Chapter Seven: Entropy

Slides:



Advertisements
Similar presentations
Chapter 8 Exergy: A Measure of Work Potential Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 7th edition by Yunus.
Advertisements

Entropy Balance Equation
The Second Law of Thermodynamics
Chapter 4 Mass and Energy Analysis of Control Volumes (Open Systems)
Department of Mechanical Engineering ME 322 – Mechanical Engineering Thermodynamics Lecture 18 Introduction to 2 nd Law and Entropy.
Chapter 7 Entropy (Continue).
Advanced Thermodynamics Note 4 The Second Law of Thermodynamics
Exergy: A Measure of Work Potential Study Guide in PowerPoint
Chapter 7 Continued Entropy: A Measure of Disorder Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 5th edition.
Entropy: A Measure of Disorder. 2 Entropy and the Clausius Inequality The second law of thermodynamics leads to the definition of a new property called.
Thermodynamics Lecture Series Applied Sciences Education.
PTT 201/4 THERMODYNAMIC SEM 1 (2013/2014) CHAPTER 7: Entropy.
Chapter 7 ENTROPY Mehmet Kanoglu
PTT 201/4 THERMODYNAMIC SEM 1 (2012/2013). Objectives Apply the second law of thermodynamics to processes. Define a new property called entropy to quantify.
THERMODYNAMICS CH 15.
Calculating Entropy Change
Lecture slides by Mehmet Kanoglu
Chapter 5 The Second Law of Thermodynamics. Learning Outcomes ►Demonstrate understanding of key concepts related to the second law of thermodynamics,
The Laws of Thermodynamics
ERT 206 THERMODYNAMICS WAN KHAIRUNNISA WAN RAMLI
Entropy Rate Balance for Closed Systems
ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical Engineering University of Oklahoma.
The Second Law of Thermodynamics Chapter 6. The Second Law  The second law of thermodynamics states that processes occur in a certain direction, not.
Energy and the Environment Fall 2013 Instructor: Xiaodong Chu : Office Tel.:
AGUS HARYANTO 01 March  Examine the moving boundary work or P.dV work.  Identify the first law of thermodynamics for closed (fixed mass) systems.
Chapter 7 ENTROPY Dr. Kagan ERYURUK
6. ENTROPY. Objectives Apply the second law of thermodynamics to processes. Define a new property called entropy to quantify the second-law effects. Establish.
1 Second Law of Thermodynamics - Entropy. 2 Introduction The second low often leads to expressions that involve inequalities.
CHAPTER 6 Entropy. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. The Clausius Inequality: This inequality.
ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical Engineering University of Oklahoma.
Thermodynamics Thermodynamics is a branch of physics concerned with heat and temperature and their relation to energy and work.
Physics 101 Lecture 11. Thermal Physics Thermodynamics.
SUBJECT : Engineering Thermodynamics. UNIT : Entropy Prepared by NAMEENROLLMENT NO SUNILKUMAR PATEL UTSAVKUMAR PATEL VAIDIK PATEL
CH4 Energy Analysis of Closed System 1. Objectives Examine the moving boundary work or P dV work commonly encountered in reciprocating devices such as.
Chapter 8 Exergy: A Measure of Work Potential Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 7th edition by Yunus.
Chapter: 07 ENTROPY.
Chapter 8 Exergy: A Measure of Work Potential Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 8th edition by Yunus.
AHMEDABAD INSTITUTE OF TECHNOLOGY
G.K.BHARAD INSTITUTE OF ENGINEERING(059)
Chapter 7 Entropy.
Chapter 8 Exergy: A Measure of Work Potential Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 5th edition by Yunus.
Chapter 7 Entropy: A Measure of Disorder Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 8th edition by Yunus A.
Chapter 1 Concepts of Thermodynamics and Properties of Gases
An Engineering Approach
Chapter 7 Entropy: A Measure of Disorder
Thermodynamic.
Advanced Thermodynamics Exergy / Availability:
THERMOCHEMISTRY Thermodynamics The study of Heat and Work and State Functions To play the movies and simulations included, view the presentation in Slide.
Chapter 8 EXERGY: A MEASURE OF WORK POTENTIAL
Lecture 45 Entropy Clausius theorem Entropy as a state function
Thermodynamics Lecture Series
Thermodynamics: An Engineering Approach Yunus A. Cengel, Michael A
Chapter 6: Entropy What is Entropy?
Heat Engines Entropy The Second Law of Thermodynamics
An Engineering Approach
Mass and Energy Analysis of Control Volumes (Open Systems)
Fundamentals of Thermal-Fluid Sciences
Z.E. Z.E. Z.E. IE 211 INTRODUCTION TO ENGINEERING THERMODYNAMICS
Entropy Entropy is a measure of molecular disorder, or molecular
The Second Law of Thermodynamics
The Second Law of Thermodynamics
Chapter Seven: Entropy
Lecture slides adopted by William G. Tanner, Jr., PhD
Chapter 8 EXERGY: A MEASURE OF WORK POTENTIAL
Thermodynamics Lecture Series
Chapter 6 ENERGY ANALYSIS OF CLOSED SYSTEM
SECOND LAW OF THERMODYNAMICS
Chapter 6: Entropy What is Entropy?
Chapter 6: Entropy First law: Energy conservation concept.
Presentation transcript:

