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Thermodynamics : an engineering approach
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Mô tả chi tiết
c w l e
Acceleration, m/s^
Specific Helnưioltz function, u - Ts, kJ/kg
Area,
Hebnholtz function, u - TS,k3
Air-fuel ratio
Speed of sound, m/s
Specific heat, kJ/kg ■ K
Constant pressure specific heat, kJ/kg • K
Constant volume specific heat, kJ/kg • K
Coefficient of performance
Coefficient of performance of a heat pump
Coefficient of performance of a refrigerator
Diameter, m
Specific total energy, kj/kg
Total energy, kJ
Energy efficiency rating
Force, N
Fuel-air ratio
Gravitational acceleration, m/s^
Specific Gibbs function, h - Ts, kJ/kg
Total Gibbs function, H — TS, kj
Convection heat transfer coefficient,
W/m2 • °c
Specific enthalpy, u + P\y, kj/kg
Total enthalpy, u + PV, kĩ
Enửialpy of combustion, kJ/kmol fuel
Enthalpy of formation, kJ/kmol
Enthalpy of reaction, kJ/kmol
Higher heating value, kj/kg fuel
Specific iưeversibility, kj/kg
Electric current, A
Total irreversibility, kJ
Specific heat ratio, C^/Cy
Spring constant
Thermal conductivity
Equilibrium constant
Specific kinetic energy, V-12, kJ/kg
Total kinetic energy, mV-/2, kJ
Lower heating value, kJ/kg fuel
Mass, kg
Mass flow rate, kg/s
Molar mass, kg/kmol
M a ch n u m b e r
MEP
m f
n
N
p
Pn
p'
^0
pe
PE
9
Q
Q
Ql
r
R
K
s
s
■^gen
SG
t
T
T
r
db
‘ w b
u
u
Mean effective pressure, kPa
Mass fraction
Polytropic exponent
Number of moles, kmol
Pressure, kPa
Critical pressure, kPa
Partial pressure, kPa
Mixture pressure, kPa
Relative pressure
Reduced pressure
Vapor pressure, kPa
Suưoundings pressure, kPa
Specific potential energy, gz, kj/kg
Total potential energy, mgz, kj
Heat ữansíer per unit mass, kj/kg
Total heat transfer, kj
Heat transfer rate, kw
Heat transfer with high-temperature body, kj
Heat transfer with low-temperature body, kJ
Compression ratio
Gas constant, kJ/kg • K
Cutoff ratio
Pressure ratio
Universal gas constant, kj/kmol • K
Specific entropy, kJ/kg • K
Total enttopy, kJ/K
Specific entropy generation, kJ/kg • K
Total entropy generation, kJ/K
Specific weight or relative density
Time, s
Temperature, °c or K
Torque, N • m
Critical temperature, K
Dry-bulb temperature, °c
Dew-point temperature, °c
Bulk fluid temperature, °c
Temperature of high-temperature body, K
Temperature of low-temperature body, K
Reduced temperature
Wet-bulb temperature, °c
Suưoundings temperature, °c or K
Specific internal energy, kJ/kg
Total internal energy, kJ
ỵ
\J
V
V
V .. avg
w
w
w
c
X
X
X
^ d e st
x Z
y
z
z
dest
Specific volume, m^/kg
Critical specific volume, m^/kg
Relative specific volume
Pseudoreduced specific volume
Total volume,
Volume flow rate, m^/s
Voltage, V
Velocity, m/s
Average velocity
Work per unit mass, kJ/kg
Total work, kJ
Power, kW
Work input, kJ
Work output, kJ
Reversible work, kJ
Quality
Specific exergy, kJ/kg
Total exergy, kJ
Specific exergy destruction, kj/kg
Total exergy destruction, kJ
Rate of total exergy destruction, kW
Mole fraction
Elevation, m
Compressibility factor
Enthalpy departure factor
Entropy departure factor
Greek Letters
a Absorptivity
a Isothermal compressibility, 1/kPa
Ị3 Volume expansivity, 1/K
A Finite change in quantity
£ Emissivity; effectiveness
Tjd, Thermal efficiency
Tjjj Second-law efficiency
6 Total energy of a flowing fluid, kJ/kg
ụ.jj Joule-Thomson coefficient, K/kPa
ụ. Chemical potential, kJ/kg
V Stoichiometric coefficient
p Density, kg/m^
Ơ Stefan-Boltzmann constant
ơ„ Normal stress, N/m^
Surface tension, N/m
