Index 795 E e (specific energy), 102, 707 E (total energy), 46, 62, 102, 106, 168, 749 E G (energy gain), 102 Edison, Thomas Alva, 477, 638 Effective molecular radius, 733t Effective voltage, 117–118 Efficiency, Defined, 460t of biological systems, 699–702 of food energy conversion, 706 of fuel cells, 636 of locomotion, 714, 716 of nozzle and diffuser systems, 681–685 second law, 340, 343, 345, 347 thermal. See Thermal efficiency work, 124–126 Efficiency ratio, power plant, 482 Einstein, Albert, 84 Einstein’s mass-energy relation, 748 Elastic modulus (γ), 713 Elastic work, 114–115 Electrical device example, 150–151 problem, 150 Electrical resistance, 125, 238, 770 Electrical resistivity, 238, 770 Electrical units current, fundamental units, 10 fundamental equations, 10 Electrical work current flow work, 117–118 polarization work, 118–120 Electric dipoles, 116 Electric field strength vector, (E), 118 Electric permittivity of a vacuum, 119 Electric potential, 117 Electric susceptibility, 119 various materials, 119t Electrochemical work, cell, 696 Electrodynamic, 782 Electrohydrodynamic coupling, 782–783 Electron spin quantum number, 748 Electrostatic equilibrium, 38 Emission spectrum of atomic hydrogen, 748 Emissivity, 129 Empedocles, 592 Endothermic reaction, 606 Energy balance general closed system, 108, 135 modified, 173, 282 Energy content basic food components, 707 common foods, 708 Energy conversion direct, 123, 701, 764 efficiency (η), 125, 340, 699–702 heat pump, 217, 339 nozzle, 174 Energy gain (E G ), 102 Energy level, degeneracy of, 749 Energy rate balance and biological rate of energy expenditure, 713 in a closed system, general, 108, 135, 138 equation for, 171, 285, 287 of life, 699 in a living cell, 698 modified, 172, 178, 296 in a nonequilibrium system, 104 in an open system, 698–699 general, 139, 171 in wet airstreams, 428 Energy rates of the primitive earth, 695 Energy transport heat modes of, 127–128 in living systems, 699f mechanical work modes, 108–116 mechanisms, 99–140 and nonconservative forces, 104 nonmechanical work modes, 116–123 rates, power modes of, 124 <strong>Engineering</strong> English units system, 12, 15, 25, 173 English Gun Barrel Proof Act, 27 Enthalpy change, measuring, 207 correction chart, 391f defined, 63 psychrometric, 426–427, 440 Entropy and aging, 718 analysis, 297 and chemical reactions, 621–625 Clausius’ definition of, 218–221 correction chart, 394f determining closed system direct method, 250 closed system indirect method, 250 and Gibbs function of formation, 625–626 of phase change production, 239–240 production of. See also Entropy production rate, 207, 237, 261, 281, 284, 579 diffusional mixing, 271 heat, 232–234 due to laminar viscous losses, 268, 307 mass flow, 280 work mode, 235–239 production ratio, 301, 301f transport of heat, 229–234 mass flow, 279–280 and the second law, 205–243 work mode, 231 Entropy balance closed system, 250 equation, 240–241, 271 modified, 282, 309 Entropy production rate fuel cell, 639 heat exchanger, 290–291 maximum, mixing liquids, 295f for viscous effects, 269 Entropy rate balance closed system, 240, 250, 672 equation for, 240–241 fuel cell, 636 general open system, 281 living system, 717 modified, 282, 296, 308 open system, 621, 699 problem, 281 shock waves, 678 Environment as a heat transfer fluid, 185 temperatures and survival curves, 718f Enzymes, 694–695 Equation of state dielectric, 119 empirical, 400 ideal gas, 41, 79 ideal gas mixtures, 412 for a magnetic field, 121 of nonlinear rubber band, 369 simple magnetic substance, 400 Equilibrium, defined, 36, 630 Equilibrium constant, 629, 634–635 Equilibrium reaction, 627, 630 Equilibrium state, 36, 747 Equilibrium temperature, 421 Equipartition of energy, 738–741 Equivalent gas constant, mixture, 410, 439 Ericsson, John, 490 Ericsson cycle, 490–493 Essergy, 319 Ethane, 549, 597f Ethylene, 394 Euler, Leonhard, 669 Eulerian analysis, 669 Evaporator, 542 Event-frequency table, 742t Excess air, 595 Exercise, thermodynamics of, 46, 47–48, 50 Exergy, 319 Exothermic reaction, 606 Expansion engines, 454 of a pure gas, 127 work, 400 Explosive energy, pressure vessels, 159–160 Extensive property defined, 37 generalized displacements, 116 as a point function, 107 External combustion engine, 486, 505 External forces, 673 F Factorial, 745 Fahrenheit, Gabriel Daniel, 28, 54, 92 Fanno line, 690 Faraday’s constant (F), 639 Farad (F), 639 Fats, 705 Fermi, Enrico, 728 Fermi-Dirac model, 749 Ferromagnetic material, 120 F (farad), 639 Fields conservative, 321 electric, 116 magnetic, 120–121 scalar, 320 vector, 320
