Datasets
-
Mass fraction
-
η - Viscosity, Pa*s
-
Molar enthalpy
-
ρl - Mass density, kg/m3 (5)
-
csound,fluid - Speed of Sound, m/s (2)
-
γ - Surface tension liquid-gas, N/m
-
Binary diffusion coefficient, m2/s
Mass fraction of L-Phenylalanine (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Temperature, K - Liquid |
Mass fraction of L-Phenylalanine (1) - Liquid |
| 283.15 |
0.0254 |
| 293.15 |
0.0281 |
| 298.15 |
0.0297 |
| 303.15 |
0.0322 |
| 313.15 |
0.0365 |
| 318.15 |
0.0417 |
| 323.15 |
0.0443 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Viscosity, Pa*s - Liquid |
| 298.15 |
0.0000 |
0.0009 |
| 298.15 |
0.0249 |
0.0009 |
| 298.15 |
0.0498 |
0.0009 |
| 298.15 |
0.0749 |
0.0009 |
| 298.15 |
0.0999 |
0.0009 |
| 298.15 |
0.1250 |
0.0010 |
| 298.15 |
0.1499 |
0.0010 |
| 303.15 |
0.0000 |
0.0008 |
| 303.15 |
0.0249 |
0.0008 |
| 303.15 |
0.0498 |
0.0008 |
| 303.15 |
0.0749 |
0.0008 |
| 303.15 |
0.0999 |
0.0008 |
| 303.15 |
0.1250 |
0.0009 |
| 303.15 |
0.1499 |
0.0009 |
| 308.15 |
0.0000 |
0.0007 |
| 308.15 |
0.0249 |
0.0007 |
| 308.15 |
0.0498 |
0.0007 |
| 308.15 |
0.0749 |
0.0007 |
| 308.15 |
0.0999 |
0.0008 |
| 308.15 |
0.1250 |
0.0008 |
| 308.15 |
0.1499 |
0.0008 |
| 313.15 |
0.0000 |
0.0007 |
| 313.15 |
0.0249 |
0.0007 |
| 313.15 |
0.0498 |
0.0007 |
| 313.15 |
0.0749 |
0.0007 |
| 313.15 |
0.0999 |
0.0007 |
| 313.15 |
0.1250 |
0.0007 |
| 313.15 |
0.1499 |
0.0007 |
| 318.15 |
0.0000 |
0.0006 |
| 318.15 |
0.0249 |
0.0006 |
| 318.15 |
0.0498 |
0.0006 |
| 318.15 |
0.0749 |
0.0006 |
| 318.15 |
0.0999 |
0.0006 |
| 318.15 |
0.1250 |
0.0006 |
| 318.15 |
0.1499 |
0.0006 |
Molar enthalpy of dilution, kJ/mol
[ref]
| Fixed |
Measured |
| Initial molality of solute, mol/kg - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.0016 |
298.15 |
101.00 |
0.0008 |
0.7500 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 283.15 |
0.0102 |
1000.19 |
| 283.15 |
0.0203 |
1000.64 |
| 283.15 |
0.0293 |
1001.05 |
| 283.15 |
0.0398 |
1001.53 |
| 283.15 |
0.0509 |
1002.02 |
| 283.15 |
0.0606 |
1002.47 |
| 283.15 |
0.0610 |
1002.49 |
| 283.15 |
0.0736 |
1003.05 |
| 283.15 |
0.0915 |
1003.87 |
| 283.15 |
0.1028 |
1004.36 |
| 288.15 |
0.0102 |
999.59 |
| 288.15 |
0.0203 |
1000.04 |
| 288.15 |
0.0293 |
1000.44 |
| 288.15 |
0.0398 |
1000.91 |
| 288.15 |
0.0509 |
1001.39 |
| 288.15 |
0.0606 |
1001.83 |
| 288.15 |
0.0610 |
1001.85 |
| 288.15 |
0.0736 |
1002.4 |
| 288.15 |
0.0915 |
1003.2 |
| 288.15 |
0.1028 |
1003.69 |
| 293.15 |
0.0102 |
