Index

From Lectures in Thermodynamics: Heat and Work, by J. M. Haile, Macatea Productions, 2002. An ebook version is also available.

For values of properties for 43 pure fluids, visit our Property Calculator.

Acceleration of gravity, 4, 100, 561
Acentric factor, 94, 121, 531
. . . Of pure fluids, 521
Adiabat
. . . Irreversible, 235, 239, 243, 328, 337
. . . Reversible, 190f, 193, 319, 326, 335, 337f, 353
Adiabatic
. . . Compressibility, 424
. . . Compression, 190f, 235, 319, 352f,
. . . . . . 381, 397, 409, 412
. . . Expansion, 381, 409
. . . Mixing, 273f, 276f
. . . Processes, 325f, 352f
. . . Work, 163f, 166f, 352f
Additivity, pairwise, 108
Alkane, 109, 110
. . . Second virial coefficients of, 89, 106
Always True, 72, 113, 151, 214, 248, 256,
. . . . . . 271, 322, 343, 346, 349, 425f, 490,
. . . . . . 493, 495f
Analysis, 158, 274, 276
Antiknock compound, 406
Antoine equation, 226
Argon, 126
Attractive force
. . . Dipolar, 102
. . . Dispersion, 104f, 107
. . . Induction, 104
. . . Nondipolar, 103
Avogadro's number, 15, 651

Batch process, 218, 251
Benzene, 530
. . . TS diagram, 357
Benzenebergs, 35
Bernoulli equation, 271, 301, 312
Blowers, 304, 312
Boiling point
. . . Of hydrogen selenide, 56
. . . Of hydrogen sulfide, 56
. . . Of hydrogen telluride, 56
. . . Of pure fluids, 521f
. . . Of water, 36, 56
Boundary, 13, 151, 154, 169, 256, 260
. . . Kinds of, 19
Brayton cycle,
. . . Analysis, 398
. . . Description, 397
. . . Efficiency of, 398, 401
Bulk mass transfer, 13, 462

Calorimeter, 173f, 202
. . . Constant volume, 173
. . . Flow, 202, 298f
Calorimetry, 177, 298f, 431, 444
Carbon dioxide, 229f
Carbon tetrachloride, 56, 530
Carnot
. . . Coefficient of performance, 411
. . . Cycle, 319f, 338, 389, 402
. . . Efficiency, 322, 332, 376, 389, 391, 402
. . . Heat pump, 408
Change of state, 43, 51f
. . . Irreversible, 143
. . . Reversible, 51f, 138, 140f, 142, 144, 316,
. . . . . . 334, 337
Chemical reaction, 7, 9, 18, 25, 217, 253, 306,
. . . . . . 376, 423, 427, 500
Clapeyron equation, 222, 248, 482
Classes
. . . Of derivatives, 424
. . . Of properties, 24f
. . . Of pure fluids, 108f
Classical mechanics, 9
Clausius-Clapeyron equation, 225, 482
Clean notebook, 11, 28, 113, 216
Closed system, 19
. . . Always true, 247f
. . . First law, 168, 247
. . . Fundamental equations, 342f, 421f
. . . Second law, 337f, 376
Coefficient of performance, 411
Compressibility
. . . Factor, 69, 72, 78f, 82f, 122f, 225, 445f,
. . . . . . 453, 499
. . . Isothermal, 52, 66, 87, 179, 424, 498
. . . . . . divergence, 67f, 478
. . . . . . of ideal gas, 70
. . . . . . of liquids, 66, 530
. . . . . . of nitrogen, 127
. . . . . . of van der Waals fluid, 88
. . . Lee-Kesler correlation for, 123
Compression
. . . Adiabatic, 190f, 230, 235, 319
. . . -Ignition, engines, 405
. . . Isothermal, 188, 230, 319, 321
Compressor, isothermal, 153, 305
Conceptual, 26, 196, 214, 247f, 339, 342, 419f,
. . . . . . 422, 430, 434, 445, 449, 458, 495f, 497
. . . From models, 434f
Conservative force, 100f, 108
Constants, 561
. . . Avogadro's number, 15, 561
. . . Boltzmann, 561
. . . Gas, 15, 70, 175, 561
Constants (con'd)
. . . Planck, 6, 16, 561
Constraints, 262f
. . . On adiabatic processes, 325f
. . . On heat transfer, 360f
. . . Special, 264
Continuous process, 218, 251f
Contraction, sudden, 266
Control volume, 251
Conundrum, engineer's, 246
Correlation, 90, 121, 458, 500
. . . For ideal-gas heat capacities, 524
. . . For liquid molar volumes, 49, 531
. . . For vapor pressures, 48f, 224, 226, 527
. . . For virial coefficients, 120f, 122, 451
. . . Lee-Kesler, 123
Corresponding states, 98f, 114f, 500
. . . In critical properties, 118f, 121f
. . . In molecular parameters, 115f
Counter-current flow, 283, 290, 294
Critical opalescence, 478
Critical point, 34, 42, 67, 478, 485
. . . Compressibility factor at, 118f, 531
. . . Of propane, 68
. . . Of pure fluids, 521f
. . . Of water, 36
Cubic equation of state, 86f, 472f,483f, 486
. . . Solving for volume, 95, 475f
Cubic polynomial, roots of, 534f
Cycle, 315f
. . . Brayton, 397f
. . . Carnot, 319, 332, 389, 402
. . . Diesel, 405
. . . Gas power, 395
. . . Otto, 404
. . . Rankine, 332, 380f
. . . Vapor-Liquid, 379


