Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

Heat transfer coefficients for a vapor condensing on a surface can be increased by promoting (a) film condensation (b) dropwise condensation (c) rolling action (d) none of them

Short Answer

Expert verified
Answer: Dropwise condensation.

Step by step solution

01

Understanding film condensation

Film condensation occurs when the vapor condenses on the surface and forms a continuous liquid film. The heat transfer in this case is mainly through the flowing liquid film, which has relatively lower thermal conductivity compared to the vapor. As the film thickness increases, the overall heat transfer coefficient decreases, leading to lower efficiency.
02

Understanding dropwise condensation

Dropwise condensation occurs when the vapor condenses as individual droplets on the surface, which then combine and roll off the surface when they reach a certain size. The heat transfer in this case is much more efficient as the droplets expose more surface area between the vapor and the coolant. This allows for quicker and more effective heat transfer, resulting in higher heat transfer coefficients compared to film condensation.
03

Understanding rolling action

Rolling action refers to the movement of liquid droplets on the surface, which also aids in heat transfer. However, this movement is more associated with dropwise condensation, as it involves the movement and combination of droplets on the surface. Thus, rolling action itself is not an independent process that enhances heat transfer coefficients in vapor condensation on a surface.
04

Identify the correct option

Now that we have understood film and dropwise condensation, and their effects on heat transfer coefficients, we can choose the correct option. It is clear that promoting dropwise condensation increases the heat transfer coefficient. Hence, the correct option is (b) dropwise condensation.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Saturated steam at 1 atm condenses on a \(2-\mathrm{m}\)-high and 10 -m-wide vertical plate that is maintained at \(90^{\circ} \mathrm{C}\) by circulating cooling water through the other side. Determine (a) the rate of heat transfer by condensation to the plate, and (b) the rate at which the condensate drips off the plate at the bottom. Assume wavy-laminar flow. Is this a good assumption?

Consider a non-boiling gas-liquid two-phase flow in a tube, where the ratio of the mass flow rate is \(\dot{m}_{l} / \dot{m}_{g}=300\). Determine the flow quality \((x)\) of this non-boiling two-phase flow.

Saturated steam at \(55^{\circ} \mathrm{C}\) is to be condensed at a rate of $10 \mathrm{~kg} / \mathrm{h}$ on the outside of a 3 -cm-outer-diameter vertical tube whose surface is maintained at \(45^{\circ} \mathrm{C}\) by the cooling water. Determine the required tube length. Assume wavy-laminar flow and that the tube diameter is large relative to the thickness of the liquid film at the bottom of the tube. Are these good assumptions?

Water is boiled at atmospheric pressure by a horizontal polished copper heating element of diameter \(D=0.5\) in and emissivity \(\varepsilon=0.2\) immersed in water. If the surface temperature of the heating element is \(788^{\circ} \mathrm{F}\), determine the rate of heat transfer to the water per unit length of the heating element.

A \(10-\mathrm{cm} \times 10\)-cm horizontal flat heater is used for vaporizing refrigerant- \(134 \mathrm{a}\) at \(350 \mathrm{kPa}\). The heater is supplied with \(0.35 \mathrm{MW} / \mathrm{m}^{2}\) of heat flux, and the surface temperature of the heater is \(25^{\circ} \mathrm{C}\). If the experimental constant in the Rohsenow correlation is \(n=1.7\), determine the value of the coefficient \(C_{s f}\). Discuss whether or not the Rohsenow correlation is applicable in this analysis.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free