Chapter 2: Problem 12
Consider the cooking process of a roast beef in an oven. Would you consider this to be a steady or a transient heat transfer problem? Also, would you consider this to be one-, two-, or three-dimensional? Explain.
Chapter 2: Problem 12
Consider the cooking process of a roast beef in an oven. Would you consider this to be a steady or a transient heat transfer problem? Also, would you consider this to be one-, two-, or three-dimensional? Explain.
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Get started for freeIn metal processing plants, workers often operate near hot metal surfaces. Exposed hot surfaces are hazards that can potentially cause thermal burns on human skin. Metallic surfaces above \(70^{\circ} \mathrm{C}\) are considered extremely hot. Damage to skin can occur instantaneously upon contact with metallic surfaces at that temperature. In a plant that processes metal plates, a plate is conveyed through a series of fans to cool its surface in an ambient temperature of \(30^{\circ} \mathrm{C}\). The plate is \(25 \mathrm{~mm}\) thick and has a thermal conductivity of $13.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The temperature at the bottom surface of the plate is monitored by an infrared (IR) thermometer. Obtain an expression for the variation of temperature in the metal plate. The IR thermometer measures the bottom surface of the plate to be \(60^{\circ} \mathrm{C}\). Determine the minimum value of the convection heat transfer coefficient needed to keep the top surface below \(47^{\circ} \mathrm{C}\).
Consider a steam pipe of length \(L=30 \mathrm{ft}\), inner radius $r_{1}=2 \mathrm{in}\(, outer radius \)r_{2}=2.4 \mathrm{in}$, and thermal conductivity $k=7.2 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}$. Steam is flowing through the pipe at an average temperature of \(250^{\circ} \mathrm{F}\), and the average convection heat transfer coefficient on the inner surface is given to be $h=12 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}$. If the average temperature on the outer surfaces of the pipe is \(T_{2}=160^{\circ} \mathrm{F},(a)\) express the differential equation and the boundary conditions for steady onedimensional heat conduction through the pipe, \((b)\) obtain a relation for the variation of temperature in the pipe by solving the differential equation, and (c) evaluate the rate of heat loss from the steam through the pipe.
How do you recognize a linear homogeneous differential equation? Give an example and explain why it is linear and homogeneous.
Does heat generation in a solid violate the first law of thermodynamics, which states that energy cannot be created or destroyed? Explain.
A heating cable is embedded in a concrete slab for snow melting on a $30 \mathrm{~m}^{2}$ surface area. The heating cable is heated electrically with joule heating. When the surface is covered with snow, the heat generated from the heating cable can melt snow at a rate of \(0.1 \mathrm{~kg} / \mathrm{s}\). According to the National Electrical Code (NFPA 70), the power density for embedded snow-melting equipment should not exceed $1300 \mathrm{~W} / \mathrm{m}^{2}$. Formulate the temperature profile in the concrete slab in terms of the snow melt rate. Determine whether melting snow at $0.1 \mathrm{~kg} / \mathrm{s}$ would be in compliance with the NFPA 70 code.
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