Death Star, 28
Degrees of freedom, 175, 262
Delta operator, 4f, 220f, 254
Density expansion, 78f
Derivatives
. . . Classes of, 424
. . . Definition, 503
. . . Partial, 509
Design, 158, 229, 237, 239, 256f, 275, 279
. . . Heat exchanger, 362, 365f
Deviation from ideality
. . . Differences, 445, 456, 499
. . . Ratios, 445, 499
Diagram
. . . PH, 212f, 279, 468
. . . Process, 133
. . . PT, 39, 71, 223
Diagram (con'd)
. . . Pv, 41f, 91f, 119, 136, 397, 404, 405,
. . . . . . 466, 473
. . . State, 136
. . . TH, 292f, 363f, 370f
. . . TS, 354f, 357, 381, 387, 390, 392, 397,
. . . . . . 403, 404, 405, 411f, 414
Diesel cycle, 405
Differential, 504f
. . . Driving force, 141f, 316
. . . Exact, 22, 51, 168, 256, 329f, 342, 442, 507
. . . Total, 23, 147, 172, 202, 341, 497f, 507
Diffuser, 268
Diffusion, 13
Diffusional equilibrium, 18, 462, 463
Dipolar
. . . Associating fluids, 108f, 112
. . . Nonassociating fluids, 108f, 111
Dipole, 102
. . . Moments, 102f, 104
Dispersion force, 104f, 106f
Dissipative force, 134
Driving force, 18, 134, 462
. . . Differential, 141, 316, 362
. . . Finite, 143
. . . Heat Transfer, 289f, 290, 366
Duhem's theorem, 21, 31f


