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Moist air at \(20^{\circ} \mathrm{C}, 1 \mathrm{~atm}, 43 \%\) relative humidity and a volumetric flow rate of \(900 \mathrm{~m}^{3} / \mathrm{h}\) enters a control volume at steady state and flows along a surface maintained at \(65^{\circ} \mathrm{C}\), through which heat transfer occurs. Liquid water at \(20^{\circ} \mathrm{C}\) is injected at a rate of \(5 \mathrm{~kg} / \mathrm{h}\) and evaporates into the flowing stream. For the control volume, \(\dot{W}_{\mathrm{cv}}=0\), and kinetic and potential energy effects are negligible. Moist air exits at \(32^{\circ} \mathrm{C}, 1 \mathrm{~atm}\). Determine (a) the rate of heat transfer, in \(\mathrm{kW}\). (b) the rate of entropy production, in \(\mathrm{kW} / \mathrm{K}\).

Short Answer

Expert verified
For part (a), the rate of heat transfer, \( \dot{Q}_{cv} \), is calculated using energy conservation principles and properties of moist air. For part (b), the entropy generation rate, \( \dot{S}_{gen} \), is found based on the entropy balance.

Step by step solution

01

List known values and assumptions

Identify and list all given values and assumptions for the problem: Initial conditions:-Temperature of moist air: \(20^{\circ} \text{C}\)-Pressure: \(1 \text{ atm}\)-Relative Humidity: 43%-Volumetric flow rate: \(900 \text{ m}^{3}/\text{h}\)Additional details:-Liquid water injected: \(5 \text{ kg}/\text{h}\)-Heat transfer surface temperature: \(65^{\circ} \text{C}\)-Moist air exit temperature: \(32^{\circ} \text{C}\)-Kinetic and potential energy effects are negligible.
02

Calculate the mass flow rate of dry air

Use the volumetric flow rate and the ideal gas law to determine the mass flow rate of dry air. The formula for the ideal gas law is: \[ PV = nRT \rightarrow V = \frac{nRT}{P} \]where:-\( P \) is pressure (1 atm)-\( V \) is volume (900 m³/h)-\( R \) is the specific gas constant for air (287 J/kg·K)-\( T \) is temperature in Kelvin (293 K)\[ n = \dot{m}_a \rightarrow \dot{m}_a = \frac{PV}{RT} \] convert units as necessary to find \( \dot{m}_a \approx 1.247.8 kg/h \)
03

Calculate the initial and final specific humidity

Use the relative humidity and saturation pressure to calculate the specific humidity: The saturation pressure at 20ºC: \( P_{sat,20ºC} = 2.34 \ kPa \) Relative Humidity (RH) = 0.43 Using the specific humidity formula: \[ \text{Specific Humidity} \left( \omega \right) = \frac{0.622 \cdot \text{RH} \cdot P_{sat}}{P - (RH \cdot P_{sat})} \]
04

Apply the Mass and Energy Balances

Use the conservation of mass and energy equations for the control volume: Mass balance: \[ \dot{m}_a \cdot \omega_1 + \dot{m}_{water} = \dot{m}_a \cdot \omega_2 \] Energy balance: \[ \dot{m}_a \cdot (h_{a2} - h_{a1}) + \dot{m}_{water}\cdot h_{fg,65ºC} = \dot{Q}_{cv} \] Solve for \( \dot{Q}_{cv} \)
05

Calculation the entropy production rate

The entropy balance for this control volume looks like: \[ \dot{S}_{gen} = \sum \dot{m} s_2 - \sum \dot{m} s_1 \] where: -\( s_2 \) is the specific entropy of the exiting moist air-\( s_1 \) is the specific entropy of the entering moist airPlug known values into these formulas and solve for \( \dot{Q}_{cv} \) and \( \dot{S}_{gen} \)

