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

Liquid water at \(50^{\circ} \mathrm{C}\) enters a forced draft cooling tower operating at steady state. Cooled water exits the tower with a mass flow rate of \(80 \mathrm{~kg} / \mathrm{min}\). No makeup water is provided. A fan located within the tower draws in atmospheric air at \(17^{\circ} \mathrm{C}\), \(0.098 \mathrm{MPa}, 60 \%\) relative humidity with a volumetric flow rate of \(110 \mathrm{~m}^{3} / \mathrm{min}\). Saturated air exits the tower at \(30^{\circ} \mathrm{C}, 0.098\) MPa. The power input to the fan is \(8 \mathrm{~kW}\). Ignoring kinetic and potential energy effects, determine (a) the mass flow rate of the liquid stream entering, in \(\mathrm{kg} / \mathrm{min}\). (b) the temperature of the cooled liquid stream exiting, in \({ }^{\circ} \mathrm{C}\).

Short Answer

Expert verified
Mass flow rate entering: 80 kg/min, Temperature exiting: Requires detailed energy balance.

Step by step solution

01

- Define the System and Assumptions

Identify the system boundaries. Assume steady state conditions, meaning the mass flow rate of liquid entering equals the mass flow rate of liquid exiting. Ignore kinetic and potential energy effects as stated.
02

- Calculate Mass Flow Rate of Air

Use the ideal gas law to determine the mass flow rate of the air entering the cooling tower. The ideal gas law is \[ PV = nRT \]. Rearrange to find the mass: \[ m = \frac{PV}{RT} \]. Given: Volumetric flow rate \(V = 110 \; m^3 / min\), Temperature \(T = 17^{\circ}C\) (add 273 to convert to Kelvin), Pressure \( P = 0.098\;MPa \), Gas Constant \( R = 0.287 \; kJ/kg \cdot K \).
03

- Determine Humidity

Calculate the specific volume of the air. Use the psychrometric chart or equations to find the mass flow rate of dry air and water vapor. Using the relative humidity (60\%) and air properties at \(17^{\circ}C, 0.098\;MPa\).
04

- Energy Balance for Cooling Tower

Set up an energy balance for the cooling tower.Take into account the energy change in air and water as well as the power input from the fan. The equation is given by: \[ \dot{m}_\text{air} (h_\text{in} - h_\text{out}) + \dot{m}_{water\; entering} h_{water\; in} = \dot{m}_{water \; exiting} h_{water\; out} + Power_{input} \].
05

- Solve for Mass Flow Rate of Liquid Entering

Reorganize the energy balance equation from step 4 to solve for the unknown mass flow rate of the liquid stream entering: \[ \dot{m}_{water \; entering} = \frac{\dot{m}_{water \; exiting} h_{water\; out} + P_{input} - \dot{m}_\text{air} (h_\text{in} - h_\text{out})}{h_{water\; in}} \]. Insert known values to find the mass flow rate of liquid water entering.
06

- Solve for Temperature of Cooled Liquid Stream Exiting

Use the mass flow rate found in step 5 and set up a sensible heat transfer equation to solve for temperature of cooled liquid stream exiting\textcolor{red}{}: \[ h_{water \; out}= c_p \cdot (T_{water \; exit} - T_{water \; enter}) \]. With appropriate substitutions, solve for \( T_{water \; exit} \).

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!

Key Concepts

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

mass flow rate calculation
One of the key concepts in this problem is the calculation of the mass flow rate. The mass flow rate measures how much mass flows through a cross-section of a pipe per unit of time. It is crucial for determining how much water needs to be cooled and how much air must be processed. Mass flow rate is often calculated using the equation: \[\frac{\text{mass}}{\text{time}} = \rho \times \text{volumetric flow rate} \] where \( \rho \) represents the density of the fluid. Using the ideal gas law and given properties of the air, we can calculate the mass flow rate of dry air and water vapor needed in the cooling process. Knowing these values allows us to set up the energy balance equations correctly and solve the problem accurately. Proper understanding and calculation of mass flow rate is crucial for optimizing the efficiency of the cooling tower.
ideal gas law application
The ideal gas law, represented by the equation \[ PV = nRT \], is a fundamental concept applied in this problem to determine the mass flow rate of air entering the cooling tower. Here, \( P \) is the pressure, \( V \) is the volume, \( n \) is the number of moles, \( R \) is the gas constant, and \( T \) is the temperature. By arranging the equation as \[ m = \frac{PV}{RT} \], we can solve for the mass of air. To apply this, convert the given temperature from Celsius to Kelvin, and use the provided volumetric flow rate. Considering these calculations helps us understand how air properties affect the cooling tower's operation. This step not only emphasizes the importance of the ideal gas law in real-world engineering applications but also showcases its utility in calculating mass under varying conditions.
energy balance equation
Setting up an energy balance is essential for understanding the heat exchange in the cooling tower. The energy balance equation considers the energy inputs and outputs to ensure energy conservation. For this problem, we employ the equation: \[\begin{aligned} \dot{m}_\text{air} (h_\text{in} - h_\text{out}) + \ \ \dot{m}_{water\; entering} h_{water\; in} = \ \ \ \ \dot{m}_{water \; exiting} h_{water\; out} + Power_{input} \end{aligned} \] Here, \( h \) represents the specific enthalpy. First, determine the specific enthalpy values for each part of the air and water streams. With the enthalpy and mass flow rates known, we can account for the energy added by the fan. This helps identify the unknown mass flow rate of the liquid stream entering the cooling tower. Energy balance ensures both mass and energy conservation, critical for system stability and performance.
relative humidity in air
Relative humidity is the ratio of the current mass of water vapor in the air to the maximum possible mass of water vapor the air can hold at a given temperature. It is crucial in the operation of the cooling tower, as it dictates how much water can evaporate into the air stream. In our problem, air with 60% relative humidity enters the tower. This affects the mass flow rate of dry air and water vapor that we need to calculate using psychrometric charts or related equations. The accurate determination of relative humidity helps in calculating the specific volume and other properties needed for energy balance calculations. Thus, understanding and calculating relative humidity ensures that the system's design and operation can efficiently remove heat from the liquid stream.
psychrometric chart usage
A psychrometric chart is a powerful tool for analyzing the properties of moist air. It visually represents various parameters such as dry bulb temperature, wet bulb temperature, relative humidity, and specific volume. For our cooling tower problem, the psychrometric chart helps us find properties like the specific volume of air and the enthalpy of dry air and water vapor. Using the chart, we can determine the state of the air entering and leaving the cooling tower. This information is essential for setting up the energy balance equations. Understanding how to read and use a psychrometric chart aids in solving complex thermodynamic problems and optimizing HVAC systems and other applications involving air-water mixtures.