Efficiency, 305
. . . Carnot, 322, 332, 376, 389, 391, 402
. . . Maximum thermal, 330
. . . Mechanical, 137, 145
. . . Of Brayton cycle, 400f
. . . Of pumps, 308f
. . . Of Rankine cycle, 388, 391
. . . Table of, 307
. . . Thermal, 306, 316, 324, 330, 376
Electrical work, 165, 173, 412
Electricity, generation of, 379f
Energy, 3, 6
. . . Balance, 253f, 256, 270f
. . . Definition, 6
. . . Gibbs, 422
. . . Gravitational, 100
. . . Helmholtz, 422
. . . Internal, 166, 172f
. . . Kinetic, 5, 169
. . . Mechanical balance, 270
Energy (con'd)
. . . Molecular kinetic, 15
. . . Molecular potential, 101f, 108
. . . Potential energy, 4, 163, 169
. . . Thermal, 15
. . . Work as, 4, 14
. . . Work to displace, 4
. . . Work to elevate, 4
Energy densities of fuels, 6
Engine
. . . Heat, 316f, 324, 379f, 395f
. . . Internal combustion, 403f
. . . Steam, 302f, 315
Enthalpy, 199f
. . . Changes, 201, 270
. . . Definition, 201
. . . Incompressible fluid, 201, 270
. . . Isothermal P-derivative, 209, 348
. . . Physical interpretation, 201
. . . Residual, 450
. . . Steady flow, 256
. . . Total differential of, 202, 248, 281, 432
Entropy, 341f
. . . Definition, 330
. . . Heat capacities and, 344f
. . . Isothermal P-derivative, 347, 426
. . . Isothermal V-derivative, 345, 426
. . . Residual, 450,
. . . Total differential of, 341, 346f, 433f
Equation of state
. . . As model, 65f, 82f, 486
. . . Corresponding states for, 123f
. . . Cubics, 86f, 93
. . . Ideal gas, 68f
. . . Nearly incompressible liquid, 66
. . . P-independent, 435
. . . Peng-Robinson, 94
. . . Redlich-Kwong, 93
. . . Redlich-Kwong-Soave, 94
. . . Types of, 22
. . . V-independent, 22, 434
. . . Van der Waals, 86f, 485
. . . Virial equations, 77f
Equilibrium, 18
. . . Diffusional, 18, 462, 463
. . . Mechanical, 18, 462
. . . Phase, 462, 473
. . . States, 17f, 140
Equilibrium (con'd)
. . . Thermal, 18, 462
Ethane, 446
. . . PH diagram, 468
Ethanolberg, 35
Exact differential, 23, 507
. . . Test for, 23, 345, 426
Expansion
. . . Adiabatic, 319
. . . Isenthalpic, 208f
. . . Isothermal, 319
. . . Joule, 180
. . . Joule-Thomson, 280, 467
. . . Sudden, 266
Expansivity, volume, 53, 66, 214
. . . Definition, 53
. . . Joule-Thomson inversion and, 212
. . . Of benzene, 530
. . . Of carbon tetrachloride, 530
. . . Of ideal gas, 70
. . . Of n-heptane, 530
. . . Of propane, 530
. . . Of steam, 53
. . . Of water, 53, 56, 530
. . . Relate to isothermal entropy derivative, 537
. . . Relate to heat capacities, 204
Experiment, 15, 26, 37, 70, 128, 458, 487
. . . Calorimetry, 173, 182, 299
. . . Joule's, 163f, 196, 315
. . . Reduction of, 55, 65, 499
. . . Second virial coefficient from, 80, 120, 122
. . . Thermal, 173, 177, 182, 299, 430, 444
. . . Volumetric, 177, 182, 430, 444
Explosion, 49
Extensive
. . . Quantity, 25
. . . State, 32
External pressure, 131, 142, 181


Fan, 304
Feasibility, 351f
First law, 495
. . . Closed systems, 168, 196
. . . Open steady flow, 253, 256, 270
Flow
. . . Counter-current, 283, 290
. . . Parallel, 283, 288
. . . Work, 254f
Fluid, 34, 40
. . . Classes of, 108
Force
. . . Attractive molecular, 80, 87, 102, 103f
. . . Conservative, 100, 108
. . . Dipolar, 102
. . . Dispersion, 104f
. . . Dissipative, 134
. . . Driving, 18, 134, 462
. . . . . . differential, 141, 316, 362
. . . . . . finite, 143
. . . . . . heat transfer, 289f, 290, 366
. . . Gravitational, 99f
. . . Induction, 104
. . . Intermolecular, 87, 101f, 166
. . . Overlap, 101
. . . Repulsive molecular, 80, 87, 101f
. . . Virial coefficients and, 80
Free expansion, 181
Freon, 416
Friction, 134f, 301f, 309
Fundamental eqs., 342, 421f, 430, 498
. . . Uses of, 423, 430f, 462