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Key Concepts

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

entropy production calculation
Entropy production is important in understanding the irreversibility in a thermodynamic process. For this control volume, the entropy balance is given by the formula:\[ \dot{S}_{gen} = \sum \dot{m} s_2 - \sum \dot{m} s_1 \]Here,- \( \dot{S}_{gen} \) is the rate of entropy production- \( s_2 \) and \( s_1 \) are the specific entropies of the moist air exiting and entering, respectivelyBy substituting the known values into this equation, we can determine the system's entropy production rate. This calculation reveals the amount of disorder or energy dispersion occurring within the control volume. Ensuring that students understand this concept is key to grasping the second law of thermodynamics.
specific humidity
Specific humidity is a measure of the water vapor present in the air and is essential in drying and air conditioning processes. Calculating specific humidity involves the relative humidity and the saturation pressure of water vapor.The formula for specific humidity (\( \omega \)) is:\[ \omega = \frac{0.622 \cdot \text{RH} \cdot P_{sat}}{P - (\text{RH} \cdot P_{sat})} \]By using the initial conditions:- Relative Humidity (RH): 43%- Saturation pressure at 20ºC: \( P_{sat,20ºC} = 2.34 \text{ kPa} \)- Atmospheric pressure (P): 1 atmWe can calculate the initial and final specific humidities. Understanding specific humidity and its role in thermodynamic calculations assists in determining the moisture content changes in air processing applications.
ideal gas law
The ideal gas law, represented by the equation \[ PV = nRT \], relates a gas's pressure, volume, temperature, and amount. Here, \( P \) is pressure, \( V \) is volume, \( n \) is the amount of substance, \( R \) is the gas constant, and \( T \) is temperature.In many thermodynamic problems, like the mass flow rate determination, the ideal gas law provides a foundation for connecting these properties. Whether converting volumes or calculating the effects of temperature changes, sound knowledge of this law is pivotal. For instance, we used this law to determine:\[ \dot{m}_a = \frac{PV}{RT} \]The idea is that under standard conditions, air behaves almost like an ideal gas, permitting these calculations.

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Most popular questions from this chapter

Atmospheric air having dry-bulb and wet-bulb temperatures of 33 and \(29^{\circ} \mathrm{C}\), respectively, enters a well-insulated chamber operating at steady state and mixes with air entering with dry-bulb and wet- bulb temperatures of 16 and \(12^{\circ} \mathrm{C}\), respectively. The volumetric flow rate of the lower temperature stream is three times that of the other stream. A single mixed stream exits. The pressure is constant throughout at 1 atm. Neglecting kinetic and potential energy effects, determine for the exiting stream (a) the relative humidity. (b) the temperature, in \({ }^{\circ} \mathrm{C}\).

A stream consisting of \(35 \mathrm{~m}^{3} / \mathrm{min}\) of moist air at \(14^{\circ} \mathrm{C}\), \(1 \mathrm{~atm}, 80 \%\) relative humidity mixes adiabatically with a stream consisting of \(80 \mathrm{~m}^{3} / \mathrm{min}\) of moist air at \(40^{\circ} \mathrm{C}, 1 \mathrm{~atm}\), \(40 \%\) relative humidity, giving a single mixed stream at \(1 \mathrm{~atm}\). Using the psychrometric chart together with the procedure of Prob. 12.58, determine the relative humidity and temperature, in \({ }^{\circ} \mathrm{C}\), of the exiting stream.

Figure P12.5D shows a system for supplying a space with \(2100 \mathrm{~m}^{3} / \mathrm{min}\) of conditioned air at a dry-bulb temperature of \(22^{\circ} \mathrm{C}\) and a relative humidity of \(60 \%\) when the outside air is at a dry-bulb temperature of \(35^{\circ} \mathrm{C}\) and a relative humidity of \(55 \%\). Dampers A and B can be set to give three alternative operating modes: (1) Both dampers closed (no use of recirculated air). (2) Damper A open and damper B closed. One-third of the conditioned air comes from outside air. (3) Both dampers open. One-third of the conditioned air comes from outside air. One- third of the recirculated air bypasses the dehumidifier via open damper B, and the rest flows through the damper A. Which of the three operating modes should be used? Discuss.

Air at \(77^{\circ} \mathrm{C}, 1\) bar, and a molar flow rate of \(0.1 \mathrm{kmol} / \mathrm{s}\) enters an insulated mixing chamber operating at steady state and mixes with water vapor entering at \(277^{\circ} \mathrm{C}, 1\) bar, and a molar flow rate of \(0.3 \mathrm{kmol} / \mathrm{s}\). The mixture exits at 1 bar. Kinetic and potential energy effects can be ignored. For the chamber, determine (a) the temperature of the exiting mixture, in \({ }^{\circ} \mathrm{C}\). (b) the rate of entropy production, in \(\mathrm{kW} / \mathrm{K}\).

Investigate the development of the heat index used to alert us to possible hot weather health dangers. Write a report including at least three references.

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