Chapter Seven: Entropy

WHAT IS ENTROPY Entropy is a measure of molecular disorder, or molecular randomness. As a system becomes more disordered, the positions of the molecules become less predictable and the entropy increases. The entropy of a substance is lowest in the solid phase and highest in the gas phase. Unlike energy, entropy is a nonconserved property, and there is no such thing as a conservation of entropy principle.

Derivation of Entropy from First and Second Laws Consider the following combined system consisting of a heat engine and a piston cylinder system First Law applied to the combined system (for example Carnot cycle)

The Carnot Cycle Idealized thermodynamic cycle consisting of four reversible processes (working fluid can be any substance): The four steps for a Carnot Heat Engine are: Reversible isothermal expansion (1-2, TH= constant) Reversible adiabatic expansion (2-3, Q = 0, THTL) Reversible isothermal compression (3-4, TL=constant) Reversible adiabatic compression (4-1, Q=0, TL TH) TL 1-2 2-3 3-4 4-1

Carnot Efficiency QR =Q12 = W12 = PdV = mRTHln(V2/V1) (1) Consider an ideal gas undergoing a Carnot cycle between two temperatures TH and TL. 1 to 2, isothermal expansion, DU12 = 0 QR =Q12 = W12 = PdV = mRTHln(V2/V1) (1) 2 to 3, adiabatic expansion, Q23 = 0 (TL/TH) = (V2/V3)k-1 (2) 3 to 4, isothermal compression, DU34 = 0 QL = Q34 = W34 = - mRTln(V4/V3) (3) 4 to 1, adiabatic compression, Q41 = 0 (TL/TH) = (V1/V4)k-1 (4) From (2) & (4): (V2/V3) = (V1/V4)  (V2/V1) = (V3/V4) Since ln(V2/V1) = - ln(V4/V3); substituting for ln(V4/V3) in (1)  (QL/QR )= (TL/TH) Hence: th = 1-(QL/QR)= 1-(TL/TH) Therefore: QL/QR =TL/TH Or

Derivation of Entropy from First and Second Laws Consider the following combined system consisting of a Carnot heat engine and a piston cylinder system First Law applied to the combined system For a Carnot Engine (reversible cycle) Substituting: 6

Derivation of Entropy from First and Second Laws Let the system undergo a cycle while the Carnot cycle undergoes one or more cycles. Integrate over entire cycle : The net work for one cycle is The integral must be evaluated at the system boundary The combined system (cycle) draws heat from a single reservoir while involving work WC. Based on Kelvin–Planck statement (no system can produce a net amount of work while operating in a cycle and exchanging heat with a single thermal energy reservoir) the combined system cannot produce net work output. Therefore, WC 0 This is the Clausius Inequality which is valid for all thermodynamic cycles, reversible or irreversible.

Derivation of Entropy from First and Second Laws For a reversible cycle Since the cyclic integral of (dQ/T) is 0, the quantity dQ/T is a state property, it does not depend on the path We call this new property entropy, S, For a process where the system goes from state 1 to 2 Specific entropy s= S/M=

A Special Case: Internally Reversible Isothermal Heat Transfer Processes Internally reversible process : is the process that has no irreversibilities that occur within the boundaries of the system during the process. During an internally reversible process, a system proceeds through a series of equilibrium states, and when the process is reversed, the system passes through exactly the same equilibrium states while returning to its initial state. Recall that isothermal heat transfer processes are internally reversible. Therefore, the entropy change of a system during an internally reversible isothermal heat transfer process can be determined by performing the integration in : where T0 is the constant absolute temperature of the system and Q is the heat transfer for the internally reversible process.

