Chapter 2: Problem 139
How do differential equations with constant coefficients differ from those with variable coefficients? Give an example for each type.
Chapter 2: Problem 139
How do differential equations with constant coefficients differ from those with variable coefficients? Give an example for each type.
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Get started for freeLiquid water flows in a tube with the inner surface lined with polytetrafluoroethylene (PTFE). The inner diameter of the tube is $24 \mathrm{~mm}\(, and its wall thickness is \)5 \mathrm{~mm}$. The thermal conductivity of the tube wall is $15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(. The water flowing in the tube has a temperature of \)50^{\circ} \mathrm{C}$, and the convection heat transfer coefficient with the inner tube surface is \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The outer surface of the tube is exposed to convection with superheated steam at \(600^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of $50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. According to the ASME Code for Process Piping (ASME B31.3-2014, A323), the recommended maximum temperature for PTFE lining is \(260^{\circ} \mathrm{C}\). Formulate the temperature profile in the tube wall. Use the temperature profile to determine if the tube inner surface is in compliance with the ASME Code for Process Piping.
A long homogeneous resistance wire of radius \(r_{o}=5 \mathrm{~mm}\) is being used to heat the air in a room by the passage of electric current. Heat is generated in the wire uniformly at a rate of $5 \times 10^{7} \mathrm{~W} / \mathrm{m}^{3}$ as a result of resistance heating. If the temperature of the outer surface of the wire remains at \(180^{\circ} \mathrm{C}\), determine the temperature at \(r=3.5 \mathrm{~mm}\) after steady operation conditions are reached. Take the thermal conductivity of the wire to be $k=8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(. Answer: \)200^{\circ} \mathrm{C}$
In 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 20-cm-thick large concrete plane wall $(k=0.77 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ subjected to convection on both sides with \(T_{\infty 1}=22^{\circ} \mathrm{C}\) and $h_{1}=8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( on the inside and \)T_{\infty 22}=8^{\circ} \mathrm{C}$ and \(h_{2}=12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on the outside. Assuming constant thermal conductivity with no heat generation and negligible radiation, \((a)\) express the differential equations 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 temperatures at the inner and outer surfaces of the wall.
A spherical vessel is filled with chemicals undergoing an exothermic reaction. The reaction provides a uniform heat flux on the inner surface of the vessel. The inner diameter of the vessel is \(5 \mathrm{~m}\) and its inner surface temperature is at \(120^{\circ} \mathrm{C}\). The wall of the vessel has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where $k_{0}=1.01 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \beta=0.0018 \mathrm{~K}^{-1}\(, and \)T\( is in \)\mathrm{K}$. The vessel is situated in a surrounding with an ambient temperature of \(15^{\circ} \mathrm{C}\), and the vessel's outer surface experiences convection heat transfer with a coefficient of \(80 \mathrm{~W} / \mathrm{m}^{2}\). K. To prevent thermal burns to workers who touch the vessel, the outer surface temperature of the vessel should be kept below \(50^{\circ} \mathrm{C}\). Determine the minimum wall thickness of the vessel so that the outer surface temperature is \(50^{\circ} \mathrm{C}\) or lower.
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