Chapter 8: Problem 11
Consider the flow of oil in a tube. How will the hydrodynamic and thermal entry lengths compare if the flow is laminar? How would they compare if the flow were turbulent?
Chapter 8: Problem 11
Consider the flow of oil in a tube. How will the hydrodynamic and thermal entry lengths compare if the flow is laminar? How would they compare if the flow were turbulent?
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Get started for freeIn a manufacturing plant that produces cosmetic products, glycerin is being heated by flowing through a \(25-\mathrm{mm}-\) diameter and 10 -m-long tube. With a mass flow rate of \(0.5 \mathrm{~kg} / \mathrm{s}\), the flow of glycerin enters the tube at \(25^{\circ} \mathrm{C}\). The tube surface is maintained at a constant surface temperature of \(140^{\circ} \mathrm{C}\). Determine the outlet mean temperature and the total rate of heat transfer for the tube. Evaluate the properties for glycerin at \(30^{\circ} \mathrm{C}\).
Consider laminar forced convection in a circular tube. Will the heat flux be higher near the inlet of the tube or near the exit? Why?
Liquid water flows in a thin-walled circular tube, where the pumping power required to overcome the turbulent flow pressure loss in the tube is $100 \mathrm{~W}\(. The water enters the tube at \)10^{\circ} \mathrm{C}$, where it is heated at a rate of \(3.6 \mathrm{~kW}\). The average convection heat transfer coefficient for the internal flow is $120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The tube is \)3 \mathrm{~m}$ long and has an inner diameter of \(12.5 \mathrm{~mm}\). The tube surface is maintained at a constant temperature. At the tube exit, an ethylene propylene diene (EPDM) rubber o-ring is attached to the tube's outer surface. The maximum temperature permitted for the o-ring is \(150^{\circ} \mathrm{C}\) (ASME Boiler and Pressure Vessel Code, BPVC. IV-2015, HG-360). Is the EPDM o-ring suitable for this operation? Evaluate the fluid properties at \(10^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?
In a chemical process plant, liquid isobutane at \(50^{\circ} \mathrm{F}\) is being transported through a 30 -ft-long standard \(3 / 4\)-in Schedule 40 cast iron pipe with a mass flow rate of \(0.4 \mathrm{lbm} / \mathrm{s}\). Accuracy of the results is an important issue in this problem; therefore, use the most appropriate equation to determine (a) the pressure loss and \((b)\) the pumping power required to overcome the pressure loss. Assume flow is fully developed. Is this a good assumption?
The components of an electronic system dissipating \(220 \mathrm{~W}\) are located in a 1 -m-long horizontal duct whose cross section is $16 \mathrm{~cm} \times 16 \mathrm{~cm}$. The components in the duct are cooled by forced air, which enters at \(27^{\circ} \mathrm{C}\) at a rate of $0.65 \mathrm{~m}^{3} / \mathrm{min}$. Assuming 85 percent of the heat generated inside is transferred to air flowing through the duct and the remaining 15 percent is lost through the outer surfaces of the duct, determine \((a)\) the exit temperature of air and \((b)\) the highest component surface temperature in the duct. As a first approximation, assume fully developed turbulent flow in the channel. Evaluate the properties of air at a bulk mean temperature of \(35^{\circ} \mathrm{C}\). Is this a good assumption?
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