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

Methane gas \(\left(\mathrm{CH}_{4}\right)\) at \(280 \mathrm{~K}, 1\) bar enters a compressor operating at steady state and exits at \(380 \mathrm{~K}, 3.5\) bar. Ignoring heat transfer with the surroundings and employing the ideal gas model with \(\bar{c}_{p}(T)\) from Table A-21, determine the rate of entropy production within the compressor, in \(\mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\).

Short Answer

Expert verified
The rate of entropy production within the compressor is equal to the total entropy change, \(\Delta s\).

Step by step solution

01

Identify Given Data

Extract and list the given parameters from the problem statement:- Initial temperature, \(T_1 = 280 \mathrm{K}\)- Final temperature, \(T_2 = 380 \mathrm{K}\)- Initial pressure, \(P_1 = 1 \mathrm{bar}\)- Final pressure, \(P_2 = 3.5 \mathrm{bar}\)
02

Use Ideal Gas Model

Since the ideal gas model is assumed, start by identifying the specific heat capacity of methane, \(\mathrm{CH}_4\), from Table A-21: \(\bar{c}_p(T)\). For differentiation, consider the general form \(\bar{c}_p = a + bT + cT^2 + dT^3\).
03

Calculate Change in Entropy

Use the formula for entropy change for an ideal gas: \[\Delta s = \int_{T_1}^{T_2} \frac{\bar{c}_p(T)}{T} dT - R \ln\left( \frac{P_2}{P_1} \right) \]Here, \(R\) is the specific gas constant for methane (approximately \(0.518 \mathrm{kJ/kg \cdot K}\)).
04

Perform Integration for \(\Delta s = \int_{T_1}^{T_2} \frac{\bar{c}_p(T)}{T} dT\)

Integrate to find the change in entropy due to temperature difference: \[\Delta s_T = \int_{280}^{380} \frac{a + bT + cT^2 + dT^3}{T} dT \]This will yield: \[\Delta s_T = a\ln\left( \frac{T_2}{T_1} \right) + b(T_2 - T_1) + \frac{c}{2}(T_2^2 - T_1^2) + \frac{d}{3}(T_2^3 - T_1^3) \]
05

Calculate Pressure Entropy Term

Determine the change in entropy due to pressure change: \[\Delta s_P = -R \ln\left( \frac{P_2}{P_1} \right) \]With the given pressures: \[\Delta s_P = -0.518 \ln\left( \frac{3.5}{1} \right) \]
06

Calculate Total Entropy Change

Combine both entropy changes: \[\Delta s = \Delta s_T + \Delta s_P \]Numerically evaluate both terms to get \(\Delta s\).
07

Rate of Entropy Production

Since no heat is transferred to the surroundings: \[\sigma = \left( \frac{dS}{dt} \right)_{sys} = \Delta s \]Thus, the rate of entropy production within the compressor is equal to \(\Delta s\).

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.

Ideal Gas Model
The ideal gas model is a simple way to describe the behavior of gases under various conditions. It assumes that gas molecules occupy no volume and that they do not interact with one another, making calculations straightforward. This model is especially useful under standard temperature and pressure conditions. Methane gas (\text{CH}_4), like many other gases, can often be approximated as an ideal gas. This significantly simplifies our calculations by allowing us to use ideal gas laws and formulae. The behavior of an ideal gas is defined by the equation:\( PV = nRT \)where: P is the pressure, V is the volume, n is the number of moles, R is the gas constant, and T is the temperature. This relation shows how gas properties change with pressure, volume, and temperature and is the backbone of the calculations for processes such as compression or expansion of gases.
Specific Heat Capacity
Specific heat capacity is the amount of heat required to change the temperature of a unit mass of a substance by one degree. For gases, we often deal with specific heat at constant pressure, denoted as \( c_p \). The specific heat capacity of a gas can depend on temperature and is typically represented as a polynomial: \( \bar{c}_p = a + bT + cT^2 + dT^3 \). These coefficients (a, b, c, and d) are specific to each gas and are often found in tables, such as Table A-21 in thermodynamics textbooks.

• For methane (\text{CH}_4), the specific heat capacity formula helps us calculate how much entropy changes as the temperature of the gas changes. We integrate \( \frac{\bar{c}_p(T)}{T} \) between two temperatures (T1 and T2) to find the change in entropy due to temperature: \( \Delta s_T = \int_{280}^{380} \frac{a + bT + cT^2 + dT^3}{T} dT \).