998.69 |
| 293.15 |
0.0203 |
999.13 |
| 293.15 |
0.0293 |
999.52 |
| 293.15 |
0.0398 |
999.98 |
| 293.15 |
0.0509 |
1000.46 |
| 293.15 |
0.0606 |
1000.9 |
| 293.15 |
0.0610 |
1000.91 |
| 293.15 |
0.0736 |
1001.45 |
| 293.15 |
0.0915 |
1002.24 |
| 293.15 |
0.1028 |
1002.73 |
| 298.15 |
0.0102 |
997.52 |
| 298.15 |
0.0203 |
997.95 |
| 298.15 |
0.0293 |
998.35 |
| 298.15 |
0.0398 |
998.8 |
| 298.15 |
0.0509 |
999.27 |
| 298.15 |
0.0606 |
999.7 |
| 298.15 |
0.0610 |
999.71 |
| 298.15 |
0.0736 |
1000.25 |
| 298.15 |
0.0915 |
1001.03 |
| 298.15 |
0.1028 |
1001.5 |
| 303.15 |
0.0102 |
996.12 |
| 303.15 |
0.0203 |
996.54 |
| 303.15 |
0.0293 |
996.93 |
| 303.15 |
0.0398 |
997.38 |
| 303.15 |
0.0509 |
997.85 |
| 303.15 |
0.0606 |
998.27 |
| 303.15 |
0.0610 |
998.28 |
| 303.15 |
0.0736 |
998.81 |
| 303.15 |
0.0915 |
999.58 |
| 303.15 |
0.1028 |
1000.05 |
| 283.15 |
0.0000 |
999.72 |
| 288.15 |
0.0000 |
999.14 |
| 293.15 |
0.0000 |
998.24 |
| 298.15 |
0.0000 |
997.08 |
| 303.15 |
0.0000 |
995.68 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 293.15 |
0.0000 |
998.24 |
| 293.15 |
0.0249 |
999.4 |
| 293.15 |
0.0498 |
1000.55 |
| 293.15 |
0.0749 |
1001.71 |
| 293.15 |
0.0999 |
1002.88 |
| 293.15 |
0.1250 |
1004.04 |
| 293.15 |
0.1499 |
1005.2 |
| 298.15 |
0.0000 |
997.07 |
| 298.15 |
0.0249 |
998.23 |
| 298.15 |
0.0498 |
999.39 |
| 298.15 |
0.0749 |
1000.55 |
| 298.15 |
0.0999 |
1001.72 |
| 298.15 |
0.1250 |
1002.88 |
| 298.15 |
0.1499 |
1004.05 |
| 303.15 |
0.0000 |
995.68 |
| 303.15 |
0.0249 |
996.84 |
| 303.15 |
0.0498 |
998.0 |
| 303.15 |
0.0749 |
999.17 |
| 303.15 |
0.0999 |
1000.34 |
| 303.15 |
0.1250 |
1001.51 |
| 303.15 |
0.1499 |
1002.68 |
| 308.15 |
0.0000 |
994.07 |
| 308.15 |
0.0249 |
995.24 |
| 308.15 |
0.0498 |
996.4 |
| 308.15 |
0.0749 |
997.58 |
| 308.15 |
0.0999 |
998.75 |
| 308.15 |
0.1250 |
999.92 |
| 308.15 |
0.1499 |
1001.09 |
| 313.15 |
0.0000 |
992.25 |
| 313.15 |
0.0249 |
993.43 |
| 313.15 |
0.0498 |
994.6 |
| 313.15 |
0.0749 |
995.78 |
| 313.15 |
0.0999 |
996.96 |
| 313.15 |
0.1250 |
998.14 |
| 313.15 |
0.1499 |
999.32 |
| 318.15 |
0.0000 |
990.24 |
| 318.15 |
0.0249 |
991.43 |
| 318.15 |
0.0498 |
992.61 |
| 318.15 |
0.0749 |
993.8 |
| 318.15 |
0.0999 |
994.98 |
| 318.15 |
0.1250 |
996.17 |
| 318.15 |
0.1499 |
997.36 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 283.15 |
0.0036 |
999.87 |
| 282.65 |
0.0036 |
999.913 |
| 282.15 |
0.0036 |
999.952 |
| 281.65 |
0.0036 |
999.986 |
| 281.15 |
0.0036 |