796 Index First law of thermodynamics, 2, 46, 99–146 and efficiency, 528 Flash steam, 94, 164, 200 Fliegner’s formula, 665 FLMT system, 11, 29 Flowchart, problem solution, 130 Flowstream kinetic energy, 173 mass flow rate, 169 specific potential energy, 174 Flow work, 168 FLt system, 11 Fluid friction, 113, 681 Food energy intake, 698 Force, defined, 105 Forcing function, 116 Fourier, Joseph, 769 Fourier’s law, 128, 233 Fowler, R. H., 42 Freezing, 69 Freon, 548 Friction factor, 518, 777 Friction power, Otto cycle, 505 Fuel cells, 636–641 Fulton, Robert, 454–455 Fundamental units length, 6 time, 6 Fusion line, 66 G g c (dimensional constant), defined, 26 Gage pressure, 40 Galen, Claudius, 9 Galilei, Galileo, 724 Gas compressor, 498 Gas constant (R), 220 equivalent, for a mixture (R m ), 441 Gases defined, 68 properties at low pressure, 81t Gas power cycles, 447–527 Gas tables, 382–384 Gas turbine aircraft engine, 499–502 Gäugler type of heat pipe, 234 Gaussian velocity distribution, 735 Gay-Lussac, Joseph Louis, 397 Gay-Lussac’s law, 397 Generalized displacement, 116 Generalized force (F), 116 General open system, 139, 171, 198, 353 Georgian, John C., 29 Gibbs, Josiah Willard, 65, 364 Gibbs chemical potential, 122 Gibbs-Dalton ideal gas mixture law, 414, 621 Gibbs function (G) conditions for chemical reaction, 627 of formation, 625–626 and entropy, 625–626 Gibbs phase equilibrium condition, 366 Gibbs’ phase rule, 65 Goodenough, G. A., 404 Gorrie, John, 569 Grain, 424 Gram mole, defined, 14 Ground state defined, 322 notation, 323 Grover, George M., 234 Guggenheim, E. A., 42 H H (henry), 787t Heat of combustion, 607 defined, 1, 64 as a fluid, 208 of formation, 604–607 of reaction, 607–613 Heat engine characteristics of, 449t cyclic, 212, 212f Heat entropy flux, 245 Heat exchange closed loop, 470 open loop, 470 problem, 203, 358 regenerators, 470 shell and tube, 289 single-tube, single-pass, 289f, 290 temperature profiles, 290, 291f Heat loss and animal size, 711 Heat pipes, 234 Heat production energy losses, 612 entropy of, 232 Heat pump, 216 characteristics of, 536f Heat rate (power plant), 151–152, 482 Heat transfer coefficient of, 264, 266 modes of, 128–130 rate of, 150 reversible, 220, 227 Heat transport, 127 of entropy, 229–231 Helmholtz, Hermann Ludwig Ferdinand von, 363 Helmholtz function (F), 363, 365 Henry (H), 787t Heracleitus, 592 Heron of Alexandria, 474 Hertz (Hz), 787t Hess, Germain Henri, 604 Hess’ law, 604 Higher heating value (HHV), 608 Hilsch, Rudolph, 302 Homogeneous substance, defined, 36 Hooke’s law, 114 Horsepower, 30, 454 Humidification, 424 Humidity ratio (ω), 418, 440 Hydraulic flow systems, 306t Hydraulic jump, 306 Hydrocarbons, 596 classification of, 596f Hydrodynamic flow systems, 305–306 Hydroelectric water turbines, 187 Hz (hertz), 787t I IC engine. See Internal combustion engine Ideal gas Berthelot corrections, 374 diffuser efficiency, 684 internal energy of, 80 of a mixture, 412 and molar enthalpy, 391 in a polytropic process, 111 Ideal gas equation, 41, 619 Impulse turbine, 474 Incompressible materials fluid, 135 liquids, 78 example, 79 specific heat of, 77 state equations for, 77 Independent events, 750 Indicated power, Otto cycle, 505 Indicated work, Otto cycle, 460 Indicator diagram, 455, 505 Indirect calorimetry, 703 Instantaneous electrical power, 118 Insulated rigid container, filling, 298f Intensive properties defined, 37 as point functions, 107 Intermolecular collisions, 732–734 Internal combustion engine, 125, 502 typical ceramic components, 517f Internal energy of an ideal gas, 80 Internal heat flux, 232 International Bureau of Weights and Measures (BIPM), 212 International Conferences on the Properties of Steam, 396 International System of Units (SI), 730 Inversion temperature, 181 Ion pump, 696 Irreversibility defined, 328 rate, 328 Irreversible processes heat transfer, 227, 338 reactions, 627, 631 work, 250 Isenthalpic devices, defined, 180 throttling, 180 vapor-compression cycle, 544, 575 Isentropic compressibility, 687 compression ratio, 492 Isentropic efficiency compressor, 312, 401 thermal efficiency, 461–466 Rankine cycle, 479 Isentropic pressure ratio, 488 Isentropic process, 223, 241–242, 383, 488, 666 expansion, supersaturated state, 665f Isentropic sound wave, properties of, 657, 657f Isentropic stagnation state, 654f density, 653–655 enthalpy, 660 pressure, 654–655, 660, 684 properties of, 653–655, 685
- Page 2 and 3:
Modern Engineering Thermodynamics
- Page 4 and 5:
Modern Engineering Thermodynamics R
- Page 6 and 7:
Dedication WHAT IS AN ENGINEER AND
- Page 8 and 9:
Contents PREFACE . . . . . . . . .