Gas (or vapor), 34, 87
. . . Constant, 15, 70, 175, 561
. . . Liquefaction, 467
. . . Power cycles, 395f
. . . Turbine plants, 395f
Gibbs, 53, 430
. . . Energy,
. . . . . . extensive, 422, 426, 435, 462
. . . . . . molar, 463, 473, 481
. . . . . . residual, 444, 449, 452, 464, 473
. . . -Helmholtz equations, 427
. . . Phase rule, 32
Global warming, 416
Gravity, 4, 99f
. . . Feed tank, 264
Heat, 167f
. . . Duty, 287
. . . Engine, 317, 325, 379f, 395f
. . . Latent, 217, 220f, 481f
. . . Pump, 408f
. . . Reversible isobaric process, 201
. . . Sensible, 218f
. . . Sign convention for, 168
Heat capacity
. . . Ideal gas, 179, 204, 215
. . . . . . correlation for, 524
. . . Incompressible fluids, 206
. . . Isobaric, 202, 204, 215, 248, 362f
. . . Isometric, 172f, 204, 215
. . . Measurement, 173, 298
. . . Nearly incompressible liquids, 179, 206,
. . . . . . 215
. . . Ratio, 205, 402
. . . Relation between, 204, 215
. . . Temperature effect on, 175, 219f
Heat exchanger
. . . Design, 362f
. . . Double-tube, 283
. . . Second-law violations, 362f, 369
. . . Tube-in-shell, 285
Heat transfer
. . . Area, 366, 369
. . . Constraints on, 362f
. . . Isobaric, reversible, 199
Helmholtz energy, 422f, 435
. . . Definition, 422
. . . Physical interpretation of, 425
. . . T-derivative, 426
Heptane, 56, 530
Hickam, Homer, 199
Homogeneous function, 25
Hydrogen bonding, 57f, 108, 121, 486
Hypothetical process, 52, 146, 436, 442


Ice, 32, 35, 55, 58f, 223, 413
Ideal gas, 68f
. . . Enthalpy, 201
. . . Joule-Thomson coefficient, 211
. . . On PT diagram, 71
. . . Processes, 185f, 205f
. . . Properties, 70, 201
. . . Residual properties and, 441f, 456
Incompressible fluid, 66
. . . Enthalpy, 201
. . . Heat capacities, 206
Integrating factor, 329
Intensive
. . . Quantity, 25
. . . State, 32
Interaction, 13f, 17, 33
. . . Mass, 13
. . . Thermal, 15f
. . . Work modes, 14, 17
Intermolecular force, 87, 101, 166
. . . Attractive, 87, 102, 104
. . . Dipolar, 102
. . . Dispersion, 104
. . . Hydrogen bonding, 57f, 108, 121, 486
. . . Induction, 104
. . . Nondipolar, 103
. . . Overlap, 101
. . . Repulsive, 87, 101
. . . Second virial coefficient and, 89
. . . Switch, 441
Intermolecular potential energy, 101f, 107f,
. . . . . . 166
Internal combustion engine, 403f
Internal energy
. . . Definition, 166
. . . Description, 172f
. . . Isometric T-derivative, 172
. . . Isothermal V-derivative, 176, 348, 431
. . . Residual, 451, 454
. . . Tables of, 182
. . . Total differential, 172, 247, 431
Irreversibility, 144, 194
Irreversible process, 143, 164, 178, 187,
. . . . . . 190, 235, 242f, 327, 335, 337, 338,
. . . . . . 342f, 412, 436, 438
Isenthalpic process, 208f, 273f, 280, 381
Isobaric
. . . Heat capacity, 202f, 219, 248, 298, 365
. . . Process, 199f, 218, 240, 322, 397, 412
Isometric
. . . Heat capacity, 172f, 179, 181, 203, 196
. . . Process, 73, 186f, 232, 233f
Isotherm, Reversible, 188
Isothermal
. . . Compression, 188, 231, 233, 319f, 409
. . . Expansion, 319, 409
Isothermal compressibility, 66
. . . Definition, 52
. . . Divergence, 67f
. . . Of benzene, 56, 530
. . . Of carbon tetrachloride, 56, 530
. . . Of ideal gas, 70
. . . Of n-heptane, 56, 530
. . . Of nearly incompressible liquid, 66
. . . Of propane, 68, 530
. . . Of steam, 53
. . . Of water, 53, 56, 530