Ộ Relative humidity
Ộ Specific closed system exergy, kJ/kg
$ Total closed system exergy, ũ
lỊ/ Stream exergy, kJ/kg
Ũ) Specific or absolute humidity,
kg HjO/kg dry aữ
Subscripts
a Air
abs Absolute
act Actual
atm Atmospheric
avg Average
c Combustion; cross-section
cr Critical point
c v Control volume
e Exit conditions
f Saturated liquid
fg Difference in property between saturated liquid
and saturated vapor
8 Saturated vapor
gen Generation
H High temperature (as in Tfj and Qfj)
i Inlet conditions
i ỉth component
L Low temperature (as in Ti^ and Qi^)
m Mixture
r Relative
R Reduced
rev Reversible
s Isentropic
sat Saturated
suư Surroundings
sys System
V Water vapor
0 Dead state
1 Initial or inlet state
2 Final or exit state
Superscripts
(over dot)
(over bar)
° (circle)
* (asterisk)
Quantity per unit time
Quantity per unit mole
Standard reference state
Quantity at 1 atm pressure
THERMODYNAMICS
An Engineering Approach
McGRAW-HILL SERIES IN MECHANICAL ENGINEERING
Alciatore/Histand:
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Barber;
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EDS, Inc.:
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r
ẩchaỂỗr ét af.i ,
SchẹyỊ"
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Ugural: ' ' !
uilm an;
White:
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Introduction to Mechatronics and M easurement Systems
Computational Fluid Dynamics: The Basics with
Applications
Fundamentals o f Aerodynamics
Introduction to Flight
M odem Compressible Flow
Intermediate Mechanics o f Materials
Vector Mechanics fo r Engineers: Statics and Dynamics
Mechanics o f Materials
Advanced Strength and Applied Stress Analysis
Heat and Mass Transfer: A Practical Approach
Introduction to Thermodynamics & Heat Transfer
Fluid Mechanics: Fundamentals and Applications
Fundamentals o f Thermal-Fluid Sciences
Essentials o f Fluid Mechanics: Fundamentals and
Applications
Intermediate Dynamics
Engineering Design: A Materials & Processing Approach
Mechanical Metallurgy
Measurement Systems: Application & Design
Technology Ventures: From Idea to Enterprise
Measurement & Data Analysis fo r Engineering & Science
I-DEAS Student Guide
Fluid Mechanics with Engineering Applications
Fundamentals o f Machine Elements
Internal Combustion Engine Fundamentals
Experimental Methods fo r Engineers
Heat Transfer
Fundamentals o f Finite Element Analysis
Convective Heat and Mass Transfer
Fundamentals o f Vibrations
Design o f Machinery
System Dynamics
An Introduction to Finite Element Method
The Science and Design o f Engineering Materials
Introduction to Manufacturing Processes
Shigley's Mechanical Engineering Design
Foundations o f Materials Science and Engineering
An Introduction to Combustion: Concepts and
Applications
Mechanical Design: An Integrated Approach
The Mechanical Design Process
Fluid Mechanics
Viscous Fluid Flow
CAD/CAM Theory and Practice
Mastering CAD/CAM
THERMODYNAMICS
An qineerinq Approac
SIXTH EDITION
YUNUS A. ẸENGEL
University o f Nevada, Reno
MICHAEL A. BOLES
North Carolina State University
Me
G r a w
Hill Higher Education
Boston Burr Ridge, IL Dubuque, lA New York San Francisco St. Louis
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The M c G r o w H i ll Companies
Higher Education
THERMODYNAMICS: AN ENGINEERING APPROACH, SIXTH EDITION
Published by McGraw-Hill, a business unit of The McGraw-Hill Companies, Inc., 1221 Avenue
of the Americas, New York, NY 10020. Copyright © 2008 by The McGraw-Hill Companies, Inc.