This integration accounts for the varying heat capacity with temperature, making it more accurate for real-world scenarios.
Entropy Change
Entropy change is a measure of how the disorder or randomness of a system changes. For an ideal gas undergoing a process from one state to another, the entropy change can be calculated using the formula: \( \Delta s = \int_{T_1}^{T_2} \frac{\bar{c}_p(T)}{T} dT - R \ln\left( \frac{P_2}{P_1} \right) \), combining changes due to temperature (\( \Delta s_T \)) and changes due to pressure (\(\Delta s_P \)).

• For temperature changes: This part uses specific heat capacity values integrated over the temperature range.• For pressure changes: This involves the specific gas constant R of methane and the natural logarithm of the pressure ratio.

Understanding these individual components is crucial to grasp how entropy is produced or reduced during processes like compression. In this exercise, entropy production in the compressor is calculated by summing the entropy changes due to both temperature and pressure modifications. The total change in entropy tells us how much more 'disordered' the system becomes through the process.

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

Steam at \(0.7 \mathrm{MPa}, 355^{\circ} \mathrm{C}\) enters an open feedwater heater operating at steady state. A separate stream of liquid water enters at \(0.7 \mathrm{MPa}, 35^{\circ} \mathrm{C}\). A single mixed stream exits as saturated liquid at pressure \(p\). Heat transfer with the surroundings and kinetic and potential energy effects can be ignored. (a) If \(p=0.7 \mathrm{MPa}\), determine the ratio of the mass flow rates of the incoming streams and the rate at which entropy is produced within the feedwater heater, in \(\mathrm{kJ} / \mathrm{K}\) per \(\mathrm{kg}\) of liquid exiting. (b) Plot the quantities of part (a), each versus pressure \(p\) ranging from \(0.6\) to \(0.7 \mathrm{MPa}\).

At steady state, a device receives a stream of saturated water vapor at \(210^{\circ} \mathrm{C}\) and discharges a condensate stream at \(20^{\circ} \mathrm{C}, 0.1 \mathrm{MPa}\) while delivering energy by heat transfer at \(300^{\circ} \mathrm{C}\). The only other energy transfer involves heat transfer at \(20^{\circ} \mathrm{C}\) to the surroundings. Kinetic and potential energy changes are negligible. What is the maximum theoretical amount of energy, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of steam entering, that could be delivered at \(300^{\circ} \mathrm{C} ?\)

Answer the following true or false. If false, explain why. A process that violates the second law of thermodynamics violates the first law of thermodynamics. (b) When a net amount of work is done on a closed system undergoing an internally reversible process, a net heat transfer of energy from the system also occurs. (c) One corollary of the second law of thermodynamics states that the change in entropy of a closed system must be greater than zero or equal to zero. (d) A closed system can experience an increase in entropy only when irreversibilities are present within the system during the process. (e) Entropy is produced in every internally reversible process of a closed system. (f) In an adiabatic and internally reversible process of a closed system, the entropy remains constant. (g) The energy of an isolated system must remain constant, but the entropy can only decrease.

Methane gas \(\left(\mathrm{CH}_{4}\right)\) enters a compressor at \(298 \mathrm{~K}, 1\) bar and exits at 2 bar and temperature \(T\). Employing the ideal gas model, determine \(T\), in \(\mathrm{K}\), if there is no change in specific entropy from inlet to exit.

A system undergoes a thermodynamic power cycle while receiving energy by heat transfer from an incompressible body of mass \(m\) and specific heat \(c\) initially at temperature \(T_{\mathrm{H}}\). The system undergoing the cycle discharges energy by heat transfer to another incompressible body of mass \(m\) and specific heat \(c\) initially at a lower temperature \(T_{\mathrm{C}}\). Work is developed by the cycle until the temperature of each of the two bodies is the same, \(T^{\prime}\). (a) Develop an expression for the minimum theoretical final temperature, \(T^{\prime}\), in terms of \(m, c, T_{\mathrm{H}}\), and \(T_{\mathrm{C}}\), as required. (b) Develop an expression for the maximum theoretical amount of work that can be developed, \(W_{\max }\), in terms of \(m, c, T_{\mathrm{H}}\), and \(T_{\mathrm{C}}\), as required. (c) What is the minimum theoretical work input that would be required by a refrigeration cycle to restore the two bodies from temperature \(T^{\prime}\) to their respective initial temperatures, \(T_{\mathrm{H}}\) and \(T_{\mathrm{C}} ?\)

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