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

A device is being designed to separate into components a natural gas consisting of \(\mathrm{CH}_{4}\) and \(\mathrm{C}_{2} \mathrm{H}_{6}\) in which the mole fraction of \(\mathrm{C}_{2} \mathrm{H}_{6}\), denoted by \(y\), may vary from \(0.05\) to \(0.50\). The device will receive natural gas at \(20^{\circ} \mathrm{C}, 1 \mathrm{~atm}\) with a volumetric flow rate of \(100 \mathrm{~m}^{3} / \mathrm{s}\). Separate streams of \(\mathrm{CH}_{4}\) and \(\mathrm{C}_{2} \mathrm{H}_{6}\) will exit, each at \(20^{\circ} \mathrm{C}, 1 \mathrm{~atm}\). Heat transfer between the device and its surroundings occurs at \(20^{\circ} \mathrm{C}\). Ignoring kinetic and potential energy effects, plot versus \(y\) the minimum theoretical work input required at steady state, in \(\mathrm{kW}\).

At steady state, moist air is to be supplied to a classroom at a specified volumetric flow rate and temperature \(T\). Air is removed from the classroom in a separate stream at a temperature of \(27^{\circ} \mathrm{C}\) and \(50 \%\) relative humidity. Moisture is added to the air in the room from the occupants at a rate of \(4.5 \mathrm{~kg} / \mathrm{h}\). The moisturc can be regardcd as saturated vapor at \(33^{\circ} \mathrm{C}\). Hcat transfer into the occupied space from all sources is estimated to occur at a rate of \(34,000 \mathrm{~kJ} / \mathrm{h}\). The pressure remains uniform at \(1 \mathrm{~atm}\). (a) For a supply air volumetric flow rate of \(40 \mathrm{~m}^{3} / \mathrm{min}\), determine the supply air temperature \(T\), in \({ }^{\circ} \mathrm{C}\), and the relative humidity. (b) Plot the supply air temperature, in \({ }^{\circ} \mathrm{C}\), and relative humidity, each versus the supply air volumetric flow rate ranging from 35 to \(90 \mathrm{~m}^{3} / \mathrm{min}\).

Helium at \(400 \mathrm{~K}, 1\) bar enters an insulated mixing chamber operating at steady state, where it mixes with argon entering at \(300 \mathrm{~K}, 1\) bar. The mixture exits at a pressure of \(1 \mathrm{bar}\). If the argon mass flow rate is \(x\) times that of helium, plot versus \(x\) (a) the exit temperature, in \(\mathrm{K}\). (b) the rate of exergy destruction within the chamber, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of helium entering. Kinetic and potential energy effects can be ignored. Let \(T_{0}=\) \(300 \mathrm{~K}\).

On entering a dwelling maintained at \(20^{\circ} \mathrm{C}\) from the outdoors where the temperature is \(10^{\circ} \mathrm{C}\), a person's eye-glasses are observed not to become fogged. A humidity gauge indicates that the relative humidity in the dwelling is \(55 \%\). Can this reading be correct? Provide supporting calculations.

Natural gas at \(23^{\circ} \mathrm{C}, 1\) bar enters a furnace with the following molar analysis: \(40 \%\) propane \(\left(\mathrm{C}_{3} \mathrm{H}_{8}\right), 40 \%\) ethane \(\left(\mathrm{C}_{2} \mathrm{H}_{6}\right), 20 \%\) methane \(\left(\mathrm{CH}_{4}\right)\). Determine (a) the analysis in terms of mass fractions. (b) the partial pressure of each component, in bar. (c) the mass flow rate, in \(\mathrm{kg} / \mathrm{s}\), for a volumetric flow rate of \(20 \mathrm{~m}^{3} / \mathrm{s}\).

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