heat flux of \(\dot{q}_{0}=700 \mathrm{~W} / \mathrm{m}^{2}\) while the temperature at that surface is measured to be \(T_{1}=80^{\circ} \mathrm{C}\). 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 temperature of the right surface of the wall at \(x=L\).

A solar heat flux \(\dot{q}_{s}\) is incident on a sidewalk whose thermal conductivity is \(k\), solar absorptivity is \(\alpha_{s}\), and convective heat transfer coefficient is \(h\). Taking the positive \(x\) direction to be towards the sky and disregarding radiation exchange with the surroundings surfaces, the correct boundary condition for this sidewalk surface is (a) \(-k \frac{d T}{d x}=\alpha_{s} \dot{q}_{s}\) (b) \(-k \frac{d T}{d x}=h\left(T-T_{\infty}\right)\) (c) \(-k \frac{d T}{d x}=h\left(T-T_{\infty}\right)-\alpha_{s} \dot{q}_{s}\) (d) \(h\left(T-T_{\infty}\right)=\alpha_{s} \dot{q}_{s}\) (e) None of them

A long homogeneous resistance wire of radius \(r_{o}=\) \(0.6 \mathrm{~cm}\) and thermal conductivity \(k=15.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is being used to boil water at atmospheric pressure by the passage of electric current. Heat is generated in the wire uniformly as a result of resistance heating at a rate of \(16.4 \mathrm{~W} / \mathrm{cm}^{3}\). The heat generated is transferred to water at \(100^{\circ} \mathrm{C}\) by convection with an average heat transfer coefficient of \(h=3200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming steady one-dimensional heat transfer, \((a)\) express the differential equation and the boundary conditions for heat conduction through the wire, \((b)\) obtain a relation for the variation of temperature in the wire by solving the differential equation, and \((c)\) determine the temperature at the centerline of the wire.

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