Joule,
. . . Expansion, 180
. . . Experiment, 163f
. . . -Thomson coefficient, 211, 281
. . . -Thomson expansion, 280, 412, 467
. . . -Thomson inversion curve, 211f
. . . Unit of energy, 3, 561


Kinetic energy, 5
. . . Change, 5, 262f, 301, 305
. . . Molecular, 15, 166


Latent heat, 220
. . . Melting, 220
. . . Relate to PT curve, 222
. . . Sublimation, 221
. . . Vaporization, 220f, 481f
Law,
. . . First, 495
. . . . . . closed system, 168f, 196
. . . . . . open steady-flow, 253, 270
. . . Second, 495
. . . . . . closed system, 337f
. . . . . . open steady-flow, 351
. . . . . . violations of, 362
Lee-Kesler correlation, 123f
Lennard-Jones potential, 107
Lever Rule, 489
. . . Enthalpy, 278f, 384, 469
. . . Entropy,. . . 384
. . . Volume, 467
Light, 5, 478
Liquid, 32, 34f, 55f, 71, 72f, 66, 87, 91, 93,
. . . . . . 123, 174f, 179, 182, 206, 209, 212,
. . . . . . 220, 222, 239f, 256f, 264f, 268f,
. . . . . . 276f, 285, 318, 356f, 380f, 390, 409,
. . . . . . 450, 461f, 464f, 467, 472f, 483f
. . . Molar volumes of, 531
Log-mean temperature, 367, 536
London force, 105
Lost work, 134f, 140, 144, 327


Mass Transfer, 13
. . . Bulk, 13, 18, 462
. . . Diffusion, 13, 18, 462f
Material balance, 251, 263, 274, 466
. . . Steady state, 253
Maximum-work theorem, 332
Maxwell relations, 345f, 425
Measurable, 26, 31, 51, 65, 128, 176,
. . . . . . 196, 208f, 211, 214, 247, 338, 341,
. . . . . . 348, 419f, 424, 430f, 458, 494, 497
Mechanical
. . . Efficiency, 145
. . . Energy balance, 270
. . . Equilibrium, 18, 462
. . . Instability, 53
Mechanics
. . . Classical, 9
. . . Continuum, 9
. . . Quantum, 9
. . . Statistical, 9, 69, 89, 116, 174
Melting
. . . Latent heat of, 220
. . . Line, 34, 40f, 47, 222
Melting point
. . . Of hydrogen selenide, 56
. . . Of hydrogen sulfide, 56
. . . Of hydrogen telluride, 56
. . . Of pure substances, 521f
. . . Of water, 56
Metastable state, 49, 91f
Methane, 153
. . . PT diagram, 223
Microwave oven, 16
Mixing, Adiabatic, 273f, 276f
Model, 65f, 72
. . . Bad choice for, 72f
. . . Cubic, 86f
. . . Ideal gas, 68f
. . . Nearly incompressible fluid, 66
. . . P-independent, 22, 435, 449
. . . Parameters in, 486
. . . Problem solving and, 152
. . . Process, 152, 155, 398, 496
. . . PvT, 65f, 77f, 86f
. . . Substance, 152, 187, 239, 398
. . . V-independent, 22, 434, 453
. . . Vapor pressure from, 472f
. . . Virial equations, 82
Molar volume of liquids, 531
Molecular kinetic energy, 15
Multistep process, 229f, 239f
Murphy, 487


Nearly incompressible fluid, 66, 74
. . . Enthalpy, 201, 209
. . . Heat capacities, 206, 215, 220
. . . Internal energy, 179
. . . On PT diagram, 71
Newton, 3, 561
. . . Law of gravity, 99
. . . Method for algebraic equations, 95,
. . . . . . 476, 538
. . . Second law, 4
NIST Website, 37
Nitrogen, 119, 146, 186f, 188f, 352
. . . Heat capacity of, 176, 402
. . . Isothermal compressibility of liquid, 127
. . . Second virial coefficient of, 120
Nondipolar substance, 103, 110
Nozzle, 268
Ohm's law, 165
Otto cycle, 404
Overlap forces, 101, 107
Ozone depletion, 416


