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

Steam is throttled from 7 MPa and \(500^{\circ} \mathrm{C}\) to a pressure of 1 MPa. Determine the decrease in exergy of the steam during this process. Assume the surroundings to be at \(25^{\circ} \mathrm{C} .\)

Short Answer

Expert verified
Question: Calculate the decrease in exergy of steam during a throttling process. The process starts with the steam at 7 MPa and \(500^{\circ} C\) and ends with the steam pressure at 1 MPa. The given surrounding temperature is \(25^{\circ} C\). Assume the steam table values of enthalpy, entropy, and specific volume for both initial and final states. Provide the step by step solution with appropriate formulae. Answer: The decrease in exergy during the throttling process can be calculated in several steps. 1. Identify the specific properties of steam at the initial state (7 MPa and \(500^{\circ} C\)) and at the final state (1 MPa) from the provided steam tables. The properties include enthalpy, entropy, and specific volume. 2. Compute the initial exergy (\(e_1\)) using the formula: \(e_1 = h_1 - T_0 s_1 - P_0 v_1\), where \(T_0 = 298.15K\) is the surrounding temperature and \(P_0 = 0.1 MPa\) is the atmospheric pressure. 3. Compute the final exergy (\(e_2\)) using the same formula: \(e_2 = h_2 - T_0 s_2 - P_0 v_2\). Note that \(h_2 = h_1\) due to the isenthalpic nature of the throttling process. 4. Calculate the decrease in exergy (\(\Delta e\)) by subtracting \(e_2\) from \(e_1\). Therefore, \(\Delta e = e_1 - e_2\).

Step by step solution

01

Identify the initial and final state of the steam in the steam tables

Using the initial and final conditions given, the steam is first at 7 MPa and \(500^{\circ} \mathrm{C}\). We can use these values in the steam tables to look for the corresponding initial enthalpy (\(h_1\)), initial entropy (\(s_1\)), and specific volume (\(v_1\)) at this condition. Similarly, we need to find the enthalpy (\(h_2\)), entropy (\(s_2\)), and specific volume (\(v_2\)) of the steam at the final pressure of 1 MPa. Since the throttling process is an isenthalpic process, we can assume that the enthalpy does not change (\(h_1 = h_2\)).
02

Calculate initial exergy of steam using the given parameters

Using the values of \(h_1\), \(s_1\), and \(v_1\) from the steam tables, we will compute the initial exergy using the following equation: \(e_1 = h_1 - T_0 s_1 - P_0 v_1\) where: \(e_1\) is the initial exergy, \(T_0\) is the surrounding temperature (which is given as \(25^{\circ} \mathrm{C}\), or in Kelvin, \(T_0 = 273.15 + 25 = 298.15\,\mathrm{K}\)), \(P_0\) is the atmospheric pressure (which can be assumed as 100 kPa or 0.1 MPa).
03

Calculate final exergy of steam using the given parameters

Similarly, using the values of \(h_2\), \(s_2\), and \(v_2\), we will compute the final exergy using the same equation as for the initial exergy: \(e_2 = h_2 - T_0 s_2 - P_0 v_2\) where: \(e_2\) is the final exergy. Note that \(h_2 = h_1\) since it is a throttling (isenthalpic) process.
04

Calculate decrease in exergy

The decrease in exergy during this throttling process is the difference between the initial and final exergy: Decrese in exergy (\(\Delta e\) ) = \(e_1 - e_2\) By obtaining the values of \(e_1\) and \(e_2\) from the previous steps, and finding the difference between these two values, the decrease in exergy of steam during the throttling process will be calculated.

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!

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

Can a system have a higher second-law efficiency than the first-law efficiency during a process? Give examples.

An insulated piston-cylinder device contains 0.8 L of saturated liquid water at a constant pressure of 120 kPa. An electric resistance heater inside the cylinder is turned on, and electrical work is done on the water in the amount of 1400 kJ. Assuming the surroundings to be at \(25^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\), determine \((a)\) the minimum work with which this process could be accomplished and ( \(b\) ) the exergy destroyed during this process.

Refrigerant- 134 a is converted from a saturated liquid to a saturated vapor in a closed system using a reversible constant pressure process by transferring heat from a heat reservoir at \(6^{\circ} \mathrm{C}\). From second-law point of view, is it more effective to do this phase change at \(100 \mathrm{kPa}\) or \(180 \mathrm{kPa} ?\) Take \(T_{0}=25^{\circ} \mathrm{C}\) and \(P_{0}=100 \mathrm{kPa}\).

Combustion gases enter a gas turbine at \(900^{\circ} \mathrm{C}\) \(800 \mathrm{kPa},\) and \(100 \mathrm{m} / \mathrm{s}\) and leave at \(650^{\circ} \mathrm{C}, 400 \mathrm{kPa},\) and \(220 \mathrm{m} / \mathrm{s} .\) Taking \(c_{p}=1.15 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\) and \(k=1.3\) for the combustion gases, determine \((a)\) the exergy of the combustion gases at the turbine inlet and ( \(b\) ) the work output of the turbine under reversible conditions. Assume the surroundings to be at \(25^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\). Can this turbine be adiabatic?

Cold water \(\left(c_{p}=4.18 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) leading to a shower enters a well-insulated, thin-walled, double-pipe, counterflow heat exchanger at \(15^{\circ} \mathrm{C}\) at a rate of \(0.25 \mathrm{kg} / \mathrm{s}\) and is heated to \(45^{\circ} \mathrm{C}\) by hot water \(\left(c_{p}=4.19 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) that enters at \(100^{\circ} \mathrm{C}\) at a rate of \(3 \mathrm{kg} / \mathrm{s}\). Determine \((a)\) the rate of heat transfer and \((b)\) the rate of exergy destruction in the heat exchanger. Take \(T_{0}=25^{\circ} \mathrm{C}\)

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