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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?

Short Answer

Expert verified
Based on the analysis and solution provided, the short answer is: The heat flux will be higher near the inlet of a circular tube under laminar forced convection conditions, due to the higher temperature gradient between the wall and the fluid at the inlet as compared to the exit.

Step by step solution

01

Understand laminar forced convection in a circular tube

In a laminar forced convection flow, the fluid moves in parallel layers, and the heat is transferred primarily through the conduction mechanism. When a fluid flows through a circular tube, the flow near the walls is slowed down due to viscous effects, resulting in a velocity profile that is parabolic in nature.
02

Recognize the importance of temperature gradient

Heat flux is directly proportional to the temperature gradient, which is the difference in temperature across the fluid layer. Higher temperature gradient means higher heat transfer rate. Therefore, we need to analyze how the temperature gradient varies along the length of the circular tube.
03

Analyze the temperature gradient near the inlet and the exit of the tube

When the fluid enters the tube, it has a uniform temperature distribution. As it flows through the tube and gets heated, the temperature near the wall increases. Since the velocity of the fluid near the wall is lower than the velocity at the center of the tube, the temperature gradient near the wall is higher compared to the center of the tube. Hence, we can expect a higher heat flux near the inlet. As the fluid moves along the length of the tube towards its exit, the overall temperature of the fluid increases, and the temperature gradient between the wall and the fluid reduces. The velocity profile remains parabolic, but the temperature difference along the flow length decreases. This results in a lower heat flux near the exit.
04

Conclude the answer

The heat flux will be higher near the inlet of the circular tube compared to the exit. This is because, near the inlet, the temperature gradient between the wall and the fluid is higher, and as the fluid flows towards the exit, the temperature gradient decreases due to the increase in the overall fluid temperature. Thus, the heat transfer rate is higher at the inlet than at the exit.

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Most popular questions from this chapter

Liquid water enters a 10 -m-long smooth rectangular tube with $a=50 \mathrm{~mm}\( and \)b=25 \mathrm{~mm}$. The surface temperature is kept constant, and water enters the tube at \(20^{\circ} \mathrm{C}\) with a mass flow rate of \(0.25 \mathrm{~kg} / \mathrm{s}\). Determine the tube surface temperature necessary to heat the water to the desired outlet temperature of \(80^{\circ} \mathrm{C}\).

In a heating system, liquid water flows in a circuof \(12.5 \mathrm{~mm}\). The water enters the tube at \(15^{\circ} \mathrm{C}\), where it is heated at a rate of \(1.5 \mathrm{~kW}\). The tube surface is maintained at a constant temperature. The flow is laminar, and it experiences a pressure loss of $5 \mathrm{~Pa}$ in the tube. According to the service restrictions of the ASME Boiler and Pressure Vessel Code (ASME BPVC.IV-2015, HG-101), hot water heaters should not be operating at temperatures exceeding \(120^{\circ} \mathrm{C}\) at or near the heater outlet. The tube's inner surface is lined with polyvinylidene fluoride (PVDF) lining. According to the ASME Code for Process Piping (ASME B31.3-2014, Table A323.4.3), the recommended maximum temperature for PVDF lining is \(135^{\circ} \mathrm{C}\). To comply with both ASME codes, determine (a) whether the water exiting the tube is at a temperature below \(120^{\circ} \mathrm{C}\), and (b) whether the inner surface temperature of the tube exceeds \(135^{\circ} \mathrm{C}\). Evaluate the fluid properties at \(80^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?

Liquid water flows in a circular tube at a mass flow rate of $0.12 \mathrm{~kg} / \mathrm{s}\(. The water enters the tube at \)65^{\circ} \mathrm{C}\(, where it is heated at a rate of \)5.5 \mathrm{~kW}$. The tube is circular with a length of \(3 \mathrm{~m}\) and an inner diameter of $25 \mathrm{~mm}$. The tube surface is maintained isothermal. The inner surface of the tube is lined with polyvinylidene chloride (PVDC) lining. The recommended maximum temperature for PVDC lining is \(79^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A323.4.3). Is the PVDC lining suitable for the tube under these conditions? Evaluate the fluid properties at \(70^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?

Water enters a 2-cm-diameter and 3-m-long tube whose walls are maintained at \(100^{\circ} \mathrm{C}\) with a bulk temperature of \(25^{\circ} \mathrm{C}\) and a volume flow rate of \(3 \mathrm{~m}^{3} / \mathrm{h}\). Neglecting the entrance effects and assuming turbulent flow, the Nusselt number can be determined from \(\mathrm{Nu}=0.023 \mathrm{Re}^{0.8} \mathrm{Pr}^{0.4}\). The convection heat transfer coefficient in this case is (a) \(4140 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(6160 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(8180 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(9410 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(2870 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (For water, use $k=0.610 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=6.0, \mu=9.0 \times\( \)10^{-4} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}, \rho=1000 \mathrm{~kg} / \mathrm{m}^{3}$.)

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