Chapter 8: Problem 9
How does surface roughness affect the pressure drop in a tube if the flow is turbulent? What would your response be if the flow were laminar?
Chapter 8: Problem 9
How does surface roughness affect the pressure drop in a tube if the flow is turbulent? What would your response be if the flow were laminar?
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Get started for freeInternal force flows are said to be fully developed once the _____ at a cross section no longer changes in the direction of flow. (a) temperature distribution (b) entropy distribution (c) velocity distribution (d) pressure distribution (e) none of the above
Liquid water flows in fully developed conditions through a circular tube at a mass flow rate of \(3.5 \mathrm{~g} / \mathrm{s}\). 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 subjected to a constant heat flux at a rate of \(300 \mathrm{~W}\). 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 A323.4.3), the recommended maximum temperature for PVDC lining is \(79^{\circ} \mathrm{C}\). Would the inner surface temperature of the tube exceed the recommended maximum temperature for PVDC lining? If so, determine the axial location along the tube where the tube's inner surface temperature reaches $79^{\circ} \mathrm{C}\(. Evaluate the fluid properties at \)15^{\circ} \mathrm{C}$. Is this an appropriate temperature at which to evaluate the fluid properties?
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?
Determine the average velocity and hydrodynamic and thermal entry lengths for water, engine oil, and liquid mercury flowing through a standard 2 -in Schedule 40 pipe with a mass flow rate of \(0.1 \mathrm{lbm} / \mathrm{s}\) and a temperature of \(100^{\circ} \mathrm{F}\).
Water enters a 5-mm-diameter and 13 -m-long tube at \(15^{\circ} \mathrm{C}\) with a velocity of \(0.3 \mathrm{~m} / \mathrm{s}\) and leaves at $45^{\circ} \mathrm{C}\(. The tube is subjected to a uniform heat flux of \)2000 \mathrm{~W} / \mathrm{m}^{2}$ on its surface. The temperature of the tube surface at the exit is (a) \(48.7^{\circ} \mathrm{C}\) (b) \(49.4^{\circ} \mathrm{C}\) (c) \(51.1^{\circ} \mathrm{C}\) (d) \(53.7^{\circ} \mathrm{C}\) (e) \(55.2^{\circ} \mathrm{C}\) (For water, use $k=0.615 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=5.42, \nu=0.801 \times\( \)10^{-6} \mathrm{~m}^{2} / \mathrm{s}$.)
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