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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 $5 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}$. 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) \(0.022 \mathrm{~kg} / \mathrm{s}\) (b) \(0.048 \mathrm{~kg} / \mathrm{s}\) (c) \(0.077 \mathrm{~kg} / \mathrm{s}\) (d) \(0.16 \mathrm{~kg} / \mathrm{s}\) (e) \(0.32 \mathrm{~kg} / \mathrm{s}\)

Short Answer

Expert verified
(a) 0.022 kg/s (b) 0.045 kg/s (c) 0.067 kg/s (d) 0.090 kg/s Answer: (a) 0.022 kg/s

Step by step solution

01

Calculate the temperature difference

First, we have to find the temperature difference between the water and the plate, which is given as follows: $$ \Delta T = T_{water} - T_{plate} $$
02

Calculate the heat transfer rate

Now, we will calculate the heat transfer rate using the given average heat transfer coefficient (h), the temperature difference (ΔT), and the area (A): $$ Q = h \cdot A \cdot \Delta T $$
03

Calculate the mass flow rate of condensate

Next, we will find the mass flow rate (ṁ) of the condensate by dividing the heat transfer rate (Q) by the latent heat of vaporization (h_fg): $$ \dot{m} = \frac{Q}{h_{fg}} $$ Now, let's plug in the given values and solve:
04

Calculate the temperature difference

We are given: $$ T_{water} = 80^{\circ}C \\ T_{plate} = 60^{\circ}C $$ Using the temperature difference formula: $$ \Delta T = 80 - 60 = 20^{\circ}C $$
05

Calculate the heat transfer rate

We are given: $$ h = 5 \frac{kW}{m^2 K} \\ A = 0.5 m^2 \\ \Delta T = 20^{\circ}C $$ Using the heat transfer rate formula: $$ Q = (5 \frac{kW}{m^2 K}) \cdot (0.5 m^2) \cdot (20^{\circ}C) = 50 kW $$
06

Calculate the mass flow rate of condensate

We are given: $$ Q = 50 kW \\ h_{fg} = 2309 \frac{kJ}{kg} $$ Note that we need to convert kW to kJ/s: $$ 50 kW = 50 kJ / s $$ Using the mass flow rate formula: $$ \dot{m} = \frac{50 kJ/s}{2309 kJ/kg} \approx 0.0216 \frac{kg}{s} $$ The calculated mass flow rate is approximately equal to 0.022 kg/s, which corresponds to the answer (a).

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Most popular questions from this chapter

A 3 -mm-diameter cylindrical heater is used for boiling water at $100^{\circ} \mathrm{C}$. The heater surface is made of mechanically polished stainless steel with an emissivity of \(0.3\). Determine the boiling convection heat transfer coefficients at the maximum heat flux for \((a)\) nucleate boiling and \((b)\) film boiling. For film boiling, evaluate the properties of vapor at \(1150^{\circ} \mathrm{C}\).

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) \(2.06 \mathrm{~kg} / \mathrm{s}\)

A cylindrical rod is used for boiling water at \(1 \mathrm{~atm}\). The rod has a diameter of \(1 \mathrm{~cm}\), and its surface has an emissivity of \(0.3\). Determine the film boiling convection heat transfer coefficient at the burnout point. Evaluate the properties of vapor at \(1150^{\circ} \mathrm{C}\). Discuss whether \(1150^{\circ} \mathrm{C}\) is a reasonable film temperature for the vapor properties.

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?

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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