1000.02 |
| 280.65 |
0.0036 |
1000.045 |
| 280.15 |
0.0036 |
1000.071 |
| 279.65 |
0.0036 |
1000.094 |
| 279.15 |
0.0036 |
1000.11 |
| 278.65 |
0.0036 |
1000.124 |
| 278.15 |
0.0036 |
1000.133 |
| 277.65 |
0.0036 |
1000.141 |
| 277.15 |
0.0036 |
1000.143 |
| 276.65 |
0.0036 |
1000.14 |
| 276.15 |
0.0036 |
1000.137 |
| 275.65 |
0.0036 |
1000.129 |
| 275.15 |
0.0036 |
1000.115 |
| 274.65 |
0.0036 |
1000.095 |
| 274.15 |
0.0036 |
1000.075 |
| 273.65 |
0.0036 |
1000.049 |
| 283.15 |
0.0110 |
1000.209 |
| 282.65 |
0.0110 |
1000.251 |
| 282.15 |
0.0110 |
1000.291 |
| 281.65 |
0.0110 |
1000.326 |
| 281.15 |
0.0110 |
1000.359 |
| 280.65 |
0.0110 |
1000.388 |
| 280.15 |
0.0110 |
1000.412 |
| 279.65 |
0.0110 |
1000.434 |
| 279.15 |
0.0110 |
1000.452 |
| 278.65 |
0.0110 |
1000.467 |
| 278.15 |
0.0110 |
1000.478 |
| 277.65 |
0.0110 |
1000.487 |
| 277.15 |
0.0110 |
1000.49 |
| 276.65 |
0.0110 |
1000.489 |
| 276.15 |
0.0110 |
1000.486 |
| 275.65 |
0.0110 |
1000.478 |
| 275.15 |
0.0110 |
1000.464 |
| 274.65 |
0.0110 |
1000.446 |
| 274.15 |
0.0110 |
1000.425 |
| 273.65 |
0.0110 |
1000.402 |
| 283.15 |
0.0183 |
1000.543 |
| 282.65 |
0.0183 |
1000.586 |
| 282.15 |
0.0183 |
1000.628 |
| 281.65 |
0.0183 |
1000.663 |
| 281.15 |
0.0183 |
1000.697 |
| 280.65 |
0.0183 |
1000.725 |
| 280.15 |
0.0183 |
1000.751 |
| 279.65 |
0.0183 |
1000.773 |
| 279.15 |
0.0183 |
1000.793 |
| 278.65 |
0.0183 |
1000.81 |
| 278.15 |
0.0183 |
1000.82 |
| 277.65 |
0.0183 |
1000.829 |
| 277.15 |
0.0183 |
1000.831 |
| 276.65 |
0.0183 |
1000.833 |
| 276.15 |
0.0183 |
1000.831 |
| 275.65 |
0.0183 |
1000.82 |
| 275.15 |
0.0183 |
1000.809 |
| 274.65 |
0.0183 |
1000.793 |
| 274.15 |
0.0183 |
1000.772 |
| 273.65 |
0.0183 |
1000.75 |
| 283.15 |
0.0330 |
1001.205 |
| 282.65 |
0.0330 |
1001.25 |
| 282.15 |
0.0330 |
1001.292 |
| 281.65 |
0.0330 |
1001.327 |
| 281.15 |
0.0330 |
1001.364 |
| 280.65 |
0.0330 |
1001.394 |
| 280.15 |
0.0330 |
1001.42 |
| 279.65 |
0.0330 |
1001.445 |
| 279.15 |
0.0330 |
1001.466 |
| 278.65 |
0.0330 |
1001.483 |
| 278.15 |
0.0330 |
1001.494 |
| 277.65 |
0.0330 |
1001.504 |
| 277.15 |
0.0330 |
1001.509 |
| 276.65 |
0.0330 |
1001.512 |
| 276.15 |
0.0330 |
1001.511 |
| 275.65 |
0.0330 |
1001.503 |
| 275.15 |
0.0330 |
1001.494 |
| 274.65 |
0.0330 |
1001.478 |
| 274.15 |
0.0330 |
1001.459 |
| 273.65 |
0.0330 |
1001.438 |
| 283.15 |
0.0443 |
1001.773 |
| 282.65 |
0.0443 |
1001.818 |
| 282.15 |
0.0443 |
1001.858 |
| 281.65 |
0.0443 |
1001.898 |
| 281.15 |
0.0443 |