Paddle-wheel experiment, 164
Pairwise additivity, 108
Parallel flow, 283, 288
Parameters in models, 93f, 486
Path, Hypothetical, 52, 146, 436, 442
Peng-Robinson Equation, 94
PH diagram, 212f, 279, 468
Phase change, 34, 220, 239f, 276f, 357,
. . . . . . 379f, 412f, 467
Phase diagram, 33f
. . . PH, 212, 279, 468
. . . PT, 39, 71, 223
. . . Pv, 41, 91f, 119, 136, 397, 404f, 466, 477
. . . PvT, 31f, 52
. . . TH, 292f, 363f, 370f
. . . TS, 337f, 354f, 381, 387, 390, 392f,
. . . . . . 397, 399, 403f, 411f, 414
Phase equilibria
. . . Calculation of VL, 474f
. . . Criteria for, 461f
Phase rule, 32, 39, 43, 54, 117, 164, 172,
. . . . . . 202, 220
Photon, 16
Piston/cylinder, 14, 132, 134, 141, 180, 188,
. . . . . . 190, 199, 210
Pitzer's acentric factor, 94, 121f, 521, 531
Planck constant, 6, 16, 561
Polarizability, 105
. . . Table of, 106
Polynomial approximation, 78
Potential energy, 4
. . . Change, 4, 163f, 265, 302
. . . Molecular, 101, 107f, 116
Power, 254, 300f, 379f, 395f
Power series, 78
Pressure
. . . -Enthalpy diagram, 212, 279, 468
. . . External, 131, 142, 181
. . . -Temperature diagram, 39, 71, 223
. . . -Volume diagram, 41, 91f, 119, 136, 397,
. . . . . . 404f, 466, 477
Problem
. . . Analysis, 158, 274, 276
. . . Design, 158, 229, 237, 239, 256f, 275, 279
. . . Solving, 150f, 495f
Process, 18f
. . . Adiabatic, see Adiabatic
. . . Batch, 218, 251
. . . Continuous, 218, 251f
. . . Cyclic, see Cycle
. . . Diagram, 133
. . . Hypothetical, 52, 146, 436, 442
. . . Ideal gas, 185f, 205f
. . . Isobaric, 199f, 218, 240, 322, 397, 412
. . . Isometric, 73, 186f, 232, 233f
. . . Kinds of, 19
. . . Model, 152, 155, 398, 496
. . . Multi-step, 229f, 239f
. . . One-step, 185f
. . . Variable, 19, 23, 26, 133, 137, 163, 168,
. . . . . . 188, 193, 206, 218, 226, 376, 494
. . . Workfree, 169, 186, 218, 232, 273f,
. . . . . . 285, 287, 325, 335, 360f, 368, 382,
. . . . . . 389, 404, 412, 423
Propane, 436, 530
. . . Compressibility factor, 79, 81, 83
. . . Heat capacity, 177
. . . Isothermal compressibility, 68
. . . PT diagram, 71
. . . Vapor-liquid saturation properties, 479, 487
. . . Virial coefficient, 81, 451
Properties, 18, 22f
. . . Classes of, 25f
. . . Conceptual, 26
. . . Importance of, 24f
. . . Measurable, 26
. . . Number to set state, 21, 32, 262f
. . . Residual, 441f, 449f
PSALMS, 150f, 186, 271, 311, 319
PT diagram, 39, 71, 223
Pump, 305
. . . Efficiency of, 308f
Pv diagram, 41f, 91f, 119, 136, 397, 404,
. . . . . . 405, 466, 473
. . . Corresponding states and, 119
Quality, 277, 280, 384
Quantum mechanics, 9


