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Saturated water vapor is condensing on a \(0.5 \mathrm{~m}^{2}\) vertical flat plate in a continuous film with an average heat transfer coefficient of \(7 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\). The temperature of the water is \(80^{\circ} \mathrm{C}\left(h_{f g}=2309 \mathrm{~kJ} / \mathrm{kg}\right)\) and the temperature of the plate is \(60^{\circ} \mathrm{C}\). The rate at which condensate is being formed is (a) \(0.0303 \mathrm{~kg} / \mathrm{s}\) (b) \(0.07 \mathrm{~kg} / \mathrm{s}\) (c) \(0.15 \mathrm{~kg} / \mathrm{s}\) (d) \(0.24 \mathrm{~kg} / \mathrm{s}\) (e) \(0.28 \mathrm{~kg} / \mathrm{s}\)

Short Answer

Expert verified
Answer: (a) 0.0303 kg/s

Step by step solution

01

Determine the temperature difference between water and plate

Given, the temperature of the water \(T_w = 80^{\circ} \mathrm{C}\) and the temperature of the plate \(T_p = 60^{\circ} \mathrm{C}\). First, we will find the temperature difference between the water vapor and the plate: $$\Delta T = T_w - T_p = 80 - 60 = 20 \mathrm{~K}$$
02

Calculate the heat transfer rate

We will now find the heat transfer rate using the formula: $$Q = hA\Delta T$$ Where \(Q\) is the heat transfer rate, \(h\) is the heat transfer coefficient, \(A\) is the area, and \(\Delta T\) is the temperature difference. Given, \(h=7\ \mathrm{kW}/{\mathrm{m}^2\cdot\mathrm{K}}\), \(A=0.5\ \mathrm{m}^2\), and \(\Delta T = 20\ \mathrm{K}\): $$Q = 7 \times 0.5 \times 20 = 70\ \mathrm{kW}$$
03

Convert heat transfer rate to Watts

Now, we need to convert the heat transfer rate from kilowatts to watts: $$Q = 70\ \mathrm{kW} \times 1000\ \frac{\mathrm{W}}{\mathrm{kW}} = 70000\ \mathrm{W}$$
04

Calculate the rate of condensate formation

Finally, we will find the rate of condensate formation using the formula: $$\dot{m} = \frac{Q}{h_{fg}}$$ Where \(\dot{m}\) is the rate of condensate formation and \(h_{fg}\) is the latent heat of vaporization. Given, \(h_{fg} = 2309\ \mathrm{kJ/kg} = 2309000\ \frac{\mathrm{J}}{\mathrm{kg}}\): $$\dot{m} = \frac{70000}{2309000} = 0.0303\ \frac{\mathrm{kg}}{\mathrm{s}}$$ The rate at which condensate is being formed is (a) \(0.0303\ \mathrm{kg/s}\).

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Heat Transfer Coefficient
Understanding the heat transfer coefficient is crucial when studying how heat moves from one medium to another. It represents the amount of heat that flows per unit area, per unit time, for a temperature difference of one degree Celsius or Kelvin. In the condensation example, a high heat transfer coefficient means heat transfers efficiently from the water vapor to the cold plate, leading to rapid condensation.The coefficient depends on various factors, including the nature of the fluid, the flow regime (laminar or turbulent), and the properties of the surface where the heat exchange takes place. The heat transfer coefficient is measured in units of power per area per temperature difference, usually expressed as watts per square meter per Kelvin For students looking to deepen their understanding, remembering that this coefficient serves as a proportional constant in the basic heat transfer equation, can be beneficial. If two materials have the same temperature difference and area for heat transfer, but one has a higher heat transfer coefficient, more heat will flow through that material in a given time.
Temperature Difference
The concept of temperature difference lies at the heart of thermodynamics and heat transfer. It's the driving force behind the flow of heat energy; heat naturally flows from a hotter substance to a cooler one until thermal equilibrium is reached. The greater the temperature difference, the larger the potential for heat transfer.In the context of condensation on a plate, the temperature difference between the saturated water vapor and the cooler plate surface directly influences the rate of energy transfer. A larger difference results in a faster heat transfer rate, which in turn increases the condensate formation rate because more vapor can be cooled and condensed per unit time. Highlighting the real-world implications of temperature difference, such as in heating systems or refrigeration processes, where manipulating this difference can improve efficiency or cooling rates, can be quite enlightening for students. This practical application demonstrates the importance of understanding temperature difference in engineering and environmental control systems.
Latent Heat of Vaporization
Latent heat of vaporization is the amount of thermal energy required to change a substance from liquid to vapor phase without a temperature change. This is a form of hidden energy, as it doesn't raise the temperature, but is consumed to break the intermolecular bonds. It's crucial in phase change processes like boiling, condensation, and evaporation.In the case of the condensation on the plate, knowing the latent heat of vaporization is essential to calculate the mass of water that condenses per second. It takes a lot of energy to vaporize water; hence, a lot of energy is released when vapor condenses back into liquid. The latent heat value is usually quite substantial, indicating why cooling systems and power plants must manage phase changes very carefully.To put this in perspective, while resurfacing certain points may be repetitive, it is important for learners to recognize that the high value of water's latent heat of vaporization means that even small amounts of condensation release significant amounts of heat. Comprehending this concept is pivotal for various applications, such as designing HVAC systems, understanding weather patterns, or calculating energy requirements in phase-change materials.

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Most popular questions from this chapter

Saturated steam at \(30^{\circ} \mathrm{C}\) condenses on the outside of a 4-cm- outer-diameter, 2-m-long vertical tube. The temperature of the tube is maintained at \(20^{\circ} \mathrm{C}\) by the cooling water. Determine \((a)\) the rate of heat transfer from the steam to the cooling water, \((b)\) the rate of condensation of steam, and \((c)\) the approximate thickness of the liquid film at the bottom of the tube. 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?

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 in cylindrical shape with a heightto-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 \(2 \mathrm{~h}\) 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.

Water is boiled at sea level in a coffee maker equipped with a 20 -cm-long \(0.4\)-cm-diameter immersion-type electric heating element made of mechanically polished stainless steel. The coffee maker initially contains \(1 \mathrm{~L}\) of water at \(14^{\circ} \mathrm{C}\). Once boiling starts, it is observed that half of the water in the coffee maker evaporates in \(25 \mathrm{~min}\). Determine the power rating of the electric heating element immersed in water and the surface temperature of the heating element. Also determine how long it will take for this heater to raise the temperature of \(1 \mathrm{~L}\) of cold water from \(14^{\circ} \mathrm{C}\) to the boiling temperature.

How does film boiling differ from nucleate boiling? Is the boiling heat flux necessarily higher in the stable film boiling regime than it is in the nucleate boiling regime?

A long cylindrical stainless steel rod \(\left(c_{p}=\right.\) \(450 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, \rho=7900 \mathrm{~kg} / \mathrm{m}^{3}, \varepsilon=0.30\) ) with mechanically polished surface is being conveyed through a water bath to be quenched. The \(25-\mathrm{mm}\)-diameter stainless steel rod has a temperature of \(700^{\circ} \mathrm{C}\) as it enters the water bath. \(\mathrm{A}\) length of \(3 \mathrm{~m}\) of the rod is submerged in water as it is conveyed through the water bath during the quenching process. As the stainless steel rod enters the water bath, boiling would occur at \(1 \mathrm{~atm}\). In order to prevent thermal burn on people handling the rod, it must exit the water bath at a temperature below \(45^{\circ} \mathrm{C}\). Determine the speed of the rod being conveyed through the water bath so that it leaves the water bath without the risk of thermal burn hazard.

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