1001.934 |
| 280.65 |
0.0443 |
1001.963 |
| 280.15 |
0.0443 |
1001.991 |
| 279.65 |
0.0443 |
1002.017 |
| 279.15 |
0.0443 |
1002.038 |
| 278.65 |
0.0443 |
1002.055 |
| 278.15 |
0.0443 |
1002.069 |
| 277.65 |
0.0443 |
1002.08 |
| 277.15 |
0.0443 |
1002.086 |
| 276.65 |
0.0443 |
1002.087 |
| 276.15 |
0.0443 |
1002.089 |
| 275.65 |
0.0443 |
1002.082 |
| 275.15 |
0.0443 |
1002.074 |
| 274.65 |
0.0443 |
1002.058 |
| 274.15 |
0.0443 |
1002.042 |
| 273.65 |
0.0443 |
1002.019 |
| 283.15 |
0.0536 |
1002.147 |
| 282.65 |
0.0536 |
1002.193 |
| 282.15 |
0.0536 |
1002.238 |
| 281.65 |
0.0536 |
1002.276 |
| 281.15 |
0.0536 |
1002.313 |
| 280.65 |
0.0536 |
1002.345 |
| 280.15 |
0.0536 |
1002.373 |
| 279.65 |
0.0536 |
1002.4 |
| 279.15 |
0.0536 |
1002.422 |
| 278.65 |
0.0536 |
1002.44 |
| 278.15 |
0.0536 |
1002.456 |
| 277.65 |
0.0536 |
1002.468 |
| 277.15 |
0.0536 |
1002.474 |
| 276.65 |
0.0536 |
1002.478 |
| 276.15 |
0.0536 |
1002.479 |
| 275.65 |
0.0536 |
1002.476 |
| 275.15 |
0.0536 |
1002.467 |
| 274.65 |
0.0536 |
1002.455 |
| 274.15 |
0.0536 |
1002.438 |
| 273.65 |
0.0536 |
1002.419 |
| 283.15 |
0.0623 |
1002.551 |
| 282.65 |
0.0623 |
1002.598 |
| 282.15 |
0.0623 |
1002.643 |
| 281.65 |
0.0623 |
1002.682 |
| 281.15 |
0.0623 |
1002.72 |
| 280.65 |
0.0623 |
1002.752 |
| 280.15 |
0.0623 |
1002.782 |
| 279.65 |
0.0623 |
1002.81 |
| 279.15 |
0.0623 |
1002.833 |
| 278.65 |
0.0623 |
1002.853 |
| 278.15 |
0.0623 |
1002.868 |
| 277.65 |
0.0623 |
1002.88 |
| 277.15 |
0.0623 |
1002.888 |
| 276.65 |
0.0623 |
1002.892 |
| 276.15 |
0.0623 |
1002.894 |
| 275.65 |
0.0623 |
1002.892 |
| 275.15 |
0.0623 |
1002.883 |
| 274.65 |
0.0623 |
1002.873 |
| 274.15 |
0.0623 |
1002.857 |
| 273.65 |
0.0623 |
1002.838 |
| 283.15 |
0.0740 |
1003.079 |
| 282.65 |
0.0740 |
1003.127 |
| 282.15 |
0.0740 |
1003.171 |
| 281.65 |
0.0740 |
1003.212 |
| 281.15 |
0.0740 |
1003.252 |
| 280.65 |
0.0740 |
1003.283 |
| 280.15 |
0.0740 |
1003.316 |
| 279.65 |
0.0740 |
1003.342 |
| 279.15 |
0.0740 |
1003.367 |
| 278.65 |
0.0740 |
1003.387 |
| 278.15 |
0.0740 |
1003.407 |
| 277.65 |
0.0740 |
1003.419 |
| 277.15 |
0.0740 |
1003.428 |
| 276.65 |
0.0740 |
1003.433 |
| 276.15 |
0.0740 |
1003.435 |
| 275.65 |
0.0740 |
1003.434 |
| 275.15 |
0.0740 |
1003.428 |
| 274.65 |
0.0740 |
1003.417 |
| 274.15 |
0.0740 |
1003.402 |
| 273.65 |
0.0740 |
1003.385 |
| 283.15 |
0.0855 |
1003.626 |
| 282.65 |
0.0855 |
1003.674 |
| 282.15 |
0.0855 |
1003.719 |
| 281.65 |
0.0855 |
1003.761 |
| 281.15 |
