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Consider film condensation on the outer surfaces of four long tubes. For which orientation of the tubes will the condensation heat transfer coefficient be the highest: \((a)\) vertical, \((b)\) horizontal side by side, \((c)\) horizontal but in a vertical tier (directly on top of each other), or \((d)\) a horizontal stack of two tubes high and two tubes wide?

Short Answer

Expert verified
Answer: The highest condensation heat transfer coefficient will be achieved for the vertical orientation (a) of the tubes.

Step by step solution

01

Plan of Action

The plan of action should involve evaluating the heat transfer coefficient for each orientation based on the effect of gravity on condensate draining and thermal state of the outer surface. The orientation that results in the maximum heat transfer coefficient will be selected as the answer.
02

Orientation (a): Vertical

In the vertical orientation, the tubes are aligned vertically. This allows gravity to assist in condensate drainage, leading to a thinner condensate film on the tube surfaces. A thinner condensate film means reduced thermal resistance and thus a higher heat transfer coefficient. Moreover, the tube surfaces have a uniform temperature throughout.
03

Orientation (b): Horizontal Side by Side

For horizontal side by side orientation, the tubes are placed horizontally and parallel to each other. The condensate accumulates at the bottom of the tube surface due to gravity and must flow along the circumference of the tubes. This creates a non-uniform temperature distribution along the tube surface, leading to a reduction in heat transfer coefficient as compared to the vertical orientation.
04

Orientation (c): Horizontal in a Vertical Tier

In this orientation, the tubes are horizontally placed but in a vertical tier (directly on top of each other). The condensate from the upper tubes tends to flow downwards and accumulate on the lower tubes, leading to a thicker film of condensate on the bottom tubes. This increases the thermal resistance and lowers the heat transfer coefficient compared to the vertical orientation.
05

Orientation (d): Horizontal Stack of Two Tubes High and Two Tubes Wide

In this configuration, there are a total of four tubes, two tubes on top of each other and two tubes side by side. This makes it difficult for the condensate drainage due to the interference caused by adjacent tubes. The increased condensate thickness on tubes and the non-uniform temperature distribution lead to lower heat transfer coefficients, as compared to the vertical orientation.
06

Conclusion

Comparing the four orientations, it is found that in the vertical orientation (a), gravity aids condensate drainage and results in a uniform temperature distribution on the tube surface, both factors leading to higher heat transfer coefficients. Therefore, the highest condensation heat transfer coefficient will be achieved for \((a)\) vertical orientation of the tubes.

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Most popular questions from this chapter

Consider film condensation on a vertical plate. Will the heat flux be higher at the top or at the bottom of the plate? Why?

A manufacturing facility requires saturated steam at \(120^{\circ} \mathrm{C}\) at a rate of \(1.2 \mathrm{~kg} / \mathrm{min}\). Design an electric steam boiler for this purpose under these constraints: \- The boiler will be cylindrical with a height-to-diameter ratio of \(1.5\). The boiler can be horizontal or vertical. \- The boiler will operate in the nucleate boiling regime, and the design heat flux will not exceed 60 percent of the critical heat flux to provide an adequate safety margin. \- A commercially available plug-in-type electrical heating element made of mechanically polished stainless steel will be used. The diameter of the heater cannot be between \(0.5 \mathrm{~cm}\) and \(3 \mathrm{~cm}\). \- Half of the volume of the boiler should be occupied by steam, and the boiler should be large enough to hold enough water for a \(2-\mathrm{h}\) supply of steam. Also, the boiler will be well insulated. You are to specify the following: (a) The height and inner diameter of the tank, \((b)\) the length, diameter, power rating, and surface temperature of the electric heating element, (c) the maximum rate of steam production during short periods of overload conditions, and how it can be accomplished.

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Mechanically polished, 5 -cm-diameter, stainless steel ball bearings are heated to \(125^{\circ} \mathrm{C}\) uniformly. The ball bearings are then submerged in water at \(1 \mathrm{~atm}\) to be cooled. Determine the rate of heat that is removed from a ball bearing at the instant it is submerged in the water.

Consider a two-phase flow of air-water in a vertical upward stainless steel pipe with an inside diameter of \(0.0254\) \(\mathrm{m}\). The two-phase mixture enters the pipe at \(25^{\circ} \mathrm{C}\) at a system pressure of $201 \mathrm{kPa}\(. The superficial velocities of the water and air are \)0.3 \mathrm{~m} / \mathrm{s}\( and \)23 \mathrm{~m} / \mathrm{s}$, respectively. The differential pressure transducer connected across the pressure taps set $1 \mathrm{~m}\( apart records a pressure drop of \)2700 \mathrm{~Pa}$, and the measured value of the void fraction is \(0.86\). Using the concept of the Reynolds analogy, determine the two-phase convective heat transfer coefficient. Use the following thermophysical properties for water and air: $\rho_{l}=997.1 \mathrm{~kg} / \mathrm{m}^{3}, \mu_{l}=8.9 \times 10^{-4} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}, \mu_{s}=4.66 \times\( \)10^{-4} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}, \operatorname{Pr}_{l}=6.26, k_{l}=0.595 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \sigma=0.0719 \mathrm{~N} / \mathrm{m}\(, \)\rho_{g}=2.35 \mathrm{~kg} / \mathrm{m}^{3}$, and \(\mu_{g}=1.84 \times 10^{-5} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\).

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