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What is boiling? What mechanisms are responsible for the very high heat transfer coefficients in nucleate boiling?

Short Answer

Expert verified
Answer: The high heat transfer coefficient in nucleate boiling is due to micro-layer evaporation, bubble nucleation, growth, and departure, as well as liquid agitation and mixing caused by rising bubbles.

Step by step solution

01

Define boiling

Boiling is a phase change process in which a liquid turns into a vapor when its temperature reaches the boiling point. The boiling point is the temperature at which the vapor pressure of the liquid equals the pressure exerted on it by the surrounding environment. Boiling occurs when the heat input to the liquid provides enough energy to overcome the intermolecular forces that hold the liquid together.
02

Overview of boiling regimes

There are several boiling regimes, which are distinguished based on the behavior of the liquid-vapor interface and the heat transfer mechanisms involved: 1. Natural convection: Heat transfer occurs by natural convection currents in the liquid, without boiling. 2. Nucleate boiling: The liquid forms vapor bubbles at discrete nucleation sites on the heated surface, which then grow and detach from the surface. 3. Transition boiling: A mixed-mode regime with a combination of nucleate boiling and film boiling. 4. Film boiling: The heated surface is covered with a continuous vapor film that insulates it from the liquid, leading to a low heat transfer coefficient. 5. Critical heat flux: The maximum heat flux that can be sustained without a significant drop in heat transfer coefficient, which is followed by a transition to film boiling.
03

Focus on nucleate boiling

Nucleate boiling is characterized by the formation of vapor bubbles on the heated surface, followed by bubble growth and detachment. This boiling regime has the highest heat transfer coefficient among the different boiling regimes. The high heat transfer coefficient in nucleate boiling is primarily due to the following mechanisms: 1. Micro-layer evaporation: At the nucleation site, a thin liquid micro-layer exists between the growing bubble and the heated surface. This micro-layer evaporates rapidly, causing the bubble to grow and transfer heat effectively. 2. Bubble nucleation, growth, and departure: Vapor bubbles form on nucleation sites on the heated surface, which then grow by absorbing surrounding liquid, and detach once they reach a certain size. This process continually exposes fresh liquid to the heated surface, promoting efficient heat transfer. 3. Liquid agitation and mixing: The motion of the rising bubbles creates local turbulence and mixing in the liquid, which enhances heat transfer by reducing the thermal boundary layer thickness and increasing the convective heat transfer coefficient.
04

Conclusion

Boiling is a phase change process in which a liquid turns into a vapor when its temperature reaches the boiling point. Nucleate boiling is a regime characterized by the formation and growth of vapor bubbles on the heated surface, which leads to a high heat transfer coefficient. The high heat transfer coefficient in nucleate boiling is due to micro-layer evaporation, bubble nucleation, growth, and departure, as well as liquid agitation and mixing caused by rising bubbles.

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Most popular questions from this chapter

The condenser of a steam power plant operates at a pressure of $4.25 \mathrm{kPa}$. The condenser consists of 144 horizontal tubes arranged in a \(12 \times 12\) square array. The tubes are \(8 \mathrm{~m}\) long and have an outer diameter of \(3 \mathrm{~cm}\). If the tube surfaces are at $20^{\circ} \mathrm{C}\(, determine \)(a)$ the rate of heat transfer from the steam to the cooling water and (b) the rate of condensation of steam in the condenser. Answers: (a) \(5060 \mathrm{~kW}\), (b) \(2.06 \mathrm{~kg} / \mathrm{s}\)

When a saturated vapor condenses on a vertical, isothermal flat plate in a continuous film, the rate of heat transfer is proportional to (a) \(\left(T_{s}-T_{\text {sat }}\right)^{1 / 4}\) (b) \(\left(T_{s}-T_{s a t}\right)^{1 / 2}\) (c) \(\left(T_{s}-T_{\text {sat }}\right)^{3 / 4}\) (d) \(\left(T_{s}-T_{\text {sat }}\right)\) (e) \(\left(T_{s}-T_{\text {sat }}\right)^{2 / 3}\)

What is the difference between film and dropwise condensation? Which is a more effective mechanism of heat transfer?

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?

A 1-mm-diameter nickel wire with electrical resistance of $0.129 \Omega / \mathrm{m}$ is submerged horizontally in water at atmospheric pressure. Determine the electrical current at which the wire would be in danger of burnout in nucleate boiling.

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