Chapter 8: Problem 16
What does the logarithmic mean temperature difference represent for flow in a tube whose surface temperature is constant? Why do we use the logarithmic mean temperature instead of the arithmetic mean temperature?
Chapter 8: Problem 16
What does the logarithmic mean temperature difference represent for flow in a tube whose surface temperature is constant? Why do we use the logarithmic mean temperature instead of the arithmetic mean temperature?
All the tools & learning materials you need for study success - in one app.
Get started for freeA tube with a square-edged inlet configuration is subjected to uniform wall heat flux of \(8 \mathrm{~kW} / \mathrm{m}^{2}\). The tube has an inside diameter of \(0.622\) in and a flow rate of \(2.16 \mathrm{gpm}\). The liquid flowing inside the tube is an ethylene glycol-distilled water mixture with a mass fraction of \(2.27\). Determine the friction coefficient at a location along the tube where the Grashof number is Gr \(=35,450\). The physical properties of the ethylene glycol-distilled water mixture at the location of interest are $\operatorname{Pr}=13.8, \nu=18.4 \times 10^{-6} \mathrm{ft}^{2} / \mathrm{s}\(, and \)\mu_{b} / \mu_{s}=1.12$. Then recalculate the fully developed friction coefficient if the volume flow rate is increased by 50 percent while the rest of the parameters remain unchanged.
A fluid $\left(\rho=1000 \mathrm{~kg} / \mathrm{m}^{3}, \mu=1.4 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\right.\(, \)c_{p}=4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\(, and \)k=0.58 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( ) flows with an average velocity of \)0.3 \mathrm{~m} / \mathrm{s}$ through a \(14-\mathrm{m}\)-long tube with inside diameter of $0.01 \mathrm{~m}\(. Heat is uniformly added to the entire tube at the rate of \)1500 \mathrm{~W} / \mathrm{m}^{2}\(. Determine \)(a)$ the value of convection heat transfer coefficient at the exit, \((b)\) the value of \(T_{s}-T_{\text {m }}\), and (c) the value of \(T_{e}-T_{i}\).
consider fully developed flow in a circular pipe with negligible entrance effects. If the length of the pipe is doubled, the pressure drop will \((a)\) double, \((b)\) more than double, (c) less than double, \((d)\) reduce by half, or \((e)\) remain constant.
Liquid water flows in a circular tube at a mass flow rate of $7 \mathrm{~g} / \mathrm{s}\(. The water enters the tube at \)5^{\circ} \mathrm{C}$, and the average convection heat transfer coefficient for the internal flow is $20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The tube is \)3 \mathrm{~m}$ long and has an inner diameter of \(25 \mathrm{~mm}\). The tube surface is maintained at a constant temperature. The inner surface of the tube is lined with polyvinylidene chloride (PVDC) lining. According to the ASME Code for Process Piping (ASME B31.3-2014, Table A.323.4.3), the recommended maximum temperature for PVDC lining is \(79^{\circ} \mathrm{C}\). If the water exits the tube at \(15^{\circ} \mathrm{C}\), determine the heat rate transferred to the water. Would the inner surface temperature of the tube exceed the recommended maximum temperature for PVDC lining?
Consider the velocity and temperature profiles for a fluid flow in a tube with a diameter of \(50 \mathrm{~mm}\) that can be expressed as $$ \begin{aligned} &u(r)=0.05\left[1-(r / R)^{2}\right] \\ &T(r)=400+80(r / R)^{2}-30(r / R)^{3} \end{aligned} $$ with units in \(\mathrm{m} / \mathrm{s}\) and \(\mathrm{K}\), respectively. Determine the average velocity and the mean (average) temperature from the given velocity and temperature profiles.
What do you think about this solution?
We value your feedback to improve our textbook solutions.