- Page 10 and 11:
Contents ix 7.6 Heat Engines Runnin
- Page 12 and 13:
Contents xi 14.13 Air Standard Gas
- Page 14 and 15:
Preface TEXT OBJECTIVES This textbo
- Page 16 and 17:
Preface xv Step 5. Write down the b
- Page 18 and 19:
Acknowledgments I wish to acknowled
- Page 20 and 21:
Resources That Accompany This Book
- Page 22 and 23:
List of Symbols A a B COP CR c c p
- Page 24 and 25:
Prologue PARIS FRANCE, 10:35 AM, AU
- Page 26 and 27:
CHAPTER 1 The Beginning CONTENTS 1.
- Page 28 and 29:
1.2 Why Is Thermodynamics Important
- Page 30 and 31:
1.3 Getting Answers: A Basic Proble
- Page 32 and 33:
1.5 How Do We Measure Things? 7 bei
- Page 34 and 35:
1.6 Temperature Units 9 THE DEVELOP
- Page 36 and 37:
1.7 Classical Mechanical and Electr
- Page 38 and 39:
1.7 Classical Mechanical and Electr
- Page 40 and 41:
1.9 Modern Units Systems 15 where M
- Page 42 and 43:
1.10 Significant Figures 17 CRITICA
- Page 44 and 45:
1.10 Significant Figures 19 WHAT AB
- Page 46 and 47:
1.11 Potential and Kinetic Energies
- Page 48 and 49:
1.11 Potential and Kinetic Energies
- Page 50 and 51:
Summary 25 FIGURE 1.19 Case study 1
- Page 52 and 53:
Problems 27 Problems (* indicates p
- Page 54 and 55:
Problems 29 14. Determine the mass
- Page 56 and 57:
Problems 31 49. Using the CGS units
- Page 58 and 59:
CHAPTER 2 Thermodynamic Concepts CO
- Page 60 and 61:
2.3 Phases of Matter 35 System boun
- Page 62 and 63:
2.4 System States and Thermodynamic
- Page 64 and 65:
2.6 Thermodynamic Processes 39 WHAT
- Page 66 and 67:
2.7 Pressure and Temperature Scales
- Page 68 and 69:
2.9 The Continuum Hypothesis 43 Sur
- Page 70 and 71:
2.10 The Balance Concept 45 Solutio
- Page 72 and 73:
2.11 The Conservation Concept 47 or
- Page 74 and 75:
2.11 The Conservation Concept 49 Th
- Page 76 and 77:
Summary 51 change in the mass of X
- Page 78 and 79:
Problems 53 Problems (* indicates p
- Page 80 and 81:
Problems 55 and Death rate = α 2 +
- Page 82 and 83:
CHAPTER 3 Thermodynamic Properties
- Page 84 and 85:
3.3 Fun with Mathematics 59 CRITICA
- Page 86 and 87:
3.4 Some Exciting New Thermodynamic
- Page 88 and 89:
3.6 Enthalpy 63 WHO WAS AMALIE EMMY
- Page 90 and 91:
3.7 Phase Diagrams 65 WHO WAS EMMY
- Page 92 and 93:
Pressure Vapor 3.7 Phase Diagrams 6
- Page 94 and 95:
3.7 Phase Diagrams 69 WHAT IS A “
- Page 96 and 97:
3.7 Phase Diagrams 71 considerable
- Page 98 and 99:
3.8 Quality 73 10 5 300 C Critical
- Page 100 and 101:
3.8 Quality 75 Although Eq. (3.26)
- Page 102 and 103:
3.9 Thermodynamic Equations of Stat
- Page 104 and 105:
3.9 Thermodynamic Equations of Stat
- Page 106 and 107:
3.9 Thermodynamic Equations of Stat
- Page 108 and 109:
3.9 Thermodynamic Equations of Stat
- Page 110 and 111:
3.10 Thermodynamic Tables 85 Critic
- Page 112 and 113:
3.12 Thermodynamic Charts 87 vð100
- Page 114 and 115:
3.13 Thermodynamic Property Softwar
- Page 116 and 117:
Summary 91 and e = E/m = u + V2 2g
- Page 118 and 119:
Problems 93 c. For a saturated mixt
- Page 120 and 121:
Problems 95 specific enthalpy of sa
- Page 122 and 123:
Problems 97 Table 3.23 Problem 65 M
- Page 124 and 125:
CHAPTER 4 The First Law of Thermody
- Page 126 and 127:
4.3 The First Law of Thermodynamics
- Page 128 and 129:
4.3 The First Law of Thermodynamics
- Page 130 and 131:
4.4 Energy Transport Mechanisms 105
- Page 132 and 133:
4.5 Point and Path Functions 107 4.
- Page 134 and 135:
4.6 Mechanical Work Modes of Energy
- Page 136 and 137:
4.6 Mechanical Work Modes of Energy
- Page 138 and 139:
4.6 Mechanical Work Modes of Energy
- Page 140 and 141:
4.6 Mechanical Work Modes of Energy
- Page 142 and 143:
4.7 Nonmechanical Work Modes of Ene
- Page 144 and 145:
4.7 Nonmechanical Work Modes of Ene
- Page 146 and 147:
4.7 Nonmechanical Work Modes of Ene
- Page 148 and 149:
4.7 Nonmechanical Work Modes of Ene
- Page 150 and 151:
4.9 Work Efficiency 125 In the case
- Page 152 and 153:
4.12 Heat Modes of Energy Transport
- Page 154 and 155:
4.13 Heat Transfer Modes 129 Table
- Page 156 and 157:
4.14 A Thermodynamic Problem Solvin
- Page 158 and 159:
4.14 A Thermodynamic Problem Solvin
- Page 160 and 161:
4.15 How to Write a Thermodynamics
- Page 162 and 163:
4.15 How to Write a Thermodynamics
- Page 164 and 165:
Summary 139 The general open system
- Page 166 and 167:
Problems 141 11.* Determine the hea
- Page 168 and 169:
Problems 143 where K = 0.810 lbf. D
- Page 170 and 171:
Problems 145 Table 4.12 Problem 67
- Page 172 and 173:
CHAPTER 5 First Law Closed System A
- Page 174 and 175:
5.2 Sealed, Rigid Containers 149 In
- Page 176 and 177:
5.4 Power Plants 151 Step 7. Calcul
- Page 178 and 179:
5.5 Incompressible Liquids 153 The
- Page 180 and 181:
1Q 2 − 1 W 2 = mðu 2 − u 1 Þ
- Page 182 and 183:
5.8 Closed System Unsteady State Pr
- Page 184 and 185:
5.9 The Explosive Energy of Pressur
- Page 186 and 187:
Problems 161 Problems (* indicates
- Page 188 and 189:
Problems 163 31. A thermoelectric g
- Page 190 and 191:
Problems 165 where v, T, and r are
- Page 192 and 193:
CHAPTER 6 First Law Open System App
- Page 194 and 195:
6.2 Mass Flow Energy Transport 169
- Page 196 and 197:
6.3 Conservation of Energy and Cons
- Page 198 and 199:
6.4 Flow Stream Specific Kinetic an
- Page 200 and 201:
6.5 Nozzles and Diffusers 175 m (a)
- Page 202 and 203:
6.5 Nozzles and Diffusers 177 We ar
- Page 204 and 205:
6.6 Throttling Devices 179 These as
- Page 206 and 207:
6.6 Throttling Devices 181 For an i
- Page 208 and 209:
6.7 Throttling Calorimeter 183 The
- Page 210 and 211:
6.8 Heat Exchangers 185 Convective
- Page 212 and 213:
6.9 Shaft Work Machines 187 6.9 SHA
- Page 214 and 215:
6.9 Shaft Work Machines 189 1 Basem
- Page 216 and 217:
6.10 Open System Unsteady State Pro
- Page 218 and 219:
6.10 Open System Unsteady State Pro
- Page 220 and 221:
6.10 Open System Unsteady State Pro
- Page 222 and 223:
Problems 197 we have _m R / _m D =
- Page 224 and 225:
Problems 199 Problems (* indicates
- Page 226 and 227:
Problems 201 32.* A commercial slid
- Page 228 and 229:
Summary 203 59. Incompressible liqu
- Page 230 and 231:
CHAPTER 7 Second Law of Thermodynam
- Page 232 and 233:
7.3 The Second Law of Thermodynamic
- Page 234 and 235:
7.4 Carnot’s Heat Engine and the
- Page 236 and 237:
7.4 Carnot’s Heat Engine and the
- Page 238 and 239:
7.5 The Absolute Temperature Scale
- Page 240 and 241:
7.5 The Absolute Temperature Scale
- Page 242 and 243:
7.6 Heat Engines Running Backward 2
- Page 244 and 245:
7.7 Clausius’s Definition of Entr
- Page 246 and 247:
7.8 Numerical Values for Entropy 22
- Page 248 and 249:
7.8 Numerical Values for Entropy 22
- Page 250 and 251:
7.8 Numerical Values for Entropy 22
- Page 252 and 253:
7.10 Differential Entropy Balance 2
- Page 254 and 255:
7.11 Heat Transport of Entropy 229
- Page 256 and 257:
7.13 Entropy Production Mechanisms
- Page 258 and 259:
7.14 Heat Transfer Production of En
- Page 260 and 261:
7.15 Work Mode Production of Entrop
- Page 262 and 263:
7.15 Work Mode Production of Entrop
- Page 264 and 265:
7.16 Phase Change Entropy Productio
- Page 266 and 267:
Summary 241 ■ Indirect method inv
- Page 268 and 269:
Problems 243 amount of work W irr i
- Page 270 and 271:
Problems 245 a. If the heat pump is
- Page 272 and 273:
Problems 247 51. Develop a program
- Page 274 and 275:
CHAPTER 8 Second Law Closed System
- Page 276 and 277:
8.2 Systems Undergoing Reversible P
- Page 278 and 279:
8.2 Systems Undergoing Reversible P
- Page 280 and 281:
8.2 Systems Undergoing Reversible P
- Page 282 and 283:
8.3 Systems Undergoing Irreversible
- Page 284 and 285:
8.3 Systems Undergoing Irreversible
- Page 286 and 287:
8.3 Systems Undergoing Irreversible
- Page 288 and 289:
8.3 Systems Undergoing Irreversible
- Page 290 and 291:
8.3 Systems Undergoing Irreversible
- Page 292 and 293:
8.3 Systems Undergoing Irreversible
- Page 294 and 295:
8.3 Systems Undergoing Irreversible
- Page 296 and 297:
8.4 Diffusional Mixing 271 Exercise
- Page 298 and 299:
Summary 273 Note that this example
- Page 300 and 301:
Problems 275 15. A 20.0 ft 3 tank c
- Page 302 and 303:
Problems 277 46. a. Determine a for
- Page 304 and 305:
CHAPTER 9 Second Law Open System Ap
- Page 306 and 307:
9.4 Open System Entropy Balance Equ
- Page 308 and 309:
9.4 Open System Entropy Balance Equ
- Page 310 and 311:
9.5 Nozzles, Diffusers, and Throttl
- Page 312 and 313:
9.5 Nozzles, Diffusers, and Throttl
- Page 314 and 315:
9.6 Heat Exchangers 289 Exercises 1
- Page 316 and 317:
9.6 Heat Exchangers 291 (T H ) (T H
- Page 318 and 319:
9.7 Mixing 293 Now, _m air is given
- Page 320 and 321:
9.7 Mixing 295 Critical value of y,
- Page 322 and 323:
9.9 Unsteady State Processes in Ope
- Page 324 and 325:
9.9 Unsteady State Processes in Ope
- Page 326 and 327:
9.9 Unsteady State Processes in Ope
- Page 328 and 329:
9.9 Unsteady State Processes in Ope
- Page 330 and 331:
9.9 Unsteady State Processes in Ope
- Page 332 and 333:
9.9 Unsteady State Processes in Ope
- Page 334 and 335:
Problems 309 Multiplying this equat
- Page 336 and 337:
Problems 311 entropy production rat
- Page 338 and 339:
Problems 313 heat is added to the b
- Page 340 and 341:
Problems 315 55.* Determine the max
- Page 342 and 343:
Problems 317 The cavitation process
- Page 344 and 345:
CHAPTER 10 Availability Analysis CO
- Page 346 and 347:
10.3 What Are Conservative Forces?
- Page 348 and 349:
10.6 Availability 323 WHAT IS A SYS
- Page 350 and 351:
10.6 Availability 325 and the total
- Page 352 and 353:
10.7 Closed System Availability Bal
- Page 354 and 355:
10.7 Closed System Availability Bal
- Page 356 and 357:
10.8 Flow Availability 331 EXAMPLE
- Page 358 and 359:
s − s 0 = c ln T T 0 10.8 Flow Av
- Page 360 and 361:
10.10 Modified Availability Rate Ba
- Page 362 and 363:
10.10 Modified Availability Rate Ba
- Page 364 and 365:
10.11 Energy Efficiency Based on th
- Page 366 and 367:
10.11 Energy Efficiency Based on th
- Page 368 and 369:
10.11 Energy Efficiency Based on th
- Page 370 and 371:
10.11 Energy Efficiency Based on th
- Page 372 and 373:
10.11 Energy Efficiency Based on th
- Page 374 and 375:
10.11 Energy Efficiency Based on th
- Page 376 and 377:
Summary 351 In this problem, we hav
- Page 378 and 379:
Summary 353 7. The general open sys
- Page 380 and 381:
Problems 355 12.5 Btu/hr·ft ·R. I
- Page 382 and 383:
Problems 357 flow rate of 15.0 lbm/
- Page 384 and 385:
Problems 359 85. Create a specific
- Page 386 and 387:
CHAPTER 11 More Thermodynamic Relat
- Page 388 and 389:
11.2 Two New Properties: Helmholtz
- Page 390 and 391:
11.2 Two New Properties: Helmholtz
- Page 392 and 393:
11.4 Maxwell Equations 367 11.4 MAX
- Page 394 and 395:
11.4 Maxwell Equations 369 then,
- Page 396 and 397:
11.5 The Clapeyron Equation 371 and
- Page 398 and 399:
11.6 Determining u, h, and s from p
- Page 400 and 401:
11.6 Determining u, h, and s from p
- Page 402 and 403:
11.6 Determining u, h, and s from p
- Page 404 and 405:
11.7 Constructing Tables and Charts
- Page 406 and 407:
11.8 Thermodynamic Charts 381 so th
- Page 408 and 409:
11.9 Gas Tables 383 where p r is th
- Page 410 and 411:
11.10 Compressibility Factor and Ge
- Page 412 and 413:
11.10 Compressibility Factor and Ge
- Page 414 and 415:
11.10 Compressibility Factor and Ge
- Page 416 and 417:
11.10 Compressibility Factor and Ge
- Page 418 and 419:
11.10 Compressibility Factor and Ge
- Page 420 and 421:
11.10 Compressibility Factor and Ge
- Page 422 and 423:
11.11 Is Steam Ever an Ideal Gas? 3
- Page 424 and 425:
Summary 399 equation, and a series
- Page 426 and 427:
Problems 401 20.* Estimate h fg for
- Page 428 and 429:
Problems 403 Design Problems The fo
- Page 430 and 431:
CHAPTER 12 Mixtures of Gases and Va
- Page 432 and 433:
12.2 Thermodynamic Properties of Ga
- Page 434 and 435:
12.2 Thermodynamic Properties of Ga
- Page 436 and 437:
12.2 Thermodynamic Properties of Ga
- Page 438 and 439:
12.3 Mixtures of Ideal Gases 413 Th
- Page 440 and 441:
12.3 Mixtures of Ideal Gases 415 Co
- Page 442 and 443:
12.4 Psychrometrics 417 Finally, th
- Page 444 and 445:
12.4 Psychrometrics 419 EXAMPLE 12.
- Page 446 and 447:
12.6 The Sling Psychrometer 421 The
- Page 448 and 449:
12.6 The Sling Psychrometer 423 p w
- Page 450 and 451:
12.7 Air Conditioning 425 WHAT ENVI
- Page 452 and 453:
12.8 Psychrometric Enthalpies 427 E
- Page 454 and 455:
12.8 Psychrometric Enthalpies 429 o
- Page 456 and 457:
12.9 Mixtures of Real Gases 431 Whe
- Page 458 and 459:
12.9 Mixtures of Real Gases 433 and
- Page 460 and 461:
12.9 Mixtures of Real Gases 435 The
- Page 462 and 463:
12.9 Mixtures of Real Gases 437 Sol
- Page 464 and 465:
Summary 439 Last, we combine Dalton
- Page 466 and 467:
Problems 441 Problems (* indicates
- Page 468 and 469:
Problems 443 exhaust gas is an idea
- Page 470 and 471:
Problems 445 57.* Cooling towers ar
- Page 472 and 473:
CHAPTER 13 Vapor and Gas Power Cycl
- Page 474 and 475:
13.2 Part I. Engines and Vapor Powe
- Page 476 and 477:
13.2 Part I. Engines and Vapor Powe
- Page 478 and 479:
13.2 Part I. Engines and Vapor Powe
- Page 480 and 481:
13.2 Part I. Engines and Vapor Powe
- Page 482 and 483:
13.4 Rankine Cycle 457 A B Reversib
- Page 484 and 485:
13.5 Operating Efficiencies 459 For
- Page 486 and 487:
13.5 Operating Efficiencies 461 13.
- Page 488 and 489:
13.5 Operating Efficiencies 463 b.
- Page 490 and 491:
13.5 Operating Efficiencies 465 Sta
- Page 492 and 493:
13.6 Rankine Cycle with Superheat 4
- Page 494 and 495:
13.7 Rankine Cycle with Regeneratio
- Page 496 and 497:
13.7 Rankine Cycle with Regeneratio
- Page 498 and 499:
13.7 Rankine Cycle with Regeneratio
- Page 500 and 501:
13.8 The Development of the Steam T
- Page 502 and 503:
13.9 Rankine Cycle with Reheat 477
- Page 504 and 505:
13.9 Rankine Cycle with Reheat 479
- Page 506 and 507:
13.10 Modern Steam Power Plants 481
- Page 508 and 509:
13.10 Modern Steam Power Plants 483
- Page 510 and 511:
13.10 Modern Steam Power Plants 485
- Page 512 and 513:
13.12 Air Standard Power Cycles 487
- Page 514 and 515:
13.13 Stirling Cycle 489 Q H 4 1 4
- Page 516 and 517:
13.14 Ericsson Cycle 491 Q H 4 1 3
- Page 518 and 519:
13.15 Lenoir Cycle 493 Exercises 28
- Page 520 and 521:
13.16 Brayton Cycle 495 Solution Us
- Page 522 and 523:
13.16 Brayton Cycle 497 Equation (7
- Page 524 and 525:
13.17 Aircraft Gas Turbine Engines
- Page 526 and 527:
13.17 Aircraft Gas Turbine Engines
- Page 528 and 529:
13.18 Otto Cycle 503 T Q H 1 1 1 v
- Page 530 and 531:
13.18 Otto Cycle 505 Exercises 40.
- Page 532 and 533:
13.18 Otto Cycle 507 and, since the
- Page 534 and 535:
13.20 Miller Cycle 509 13.19.1 Mode
- Page 536 and 537:
13.20 Miller Cycle 511 Then, from F
- Page 538 and 539:
13.21 Diesel Cycle 513 to stroll on
- Page 540 and 541:
13.21 Diesel Cycle 515 Solution a.
- Page 542 and 543:
13.22 Modern Prime Mover Developmen
- Page 544 and 545:
13.23 Second Law Analysis of Vapor
- Page 546 and 547:
13.23 Second Law Analysis of Vapor
- Page 548 and 549:
13.23 Second Law Analysis of Vapor
- Page 550 and 551:
Summary 525 Fill port 160 mm End of
- Page 552 and 553:
Problems 527 7. The thermal efficie
- Page 554 and 555:
efficiency increase if the condense
- Page 556 and 557:
Problems 531 horsepower hour. Assum
- Page 558 and 559:
Problems 533 72. Determine the valu
- Page 560 and 561:
CHAPTER 14 Vapor and Gas Refrigerat
- Page 562 and 563:
14.3 Carnot Refrigeration Cycle 537
- Page 564 and 565:
14.4 In the Beginning There Was Ice
- Page 566 and 567:
14.4 In the Beginning There Was Ice
- Page 568 and 569:
14.5 Vapor-Compression Refrigeratio
- Page 570 and 571:
14.5 Vapor-Compression Refrigeratio
- Page 572 and 573:
14.6 Refrigerants 547 T 3 2s 2 p 3
- Page 574 and 575:
14.7 Refrigerant Numbers 549 14.7 R
- Page 576 and 577:
14.7 Refrigerant Numbers 551 R-110
- Page 578 and 579:
14.8 CFCs and the Ozone Layer 553 H
- Page 580 and 581:
14.9 Cascade and Multistage Vapor-C
- Page 582 and 583:
14.9 Cascade and Multistage Vapor-C
- Page 584 and 585:
14.9 Cascade and Multistage Vapor-C
- Page 586 and 587:
14.10 Absorption Refrigeration 561
- Page 588 and 589:
14.11 Commercial and Household Refr
- Page 590 and 591:
14.11 Commercial and Household Refr
- Page 592 and 593:
14.11 Commercial and Household Refr
- Page 594 and 595:
14.14 Reversed Brayton Cycle Refrig
- Page 596 and 597:
14.14 Reversed Brayton Cycle Refrig
- Page 598 and 599:
14.15 Reversed Stirling Cycle Refri
- Page 600 and 601:
14.16 Miscellaneous Refrigeration T
- Page 602 and 603:
14.16 Miscellaneous Refrigeration T
- Page 604 and 605:
14.18 Second Law Analysis of Refrig
- Page 606 and 607:
14.18 Second Law Analysis of Refrig
- Page 608 and 609:
2. The coefficient of performance o
- Page 610 and 611:
Problems 585 13.* A refrigeration u
- Page 612 and 613:
Problems 587 Loop B Station 1B Stat
- Page 614 and 615:
Problems 589 under these conditions
- Page 616 and 617:
CHAPTER 15 Chemical Thermodynamics
- Page 618 and 619:
15.2 Stoichiometric Equations 593 1
- Page 620 and 621:
15.2 Stoichiometric Equations 595 C
- Page 622 and 623:
15.3 Organic Fuels 597 ANSWERS SOME
- Page 624 and 625:
15.4 Fuel Modeling 599 Hydrocarbon
- Page 626 and 627:
15.4 Fuel Modeling 601 equation, si
- Page 628 and 629:
15.5 Standard Reference State 603 I
- Page 630 and 631:
15.6 Heat of Formation 605 and H 2
- Page 632 and 633:
15.7 Heat of Reaction 607 EXAMPLE 1
- Page 634 and 635:
15.7 Heat of Reaction 609 CRITICAL
- Page 636 and 637:
15.7 Heat of Reaction 611 Then, h P
- Page 638 and 639:
15.8 Adiabatic Flame Temperature 61
- Page 640 and 641:
15.8 Adiabatic Flame Temperature 61
- Page 642 and 643:
15.8 Adiabatic Flame Temperature 61
- Page 644 and 645:
15.9 Maximum Explosion Pressure 619
- Page 646 and 647:
15.10 Entropy Production in Chemica
- Page 648 and 649:
15.10 Entropy Production in Chemica
- Page 650 and 651:
15.11 Entropy of Formation and Gibb
- Page 652 and 653:
15.12 Chemical Equilibrium and Diss
- Page 654 and 655:
15.12 Chemical Equilibrium and Diss
- Page 656 and 657:
15.12 Chemical Equilibrium and Diss
- Page 658 and 659:
H 2 O !ð1 − yÞH 2 O + yðv H2
- Page 660 and 661:
15.14 The van’t Hoff Equation 635
- Page 662 and 663:
15.15 Fuel Cells 637 Anode Electrol
- Page 664 and 665:
15.15 Fuel Cells 639 The maximum po
- Page 666 and 667:
15.16 Chemical Availability 641 and
- Page 668 and 669:
ðn i /n fuel Þðc pi Þ E system
- Page 670 and 671:
Problems 645 where j = 4n + m kgmol
- Page 672 and 673:
Problems 647 c. The percent excess
- Page 674 and 675:
Problems 649 77. Determine the mola
- Page 676 and 677:
CHAPTER 16 Compressible Fluid Flow
- Page 678 and 679:
16.3 Isentropic Stagnation Properti
- Page 680 and 681:
16.4 The Mach Number 655 Note that
- Page 682 and 683:
16.4 The Mach Number 657 Table 16.1
- Page 684 and 685:
16.4 The Mach Number 659 Since for
- Page 686 and 687:
16.5 Converging-Diverging Flows 661
- Page 688 and 689:
16.5 Converging-Diverging Flows 663
- Page 690 and 691:
16.6 Choked Flow 665 T a a p a = co
- Page 692 and 693:
16.6 Choked Flow 667 Exercises 16.
- Page 694 and 695:
16.7 Reynolds Transport Theorem 669
- Page 696 and 697:
16.7 Reynolds Transport Theorem 671
- Page 698 and 699:
16.8 Linear Momentum Rate Balance 6
- Page 700 and 701:
16.9 Shock Waves 675 16.9 SHOCK WAV
- Page 702 and 703:
16.9 Shock Waves 677 and, for an id
- Page 704 and 705:
16.9 Shock Waves 679 6 5 4 S P /(m
- Page 706 and 707:
16.10 Nozzle and Diffuser Efficienc
- Page 708 and 709:
16.10 Nozzle and Diffuser Efficienc
- Page 710 and 711:
Summary 685 Since for a diffuser, M
- Page 712 and 713:
Problems 687 Problems (* indicates
- Page 714 and 715:
43. 0.800 lbm/s of air passes throu
- Page 716 and 717:
Problems 691 A plot of this functio
- Page 718 and 719:
CHAPTER 17 Thermodynamics of Biolog
- Page 720 and 721:
17.3 Thermodynamics of Biological C
- Page 722 and 723:
17.3 Thermodynamics of Biological C
- Page 724 and 725:
17.4 Energy Conversion Efficiency o
- Page 726 and 727:
17.4 Energy Conversion Efficiency o
- Page 728 and 729:
17.5 Metabolism 703 Table 17.3 Brea
- Page 730 and 731:
17.6 Thermodynamics of Nutrition an
- Page 732 and 733:
17.6 Thermodynamics of Nutrition an
- Page 734 and 735:
17.6 Thermodynamics of Nutrition an
- Page 736 and 737:
17.7 Limits to Biological Growth 71
- Page 738 and 739:
17.7 Limits to Biological Growth 71
- Page 740 and 741:
17.8 Locomotion Transport Number 71
- Page 742 and 743:
17.9 Thermodynamics of Aging and De
- Page 744 and 745:
17.9 Thermodynamics of Aging and De
- Page 746 and 747:
1/3 V most efficient = P o ρAC D S
- Page 748 and 749:
Problems 723 a. If the monster cons
- Page 750 and 751:
Problems 725 the officer asks Paul
- Page 752 and 753:
CHAPTER 18 Introduction to Statisti
- Page 754 and 755:
18.3 Kinetic Theory of Gases 729 3.
- Page 756 and 757:
U trans = 3 2 NkT (Continued ) 18.3
- Page 758 and 759:
18.4 Intermolecular Collisions 733
- Page 760 and 761:
18.5 Molecular Velocity Distributio
- Page 762 and 763:
18.5 Molecular Velocity Distributio
- Page 764 and 765:
18.6 Equipartition of Energy 739 We
- Page 766 and 767:
18.7 Introduction to Mathematical P
- Page 768 and 769:
18.7 Introduction to Mathematical P
- Page 770 and 771: 18.7 Introduction to Mathematical P
- Page 772 and 773: 18.8 Quantum Statistical Thermodyna
- Page 774 and 775: 18.9 Three Classical Quantum Statis
- Page 776 and 777: 18.11 Monatomic Maxwell-Boltzmann G
- Page 778 and 779: 18.12 Diatomic Maxwell-Boltzmann Ga
- Page 780 and 781: 18.12 Diatomic Maxwell-Boltzmann Ga
- Page 782 and 783: 18.13 Polyatomic Maxwell-Boltzmann
- Page 784 and 785: Summary 759 In this chapter, we sum
- Page 786 and 787: Problems 761 4. Find the temperatur
- Page 788 and 789: CHAPTER 19 Introduction to Coupled
- Page 790 and 791: 19.3 Linear Phenomenological Equati
- Page 792 and 793: 19.4 Thermoelectric Coupling 767 Eq
- Page 794 and 795: 19.4 Thermoelectric Coupling 769 Th
- Page 796 and 797: 19.4 Thermoelectric Coupling 771 wh
- Page 798 and 799: 19.4 Thermoelectric Coupling 773 Th
- Page 800 and 801: 19.4 Thermoelectric Coupling 775 b.
- Page 802 and 803: 19.5 Thermomechanical Coupling 777
- Page 804 and 805: 19.5 Thermomechanical Coupling 779
- Page 806 and 807: 19.5 Thermomechanical Coupling 781
- Page 808 and 809: water), it seems reasonable that li
- Page 810 and 811: Problems 785 b. For a Knudson gas,
- Page 812 and 813: Appendix A: Physical Constants and
- Page 814 and 815: Appendix B: Greek and Latin Origins
- Page 816 and 817: Appendix B 791 Table B.4 Plural End
- Page 818 and 819: Index Page numbers followed by f in
- Page 822 and 823: Index 797 Isobaric coefficient of v
- Page 824 and 825: Index 799 Ranque, Georges Joseph, 3
- Page 826 and 827: Index 801 William III, King of Engl