EXAMPLE : Entropy Change during an Isothermal Process A piston-cylinder device contains a liquid–vapor mixture of water at 300 K. During a constant-temperature process, 750 kJ of heat is transferred to the water. As a result, part of the liquid in the cylinder vaporizes. Determine the entropy change of the water during this process.

Solution The system undergoes an internally reversible, isothermal process, and thus its entropy change can be determined directly to be: Note that the entropy change of the system is positive, as expected, since heat transfer is to the system.

THE INCREASE OF ENTROPY PRINCIPLE From Clausius inequality: For complete cycle consisting of irreversible process from 1 to 2 and internally reversible process from 2 to 1 and: We conclude from these equations that the entropy change of a closed system during an irreversible process is greater than the integral of evaluated for that process.

THE INCREASE OF ENTROPY PRINCIPLE Remove inequality sign to get the entropy balance equation for a closed system: 13

Isolated system (adiabatic closed system) This is the Increase in Entropy Principle which simply states that “for an isolated system the entropy always increases or remains the same”. For isolated system (adiabatic closed system):

Remarks about Entropy Entropy is a nonconserved property. Processes can occur in a certain direction only, not in any direction. Entropy generation is a measure of the magnitudes of the irreversibilities The greater the extent of irreversibilities, the greater the entropy generation.

Entropy Change of a System Note that entropy is a property, and the value of a property does not change unless the state of the system changes. Therefore, the entropy change of a system is zero if the state of the system does not change during the process.

Third Law of Thermodynamics Entropy is the measure of molecular disorder or randomness. As a system becomes more disordered, the position of the molecules becomes less predictable and the entropy increases. Entropy is the lowest in solids because molecules are held in place and simply vibrate and highest in gases where the molecules are free to move in any direction. Third Law of Thermodynamics States that: “Entropy of a pure crystalline substance at absolute zero temperature (zero Kelvin) is zero since the state of each molecule is known”.

Isentropic Process A process that is both adiabatic and reversible is referred to as isentropic, and for a closed ystem:

Assume that the system is at steady state ( )

For ideal gas:

ENTROPY BALANCE The second law of thermodynamics states that entropy can be created but it cannot be destroyed. The entropy change of a system during a process is greater than the net entropy transfer by an amount equal to the entropy generated during the process within the system, and the increase of entropy principle for any system is expressed as:

Mechanisms of Entropy Transfer 1. Heat Transfer 2. Mass Flow Note that there is no entropy change due to work

Entropy Generation Irreversibilities such as friction, mixing, chemical reactions, heat transfer through a finite temperature difference, unrestrained expansion or compression always cause the entropy of a system to increase, and entropy generation is a measure of the entropy created by such effects during a process. For irreversible process: For a reversible process, the entropy generation is zero and thus the entropy change of a system is equal to the entropy transfer. For reversible process:

Change in Entropy and Its Rate

Open System (Control Volumes) A control volume involves mass flow across its boundaries, and its entropy change is a combination of entropy transfer accompanying heat and mass transfer and the entropy generation within the system boundaries.

Special Cases 1. Steady state process 2. Steady state process, Single-stream 3. Steady state process, Single-stream, Adiabatic

Closed Systems A closed system involves no mass flow across its boundaries, and its entropy change is simply the difference between the initial and final entropies of the system. The entropy change of a closed system is due to the entropy transfer accompanying heat transfer and the entropy generation within the system boundaries. 37

Steps for Solving Entropy Problems Sketch the process List data you may need to solve the problem and highlight what is known and what is unknown. Perform Mass Balance. Perform Energy Balance. Perform Entropy Balance. 38

EXAMPLE: Entropy Generation in a Mixing Chamber Water at 20 psia and 50°F enters a mixing chamber at a rate of 300 lbm/min where it is mixed steadily with steam entering at 20 psia and 240°F. The mixture leaves the chamber at 20 psia and 130°F, and heat is lost to the surrounding air at 70°F at a rate of 180 Btu/min. Neglecting the changes in kinetic and potential energies, determine the rate of entropy generation during this process.

We take the mixing chamber as the system We take the mixing chamber as the system. This is a control volume since mass crosses the system boundary during the process. We note that there are two inlets and one exit. Under the stated assumptions and observations, the mass and energy balances for this steady-flow system can be expressed in the rate form as follows:

Data =

Entropy Balance: The rate of entropy generation during this process can be determined by applying the rate form of the entropy balance on an extended system that includes the mixing chamber and its immediate surroundings so that the boundary temperature of the extended system is 70°F = 530 R:

End of Chapter Seven