Page 426 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
P. 426

P1: JsY
                                              March 12, 2007
               AT029-Manual
  AT029-INDEX
         406 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS
         Riazi method, 127
                                            Surface/interfacial tension, 12,
         Riedel equation, 313, 323  AT029-Manual-v9.cls  Supercritical fluid, 200 16:37          U
         Riedel method, 342                      356–361                        Units
                                              predictive methods, 358–361         composition, 21–22
                                              theory and definition, 356–358       conversion, 25
                        S                     units, 24                           density, 20–21
                                                                                  diffusion coefficients, 23–24
         SAFT model, 386                                                          energy, 22
         Saturation curves, ethane, 209                     T                     force, 19
         Saturation pressure, thermodynamic                                       fundamental, 18
             properties, 251– 254           Temperature                           gas-to-oil ratio, 24
         Saybolt viscosity, 35                triple point, 199                   importance and types, 17–18
         Scatchard-Hildebrand relation, 258, 261  units, 19, 19–20                kinematic viscosity, 23
         Schmidt number, 345                Tensiometer, 357                      length, 18
         SCN groups                         Thermal conductivity, 12, 339–345     mass, 18
          characteristics, 161                critical, 341                       mass flow rates, 20
          exponential model, 165–167          gases, 339–342                      molar density, 20–21
          molecular weight boundaries, 168    liquids, 342–345                    molecular weight, 19
         Self-diffusion coefficient, 345       versus temperature, 340             moles, 19
         Sensitivity of fuel, 138             units, 23                           prefixes, 18
         Separation by solvents, 96         Thermal conductivity detector, 90     pressure, 19
         Shear stress, 331                  Thermodynamic properties, 232–292     rates and amounts of oil and gas,
         Shift parameter, 208                 boiling point, elevation, 282–284      24–25
         SI units, 18                         calculation for real mixtures, 263  solubility parameter, 24
         Size exclusion chromatography, 93–94  density, 300–305                   specific energy, 22
         Smoke point, petroleum fractions, 142  departure functions, 236–237      specific gravity, 21
         Solid-liquid equilibrium, 385–388    enthalpy, 316–318                   surface tension, 24
         Solid solubility, 276–281            freezing point depression, 281–283  temperature, 19–20
         Solid solution model, 378, 380–382   fugacity, 237–238                   thermal conductivity, 23
         Solids                               generalized correlations, 238–241   time, 18–19
          density, 304–305                    heat capacity, 319–321              viscosity, 23
          fugacity calculation, 261–263       heat of combustion, 324–326         volume, 20
          vapor pressure, 314–316             heat of vaporization, 321–324       volumetric flow rates, 20
         Solubility, 259–260                  heats of phase changes, 321–324   UOP characterization factor, 13
         Solubility parameter, units, 24      ideal gases, 241–247
         Solvents, 9                          measurable, 235–236
         Soreide correlation, 58              mixtures, 247–251                                 V
         Sound velocity                       nomenclature, 232–234
          equations of state based on, 286–287  property estimation, 238        Van der Waal equation, 204–205
          Lennard-Jones and van der Waals     residual properties, 236–237      Van der Waals parameters, velocity of
             parameters, 288–289              saturation pressure, 251–254           sound data, 289
          prediction of fluid properties,      solid-liquid equilibria, 276–281  Van Laar model, 257–258               --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
             284–292                          summary of recommended methods,   Vapor, 200
          RK and PR EOS parameters, 289–292      326                            Vapor-liquid equilibria, 251–253, 265–276
          virial coefficients, 287–288         use of sound velocity, 284–292      equilibrium ratios, 269–276
         Specific energy, units, 22            vapor-liquid equilibria, 265–276    formation of relations, 265–266
         Specific gravity, 11                Thermodynamic property, 199           Raoult’s law, 265–266
          comparison of distribution models,  Time, units, 18–19                  solubility of gases in liquids, 266–269
             178–179                        Toluene, effect on asphaltene precipitation,  Vapor-liquid equilibrium calculations,
          definition, 31                          377–378                             367–373
          estimation, 117                   Tortuosity, 350–351                   bubble and dew point calculations,
          hydrocarbon-plus fractions, 173   Transport properties, 329–362            370–372
          hydrocarbons, temperature effect, 301  diffusion coefficients, 345–351   gas-to-oil ratio, 368–370
          petroleum fractions, 93             diffusivity at low pressures        P-T Diagrams, 372–373
          prediction, pure hydrocarbons, 58–60  gases, 346–347                  Vapor liquid ratio, volatility index and, 133
          units, 21                             liquids, 347–348                Vapor-liquid-solid equilibrium-solid
         Specific volume, units, 20            diffusivity of gases and liquids at high  precipitation, 373–385
         Spectrometric methods, 98               pressures, 348–350               heavy compounds, 373–378
         Speed of light in vacuum, 24         interrelationship, 351–354          wax precipitation
         Splitting scheme, petroleum fractions,  measurement of diffusion coefficients in  multisolid-phase model, 382–385
             184–186                             reservoir fluids, 354–356          solid solution model, 378, 380–382
         Square-Well potential, 202           nomenclature, 329–330             Vapor pressure, 11, 200, 305–316
         Standing-Katz chart, 215–216         surface/interfacial tension, 356–361  Antoine coefficients, 310
         Stiel-Thodos method, 341             thermal conductivity, 339–345       definition, 33
         Stokes-Einstein equation, 349        viscosity, 331–338                  petroleum fractions, 312–314
         Sublimation, 314                   Triple point pressure, 199            predictive methods, 306–312
         Sublimation curve, 200             Triple point temperature, 199         pure components, 305–306
         Sublimation line, 251              Trouton’s rule, 322                   pure compounds, coefficients, 308–309
         Sublimation pressure, 315          True boiling point, distillation curve, 182  solids, 314–316
         Sulfur                             True critical properties, 372–373   Vapor pressure method, 94
          crude oil content, 191–192        Tsonopoulos correlations, 62        Vapor-solid equilibrium, 388–390
          in natural gas, 5                 Two petroleum fractions, enthalpy,  Vignes method, 347
          prediction in petroleum fractions,     316–317                        Virial coefficients, velocity of sound data,
             129–130                        Twu method, 61–62, 80                    287–288















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