All rights reserved. Previous editions © 1989, 1994, 1998,2002, and 2006. No part of ứiis
publication may be reproduced or dis&ibuted in any form or by any means, or stored in a database
or retrieval system, without the prior written consent of The McGraw-Hill Companies, Inc.,
including, but not limited to, in any network or other electronic storage or transmission, or
broadcast for distance learning.
Some ancillaries, including electronic and print components, may not be available to customers
outside the United States.
This book is printed on acid-free paper.
4 5 6 7 8 9 0 DOW/DOW 0 9 8 7
ISBN 978-0-07-352921-9
MHID 0-07-352921-4
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Library of Congress Cataloging-in-Publication Data
Ọengel, Yunus A.
Thermodynamics ; an engineering approach / Yunus A. Ọengel,
Michael A. Boles.—6th ed.
p. cm.
Includes index.
ISBN 978-0-07-352921-9 — ISBN 0-07-352921^ (hard copy : alk. paper)
1. Thermodynamics. I. Boles, Michael A. II. Title.
TJ265.C43 2008b
621.402’!—dc22 2006021201
CIP
www.mhhe.com
There is nothing more frightful than ignorance in action.
Goethe
The society which scorns excellence in plumbing because plumbing is a
humble activity, and tolerates shoddiness in philosophy because philosophy
is an exalted activity will have neither good plumbing nor good philosophy.
Neither its pipes nor its theories will hold water.
John Gardner
Integrity without knowledge is weak and useless, while knowledge
without integrity is dangerous and dreadful.
Samuel Jackson
The concern for man and his destiny must always be the chief interest of all
technical effort. Never forget it among your diagrams and equations.
Albert Einstein
Mutual resemblance is the cause of contradiction; congruity is the
basis of solidarity; smallness of character is the source of arrogance:
weakness is the source of pride; impotence is the source
of opposition; and curiosity is the teacher of knowledge.
Said Nursi
The whole art of teaching is awakening the natural curiosity of young minds.
Anatole France
A great teacher is one whose spirit enters the souls of his students.
John Milton
Nobody will know. Nobody except you. But you have to live with yourself.
And it is always better to live with someone you respect—
because respect breeds confidence.
Jerome Weidman
Habit is a cable; we weave a thread of it everyday,
and at last we cannot break it.
Horace Mann
Genius is one percent inspiration and ninety-nine percent perspiration.
Thomas A. Edison
He who ceases to be better, ceases to be good.
Oliver Cromwell
When you call a thing mysterious, all that it means is that
you don’t understand it.
Lord Kelvin
Y u n u s A . Ẹ e n g e l is Professor E m e ritu s o f Mechanical Engineering a t
the University of Nevada, Reno. He received his B.s. in mechanical engineering from Istanbul Technical University and his M.S. and Ph.D. in
mechanical engineering from North Carolina State University. His research
areas are renewable energy, desalination, exergy analysis, and energy conservation. He served as the director of the Industrial Assessment Center
(lAC) at the University of Nevada, Reno, from 1996 to 2000. He has led
teams of engineering students to numerous manufacturing facilities in
Northern Nevada and California to do industrial assessments, and has prepared energy conservation, waste minimization, and productivity enhancement reports for them.
Dr. Ợengel is the coauthor of the widely adopted textbook Fundamentals
o f Thermal-Fluid Sciences, 2nd edition (2005) and Fluid Mechanics: Fundamentals and Applications (2006), both published by McGraw-Hill. He is
also the author of the textbook Heat Transfer: A Practical Approach, 3rd
edition (2008), also published by McGraw-Hill. Some of his textbooks have
been translated into Chinese, Japanese, Korean, Spanish, Portuguese, Turkish, Italian, and Greek.
Dr. Ợengel is the recipient of several outstanding teacher awards, and he
has received the ASEE MeriamAViley Distinguished Author Award in 1992
and again in 2000 for excellence in authorship. Dr. Ọengel is a registered
professional engineer in the state of Nevada, and is a member of the American Society of Mechanical Engineers (ASME) and the American Society for
Engineering Education (ASEE).
Michael A. Boles is Associate Professor of Mechanical and Aerospace
Engineering at North Carolina State University, where he earned his Ph.D.
in mechanical engineering and is an Alumni Distinguished Professor. Dr.
