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

Air enters a nozzle steadily at \(200 \mathrm{kPa}\) and \(65^{\circ} \mathrm{C}\) with a velocity of \(35 \mathrm{m} / \mathrm{s}\) and exits at \(95 \mathrm{kPa}\) and \(240 \mathrm{m} / \mathrm{s}\). The heat loss from the nozzle to the surrounding medium at \(17^{\circ} \mathrm{C}\) is estimated to be \(3 \mathrm{kJ} / \mathrm{kg}\). Determine \((a)\) the exit temperature and ( \(b\) ) the exergy destroyed during this process. Answers: (a) \(34.0^{\circ} \mathrm{C}\) \((b) 36.9 \mathrm{kJ} / \mathrm{kg}\)

Short Answer

Expert verified
Additionally, there are heat losses from the nozzle to the surrounding medium of 3 kJ/kg.

Step by step solution

01

Calculate initial total enthalpy

To find the initial total enthalpy, we need to determine the specific enthalpy and specific kinetic energy at the entrance. Given the initial temperature and pressure, we can find the specific enthalpy from air properties table. Then, we can calculate the specific kinetic energy using the formula: $$ KE = \frac{1}{2} \cdot v_1^2 $$ Where \(v_1\) is the initial velocity. Finally, the initial total enthalpy, \(h_1+\frac{1}{2}v_1^2\), can be obtained by adding the specific enthalpy and specific kinetic energy.
02

Apply the steady-flow energy equation

The steady-flow energy equation for a nozzle can be expressed as: $$ h_1 + \frac{1}{2}v_1^2 + Q = h_2 + \frac{1}{2}v_2^2 $$ Where subscript 2 refers to the final state, and \(Q\) is the heat loss from the nozzle to the surrounding medium, given as \(-3 \ \text{kJ/kg}\). Rearrange the equation in terms of the exit specific enthalpy, \(h_2\): $$ h_2 = h_1 + \frac{1}{2}v_1^2 - \frac{1}{2}v_2^2 - Q $$ After calculating \(h_1 + \frac{1}{2}v_1^2\), substitute the values to find \(h_2\).
03

Determine the exit temperature

With the obtained value of \(h_2\), we can now use the air property table to find the exit temperature (\(T_2\)), corresponding to the final specific enthalpy and pressure.
04

Calculate initial and final exergies

The exergy at any state can be calculated using the following formula: $$ E = (h - h_0) - T_0 (s - s_0) + \frac{1}{2}v^2 $$ Where subscript 0 refers to the dead state (ambient) conditions. Calculate the exergies at initial and final states, \(E_1\) and \(E_2\), using the given data and air property table to find \(h_0\), \(s_0\), \(h\), and \(s\).
05

Calculate exergy destroyed

The exergy destroyed during the process, denoted as \(E_D\), can be found using the exergy balance equation, which states that the difference between the initial and final exergies equals the exergy destroyed: $$ E_D = E_1 - E_2 $$ Substitute the previously calculated values for \(E_1\) and \(E_2\) to find the exergy destroyed during the process.

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.

Steady-Flow Energy Equation
Picture a nozzle as a highway for air particles, where the rules of the road are governed by the principles of thermodynamics. One such rule is the steady-flow energy equation, a vital tool used in analyzing devices like nozzles, turbines, and compressors that have constant flow rates of fluid through them.

In the context of our nozzle problem, this equation dictates that the sum of a particle's specific enthalpy and kinetic energy at the entrance equals that at the exit, minus any heat lost to the surroundings. This is represented mathematically as:
\[h_1 + \frac{1}{2}v_1^2 + Q = h_2 + \frac{1}{2}v_2^2\]where \(h\) refers to specific enthalpy, \(v\) to velocity of the fluid, and \(Q\) to heat transfer.

Applying the Steady-Flow to Nozzles

In nozzles, air or any fluid is accelerated due to a decrease in area, turning pressure into kinetic energy. This process is adiabatic, meaning ideally, no heat is transferred. However, in reality, some heat loss occurs, and the equation above accounts for it, ensuring that the conservation of energy principle holds true throughout the process. It's this fundamental equation that aids in unraveling mysteries hidden within nozzles—including exit temperatures and velocities.
Specific Enthalpy
Delving deeper into our thermodynamic journey, we arrive at a concept crucial for understanding the energy changes in fluids: specific enthalpy. Specific enthalpy, \(h\), signifies the total energy content per unit mass of a fluid, amalgamating internal energy with the flow work done by the fluid.

