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What is a semi-infinite medium? Give examples of solid bodies that can be treated as semi-infinite media for heat transfer purposes.

Short Answer

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Answer: A semi-infinite medium is a material that extends to infinity in one direction, while the other dimensions are finite. This simplification is often used in heat transfer problems to make calculations more manageable. Examples of solid bodies that can be treated as semi-infinite media for heat transfer purposes include the surface of a large solid (e.g. ground or large structure), a very thin slab, thick insulation layers, and pipes with a long length and small diameter. These examples assume temperature changes occur primarily in one direction, making the other dimensions negligible for calculations.

Step by step solution

01

Definition of a Semi-infinite Medium

A semi-infinite medium refers to a material that extends to infinity in one direction, while the other dimensions are finite. This is a simplification often used in heat transfer problems to make calculations more manageable, assuming that any heat transfer in the infinite direction has negligible effects on the overall process.
02

Example 1: Surface of a Large Solid

A common example of a semi-infinite medium in heat transfer is the surface of a large solid, such as the ground or a large structure. During heat transfer, the temperature at the surface interacts with the surrounding fluid, causing conduction within the solid. For modeling purposes, the solid can be treated as a semi-infinite medium since the heat transfer occurs primarily near the surface, with negligible effects deep within the solid.
03

Example 2: Thin Slab

Another example of a semi-infinite medium is a very thin slab, where the thickness is small compared to the other dimensions. In this case, heat transfer can be assumed to occur only in the thickness direction, and the slab can be treated as a semi-infinite medium to simplify calculations.
04

Example 3: Thick Insulation Layers

Large structures, such as buildings or industrial equipment, often have thick insulation layers that can also be considered a semi-infinite medium. Since the insulation layers are much thicker than their width and height dimensions, heat transfer occurs primarily in the depth direction of the insulation, and the insulation can be treated as a semi-infinite medium.
05

Example 4: Pipes

Pipes with a long length and relatively small diameter can also be treated as semi-infinite media for heat transfer purposes. The assumption is that temperature changes occur predominantly along the axial length of the pipe while the heat transfer in the radial direction is considered negligible. This simplification can be applied to model heat losses or gains in the pipe flow.

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Most popular questions from this chapter

Carbon steel balls $\left(\rho=7833 \mathrm{~kg} / \mathrm{m}^{3}, k=54 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\(, \)c_{p}=0.465 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}\(, and \)\left.\alpha=1.474 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right) 8 \mathrm{~mm}$ in diameter are annealed by heating them first to \(900^{\circ} \mathrm{C}\) in a furnace and then allowing them to cool slowly to \(100^{\circ} \mathrm{C}\) in ambient air at \(35^{\circ} \mathrm{C}\). If the average heat transfer coefficient is $75 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine how long the annealing process will take. If 2500 balls are to be annealed per hour, determine the total rate of heat transfer from the balls to the ambient air.

Polyvinylchloride automotive body panels \((k=0.092\) $\left.\mathrm{W} / \mathrm{m} \cdot \mathrm{K}, c_{p}=1.05 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, \rho=1714 \mathrm{~kg} / \mathrm{m}^{3}\right), 1 \mathrm{~mm}$ thick, emerge from an injection molder at \(120^{\circ} \mathrm{C}\). They need to be cooled to \(40^{\circ} \mathrm{C}\) by exposing both sides of the panels to \(20^{\circ} \mathrm{C}\) air before they can be handled. If the convective heat transfer coefficient is $15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and radiation is not considered, the time that the panels must be exposed to air before they can be handled is (a) \(0.8 \mathrm{~min}\) (b) \(1.6 \mathrm{~min}\) (c) \(2.4 \mathrm{~min}\) (d) \(3.1 \mathrm{~min}\) (e) \(5.6 \mathrm{~min}\)

A large cast iron container \((k=52 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\alpha=1.70 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\) ) with \(4-\mathrm{cm}\)-thick walls is initially at a uniform temperature of \(0^{\circ} \mathrm{C}\) and is filled with ice at \(0^{\circ} \mathrm{C}\). Now the outer surfaces of the container are exposed to hot water at $55^{\circ} \mathrm{C}$ with a very large heat transfer coefficient. Determine how long it will be before the ice inside the container starts melting. Also, taking the heat transfer coefficient on the inner surface of the container to be $250 \mathrm{~W} / \mathrm{m}^{2}\(, \)\mathrm{K}$, determine the rate of heat transfer to the ice through a \(1.2-\mathrm{m}\)-wide and \(2-\mathrm{m}\)-high section of the wall when steady operating conditions are reached. Assume the ice starts melting when its inner surface temperature rises to $0.1^{\circ} \mathrm{C}$.

Spherical glass beads coming out of a kiln are allowed to cool in a room temperature of \(30^{\circ} \mathrm{C}\). A glass bead with a diameter of $10 \mathrm{~mm}\( and an initial temperature of \)400^{\circ} \mathrm{C}$ is allowed to cool for \(3 \mathrm{~min}\). If the convection heat transfer coefficient is \(28 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the temperature at the center of the glass bead using the analytical one-term approximation method. The glass bead has properties of $\rho=2800 \mathrm{~kg} / \mathrm{m}^{3}\(, \)c_{p}=750 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$, and \(k=0.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\).

Hailstones are formed in high-altitude clouds at \(253 \mathrm{~K}\). Consider a hailstone with diameter of \(20 \mathrm{~mm}\) that is falling through air at \(15^{\circ} \mathrm{C}\) with convection heat transfer coefficient of $163 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Assuming the hailstone can be modeled as a sphere and has properties of ice at \(253 \mathrm{~K}\), determine how long it takes to reach melting point at the surface of the falling hailstone. Solve this problem using the analytical one-term approximation method.

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