Boles has received numerous awards and citations for excellence as an engineering educator. He is a past recipient of the SAE Ralph R. Teetor Education Award and has been twice elected to the NCSU Academy of
Outstanding Teachers. The NCSU ASME student section has consistently
recognized him as the outstanding teacher of the year and the faculty member having the most impact on mechanical engineering students.
Dr. Boles specializes in heat transfer and has been involved in the analytical and numerical solution of phase change and drying of porous media.
He is a member of the American Society of Mechanical Engineers (ASME),
the American Society for Engineering Education (ASEE), and Sigma Xi.
Dr. Boles received the ASEE MeriamAViley Distinguished Author Award in
1992 for excellence in authorship.
VI
BRIEF CỮNTEMĨS
Chapter 1
INTRODUCTION AND BASIC CONCEPTS I 1
Chapter 2
ENERGY, ENERGY TRANSFER, AND GENERAL
ENERGY ANALYSIS I 51
Chapter 3
PROPERTIES OF PURE SUBSTANCES I 111
Chapter 4
ENERGY ANALYSIS OF CLOSED SYSTEMS I 165
Chapter 5
MASS AND E N ER G Y ANALYSIS
OF CONTROL VOLUMES I 221
Chapter 6
THE SECOND LAW OF THERMODYNAMICS I 283
Chapter 7
ENTROPY I 337
Chapter 8
EXERG Y; A M EASURE OF WORK
POTENTIAL I 433
Chapter 9
GAS POWER CYCLES I 497
Chapter 10
VAPOR AND COMBINED POWER CYCLES I 565
Chapter 11
R E FR IG ER A T IO N CYC LES I 623
Chapter 12
THERMODYNAMIC P R O P E R T Y RELATIONS I 661
Chapter 13
GAS M IXTURES I 701
Chapter 14
GAS-VAPOR MIXTURES
AND AIR-CONDITIONING I 737
Chapter 15
CHEMICAL REACTIONS I 773
Chapter 16
CHEMICAL AND PHASE EQUILIBRIUM I 817
Chapter 17
COMPRESSIBLE FLOW I 849
Appendix 1
PROPERTY TABLES AND CHARTS
(SI UNITS) I 909
Appendix 2
PROPERTY TABLES AND CHARTS
(ENGLISH UNITS) I 959
I vii
w ents
Preface xvii
Chapter 1
INTRODUCTION AND BASIC CONCEPTS I 1
1-1 Thermodynamics and Energy 2
Application Areas of Thermodynamics 3
1-2 Importance of Dimensions and Units 3
Some SI and English Units 5
Dimensional Homogeneity 8
Unity Conversion Ratios 9
1-3 Systems and Control Volumes 10
1 ^ Properties of a System 12
Continuum 12
1-5 Density and Specific Gravity 13
1-6 State and Equilibrium 14
The State Postulate 14
1-7 Processes and Cycles 15
The Steady-Flow Process 16
1-8 Temperature and the Zeroth Law
of Thermodynamics 17
Temperature Scales 17
The International Temperature Scale of 1990 (ITS-90) 20
1-9 Pressure 21
Variation of Pressure with Depth 23
1-10 The Manometer 26
Other Pressure Measurement Devices 29
1-11 The Barometer and Atmospheric Pressure 29
1-12 Problem-Solving Technique 33
Step 1: Problem statement 33
Step 2: Schematic 33
Step 3: Assumptions and Approximations 34
Step 4: Physical Laws 34
Step 5: Properties 34
Step 6; Calculations 34
Step 7: Reasoning, Verification, and Discussion 34
Engineering Software Packages 35
Engineering Equation Solver (EES) 36
A Remark on Significant Digits 38
Summary 39
References and Suggested Readings 39
Problems 40
Chapter 2
ENERGY, ENERGY TRANSFER, AND GENERAL
EN E R G Y ANALYSIS I 51
2-1 Introduction 52
2-2 Forms of Energy 53
Some Physical Insight to Internal Energy 55
More on Nuclear Energy 56
Mechanical Energy 58
2-3 Energy Transfer by Heat 60
Historical Background on Heat 61
2-4 Energy Transfer by Work 62
Electrical Work 65
2-5 Mechanical Forms of Work 66
Shaft Work 66
Spring Work 67