This concept helps us quantify the energy changes as the fluid moves through the nozzle. In essence, it can be seen as the 'energy passport' for each fluid particle, providing a record of its energetic journey.

Energy Passport in the Context of Nozzles

Within the realms of a nozzle, the specific enthalpy accounts for both the intrinsic energy within the particles (relating to temperature) and the work done to push them through (owing to pressure). By consulting tables and using the temperature and pressure at the initial state, one can find the 'entry stamp' in this energy passport. As the fluid flows and transforms within the nozzle, its new 'departure stamp'—the exit specific enthalpy—is determined by the energy equation, which reflects the fluid's latest thermodynamic state.
Exergy Destruction
Thermodynamics isn't just about energy; it's also about quality—and that's where exergy comes into play. Exergy destruction is a measure of the potential work irreversibly lost due to inefficiencies within a system, and it's caused by factors like friction, mixing, chemical reactions, and heat transfer with the surroundings.

In our nozzle scenario, exergy destruction provides insight into the performance of the nozzle by quantifying how much useful energy is being squandered.

Understanding Exergy in a Nozzle

To calculate the exergy at a certain state, we use the formula:
\[E = (h - h_0) - T_0 (s - s_0) + \frac{1}{2}v^2\]which accounts for the specific enthalpy \(h\), ambient enthalpy \(h_0\), temperature \(T\), entropy \(s\), ambient entropy \(s_0\), and velocity \(v\). Exergy destruction therefore becomes a crucial indicator of energy efficiency. Specifically, it helps pinpoint where and how improvements can be made in the nozzle design to minimize wasted potential and maximize its thrust-producing capabilities.

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

Two constant-pressure devices, each filled with \(30 \mathrm{kg}\) of air, have temperatures of \(900 \mathrm{K}\) and \(300 \mathrm{K}\). A heat engine placed between the two devices extracts heat from the high-temperature device, produces work, and rejects heat to the low-temperature device. Determine the maximum work that can be produced by the heat engine and the final temperatures of the devices. Assume constant specific heats at room temperature.

Saturated steam is generated in a boiler by converting a saturated liquid to a saturated vapor at 200 psia. This is done by transferring heat from the combustion gases, which are at \(500^{\circ} \mathrm{F}\), to the water in the boiler tubes. Calculate the wasted work potential associated with this heat transfer process. How does increasing the temperature of the combustion gases affect the work potential of steam stream? Take \(T_{0}=\) \(80^{\circ} \mathrm{F}\) and \(P_{0}=14.7\) psia.

A \(12-\mathrm{ft}^{3}\) rigid tank contains refrigerant- \(134 \mathrm{a}\) at 30 psia and 55 percent quality. Heat is transferred now to the refrigerant from a source at \(120^{\circ} \mathrm{F}\) until the pressure rises to 50 psia. Assuming the surroundings to be at \(75^{\circ} \mathrm{F}\), determine (a) the amount of heat transfer between the source and the refrigerant and ( \(b\) ) the exergy destroyed during this process.

Liquid water enters an adiabatic piping system at \(15^{\circ} \mathrm{C}\) at a rate of \(3 \mathrm{kg} / \mathrm{s}\). It is observed that the water temperature rises by \(0.3^{\circ} \mathrm{C}\) in the pipe due to friction. If the environment temperature is also \(15^{\circ} \mathrm{C}\), the rate of exergy destruction in the pipe is \((a) 3.8 \mathrm{kW}\) (b) \(24 \mathrm{kW}\) \((c) 72 \mathrm{kW}\) \((d) 98 \mathrm{kW}\) \((e) 124 \mathrm{kW}\)

\(8-74 \quad\) A \(0.6-m^{3}\) rigid tank is filled with saturated liquid water at \(170^{\circ} \mathrm{C}\). A valve at the bottom of the tank is now opened, and one-half of the total mass is withdrawn from the tank in liquid form. Heat is transferred to water from a source of \(210^{\circ} \mathrm{C}\) so that the temperature in the tank remains constant. Determine \((a)\) the amount of heat transfer and \((b)\) the reversible work and exergy destruction for this process. Assume the surroundings to be at \(25^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\).

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