R-134a, 413f, 417, 556
Rain, 170
Rankine cycle,
. . . Analysis of, 382
. . . Description of, 380
. . . Efficiency of, 388
Reaction kinetics, 9
Redlich-Kwong Equation, 93, 476, 485
Redlich-Kwong-Soave Eq., 94, 476, 485
Reference state, 182, 201, 339
Refrigerant, 413, 416
Repulsive force, 80, 87, 101f
Reservoir, 316
Residual properties, 441f
. . . Definition, 443
. . . From models, 449f
. . . Lee-Kesler correlation, for 123f
Reversible
. . . Change, 138, 140f, 142, 316
. . . Work, 135f, 143
Roots of cubics, 95, 475f, 534

Scaling laws, 98f
Secant method, 476, 540
Second law, 495
. . . Closed system, 337f
. . . Open steady-flow, 351
. . . Violations of, 362
Second virial coefficient
. . . Corresponding states for, 120f, 122
. . . Density expansion, 79, 447
. . . Intermolecular forces and, 89
. . . Of argon, 126
. . . Pressure expansion, 82, 447
Sensible heat, 218f
Shaft work, 255, 298f
Sign convention, 15, 132, 168
Solid, 32, 34f, 39, 47, 60, 69
Spark-ignition,
. . . Internal-combustion engine, 404
Spinodal, 91f, 95, 475
. . . From PvT model, 477f
Standard problem, 43, 51, 73, 131, 140, 151,
. . . . . . 158, 229, 239, 493
Stanley steamer, 303
State, 17, 22, 64
. . . Changing, 51f
State (con'd)
. . . Corresponding, 98f, 114f
. . . Diagram, 33f, 39f, 136
. . . Equilibrium, 17f, 140, 254
. . . For pures, 31
. . . For water, 36
. . . Identifying, 43f
. . . Metastable, 49, 91f
. . . Reference, 182, 201, 339
. . . Steady, 252
State diagram (see also, process diagram),
. . . . . . 33f, 39f, 136
State function, 18, 100, 136, 146, 166, 329, 507
Steady flow
. . . Energy balance, 253f, 256
. . . First law, 253, 256
. . . Independent variables, 262f
. . . Material balance, 251f
. . . Second law, 351
. . . Work, 255
Steady state, 252
Steam
. . . Engine, 302, 315
. . . Quality, 277, 280, 384
. . . Tables, 42f, 542
. . . Turbine, 302, 380f, 387
Strategy for problem solving, 150
Sublimation, 34, 39, 41
. . . Latent heat of, 221f, 223
Surroundings, 12f, 16, 18f, 131f, 135, 142,
. . . . . . 167, 170, 253, 263, 270, 315, 328
Switch on molecular forces, 441
System, 12, 151
. . . Choice of, 285f


Tables of properties, 37, 182, 339
Taylor expansion, 77
Temperature, 15, 18, 22f, 31f, 47, 62, 166
. . . -enthalpy diagrams, 292f, 363f, 370f
. . . -entropy diagrams, 337f, 354f, 381,
. . . . . . 387, 390, 392f, 397, 399, 403f, 411f,
. . . . . . 414
. . . Of approach, 295, 365, 369
Test for exactness, 23, 345, 426
TH diagram, 292f, 363f, 370f
Thermal
. . . Efficiency, 306, 316, 324, 330, 376
. . . Energy, 15
. . . Equilibrium, 18, 462
. . . Experiment (see also calorimetry),
. . . . . . 173, 177, 182, 299, 430, 444
. . . Interaction, 15f, 20
. . . Pressure coefficient, 54, 177, 426, 484
. . . . . . of benzene, 57, 530
. . . . . . of carbon tetrachloride, 57, 530
. . . . . . of ideal gas, 70
. . . . . . of n-heptane, 57, 530
. . . . . . of propane, 530
. . . . . . of water, 57, 530
. . . . . . relate to heat capacities, 204
Titanic, 59
Ton of refrigeration, 413
Total differential, 23, 507
. . . Enthalpy, 202, 208, 211, 248, 281, 432
. . . Entropy, 341f, 346, 433f
. . . Internal energy, 172, 247, 431f . . .
. . . Volume, 23, 52, 54, 62, 147
Transient process, 252, 500
Transport phenomena, 9
Triple point, 32, 34, 36, 39, 56, 182
. . . Latent heats at, 221
. . . Of water, 36, 59, 340
Triple product rule, 54, 281, 345, 385, 512, 515
TS diagram, 337f, 354f, 381, 387, 390, 392f,
. . . . . . 397, 399, 403f, 411f, 414
. . . Benzene, 357
. . . Water, 355
Turbine, 302f, 306, 317, 319, 380f, 387, 395f,
. . . . . . 398, 410, 412, 494