Work Done on Elastic Solid Bars 67
Work Associated with the stretching of a Liquid Film 68
Work Done to Raise or to Accelerate a Body 68
Nonmechanical Forms of Work 69
2-6 The First Law of Thermodynamics 70
Energy Balance 71
Energy Change of a System, 72
Mechanisms of Energy Transfer, £;„ and Eaji 73
2-7 Energy Conversion Efficiencies 78
Efficiencies of Mechanical and Electrical Devices 82
2-8 Energy and En\ ironment 86
Ozone and Smog 87
Acid Rain 88
The Greenhouse Effect: Global Warming
and Climate Change 89
Topic of Special Interest:
Mechanisms of Heat Transfer 92
Summary 96
References and Suggested Readings 97
Problems 98
IX
Chapter 3
PROPERTIES OF PURE SUBSTANCES M i l
3-1 Pure Substance 112
3-2 Phases of a Pure Substance 112
X I Contents
3-3
3-5
Phase-Change Processes
of Pure Substances 113
Compressed Liquid and Saturated Liquid 114
Saturated Vapor and Superheated Vapor 114
Saturation Temperature and Saturation Pressure 115
Some Consequences of and Psai Dependence 117
Property Diagrams for Phase-Change
Processes 118
1 The ĩ- ( /Diagram 118
2 The p~v Diagram 120
Extending the Diagrams to Include the Solid Phase 121
3 The P-7" Diagram 124
The P -v-r Surface 125
Property Tables 126
Enthalpy— A Combination Property 126
la Saturated Liquid and Saturated Vapor States 127
lb Saturated Liquid-Vapor Mixture 129
2 Superheated Vapor 132
3 Compressed Liquid 133
Reference state and Reference Values 135
The Ideal-Gas Equation of State 137
Is Water Vapor an Ideal Gas? 139
Compressibility Factor—A Measure
of Deviation from Ideal-Gas Behavior 139
Other Equations of State 144
Van der Waals Equation of state 144
Beattie-Bridgeman Equation of state 145
Benedict-Webb-Rubin Equation of state 145
Virial Equation of state 145
Topic of Special Interest: Vapor Pressure
and Phase Equilibrium 149
Summary 153
References and Suggested Readings 154
Problems 154
Chapter 4
ENERGY ANALYSIS OF CLOSED SYSTEMS I 165
4-1 Moving Boundary Work 166
Polytropic Process 171
4-2 Energy Balance for Closed Systems 173
4-3 Specific Heats 178
3-6
3-7
3-8
4-4 Internal Energy, Enthalpy, and Specific Heats
of Ideal Gases 180
Specific Heat Relations of Ideal Gases 182
4-5 Internal Energy, Enthalpy, and Specific Heats
of Solids and Liquids 189
Internal Energy Changes 189
Enthalpy Changes 189
Topic of Special Interest: Thermodynamic Aspects
of Biological Systems 193
Summary 200
References and Suggested Readings 201
Problems 201
Chapter 5
MASS AND ENERGY ANALYSIS
OF CONTROL VOLUMES I 221
5-1 Conservation of Mass 222
Mass and Volume Flow Rates 222
Conservation of Mass Principle 224
Mass Balance for Steady-Flow Processes 225
Special Case: Incompressible Flow 226
5-2 Flow Work and the Energy
of a Flowing Fluid 228
Total Energy of a Flowing Fluid 229
Energy Transport by Mass 230
5-3 Energy Analysis of Steady-Flow Systems 232
5-4 Some Steady-Flow Engineering Devices 235
1 Nozzles and Diffusers 235
2 Turbines and Compressors 238
3 Throttling Valves 241
4a Mixing Chambers 242
4b Heat Exchangers 244
5 Pipe and Duct Flow 246
5-5 Energy Analysis of Unsteady-Flow
Processes 248
Topic of Special Interest; General Energy Equation 254
Summary 257
References and Suggested Readings 258
Problems 258
Chapter 6
THE SECOND LAW OF THERMODYNAMICS I 283
6-1 Introduction to the Second Law 284
6-2 Thermal Energy Reservoirs 285