Unstable system, 53, 92


Vacuum, 16, 181
Van der Waals
. . . Equation, 86f, 476f, 485f
. . . Forces, 105
. . . Isotherms on Pv, 88
. . . Loops, 90, 473, 475, 477
. . . Parameters in, 90, 106, 486
. . . Second virial coefficient of, 89
Vapor (or gas), 32, 40, 68f
Vapor-compression heat pump, 408
Vapor-liquid
. . . Equilibrium (VLE), 462f,
. . . Power cycles, 379f
Vapor-pressure curve, 34, 39, 41, 222f, 472f
. . . Correlation, 226, 527
. . . From PvT models, 472f
. . . Lee-Kerlser correlation for,
. . . Water, 225, 543f
Vaporization, latent heat, 220f, 481f
Venn diagram, 246
Virial coefficient
. . . Alkane, 89, 106
. . . Corresponding states for, 120, 122
. . . Intermolecular forces and, 89
. . . Of argon, 126
. . . Propane, 451
. . . Second in density, 79, 447
. . . Second in pressure, 82, 447
. . . Third in density, 79
. . . Third in pressure, 82
. . . Van der Waals, 89
Virial equation, 77f
. . . In density, 78f
. . . In pressure, 82
Volume,
. . . Control, 251
. . . Excluded, 87
. . . Free, 87
. . . From cubic, 95, 534f
. . . Liquid, 531
. . . Residual, 445f, 451
. . . Total differential of, 23, 52, 54, 62, 147
Volume expansivity, 53, 66, 214, 386
. . . Definition, 53
. . . Joule-Thomson inversion and, 212
. . . Of benzene, 530
. . . Of carbon tetrachloride, 530
. . . Of ideal gas, 70
. . . Of n-heptane, 530
. . . Of propane, 530
. . . Of steam, 53
. . . Of water, 53, 56, 530
. . . Relate to isothermal entropy derivative, 537
. . . Relate to heat capacities, 204
Volumetric experiments, 177, 182, 430, 444
Warming, global, 416
Water, 16f, 37, 62, 82f, 530, 542
. . . Density maximum, 22
. . . Dipole moment of, 104
. . . Hydrogen bonding in, 55f
. . . Isothermal compressibility, 53, 56, 530
. . . Melting line, 40, 223
. . . PH diagram, 213, 279
. . . PT diagram, 40, 223
. . . States of, 36, 42f, 542
. . . Thermal pressure coefficient, 57, 530
. . . Triple point of, 35, 36
. . . TS diagram, 355
. . . Vapor pressure, 543f
. . . Vapor pressure curve, 225
. . . Volume expansivity, 53, 56, 530
Waterwheel, 302
Windmill, 300
Work, 4, 23, 129f, 168
. . . Adiabatic, 163, 166, 168f, 352f
. . . Against gravity, 4, 99
. . . Against molecular forces, 107f
. . . Electrical, 165, 173, 412
. . . Equivalence to energy, 5
. . . Flow, 254f
. . . Lost, 134f, 141
. . . Modes of, 14, 17
. . . Reversible, 135f, 141, 143
. . . Shaft, 254, 298f
. . . Sign convention for, 132
. . . Steady flow, 254
. . . To change volume, 14, 131
. . . To displace, 4
. . . To elevate, 4
Workfree process, 169, 186, 218

X-ray diffraction, 59

Yaws correlation, 527

Zero Kelvin, 15