0.0855 |
1003.8 |
| 280.65 |
0.0855 |
1003.833 |
| 280.15 |
0.0855 |
1003.865 |
| 279.65 |
0.0855 |
1003.895 |
| 279.15 |
0.0855 |
1003.919 |
| 278.65 |
0.0855 |
1003.941 |
| 278.15 |
0.0855 |
1003.958 |
| 277.65 |
0.0855 |
1003.973 |
| 277.15 |
0.0855 |
1003.983 |
| 276.65 |
0.0855 |
1003.989 |
| 276.15 |
0.0855 |
1003.996 |
| 275.65 |
0.0855 |
1003.994 |
| 275.15 |
0.0855 |
1003.987 |
| 274.65 |
0.0855 |
1003.976 |
| 274.15 |
0.0855 |
1003.964 |
| 273.65 |
0.0855 |
1003.95 |
| 283.15 |
0.0981 |
1004.21 |
| 282.65 |
0.0981 |
1004.26 |
| 282.15 |
0.0981 |
1004.307 |
| 281.65 |
0.0981 |
1004.348 |
| 281.15 |
0.0981 |
1004.39 |
| 280.65 |
0.0981 |
1004.426 |
| 280.15 |
0.0981 |
1004.458 |
| 279.65 |
0.0981 |
1004.489 |
| 279.15 |
0.0981 |
1004.515 |
| 278.65 |
0.0981 |
1004.54 |
| 278.15 |
0.0981 |
1004.559 |
| 277.65 |
0.0981 |
1004.574 |
| 277.15 |
0.0981 |
1004.587 |
| 276.65 |
0.0981 |
1004.594 |
| 276.15 |
0.0981 |
1004.599 |
| 275.65 |
0.0981 |
1004.601 |
| 275.15 |
0.0981 |
1004.597 |
| 274.65 |
0.0981 |
1004.589 |
| 274.15 |
0.0981 |
1004.579 |
| 273.65 |
0.0981 |
1004.562 |
| 283.15 |
0.1158 |
1005.056 |
| 282.65 |
0.1158 |
1005.106 |
| 282.15 |
0.1158 |
1005.156 |
| 281.65 |
0.1158 |
1005.2 |
| 281.15 |
0.1158 |
1005.242 |
| 280.65 |
0.1158 |
1005.281 |
| 280.15 |
0.1158 |
1005.315 |
| 279.65 |
0.1158 |
1005.347 |
| 279.15 |
0.1158 |
1005.375 |
| 278.65 |
0.1158 |
1005.399 |
| 278.15 |
0.1158 |
1005.419 |
| 277.65 |
0.1158 |
1005.438 |
| 277.15 |
0.1158 |
1005.45 |
| 276.65 |
0.1158 |
1005.46 |
| 276.15 |
0.1158 |
1005.468 |
| 275.65 |
0.1158 |
1005.472 |
| 275.15 |
0.1158 |
1005.469 |
| 274.65 |
0.1158 |
1005.465 |
| 274.15 |
0.1158 |
1005.455 |
| 273.65 |
0.1158 |
1005.443 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0155 |
997.721 |
| 0.0210 |
997.961 |
| 0.0298 |
998.343 |
| 0.0337 |
998.516 |
| 0.0462 |
999.058 |
| 0.0530 |
999.349 |
| 0.0583 |
999.577 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 293.15 |
0.0000 |
998.219 |
| 293.15 |
0.0192 |
999.09 |
| 293.15 |
0.0461 |
1000.308 |
| 293.15 |
0.0687 |
1001.319 |
| 293.15 |
0.0753 |
1001.611 |
| 293.15 |
0.0856 |
1002.07 |
| 293.15 |
0.1047 |
1002.911 |
| 298.15 |
0.0000 |
997.05 |
| 298.15 |
0.0192 |
997.908 |
| 298.15 |
0.0461 |
999.107 |
| 298.15 |
0.0687 |
1000.103 |
| 298.15 |
0.0753 |
1000.391 |
| 298.15 |
0.0856 |
1000.844 |
| 298.15 |
0.1047 |
1001.671 |
| 303.15 |
0.0000 |
995.645 |
| 303.15 |
0.0192 |
996.494 |
| 303.15 |
0.0461 |
997.681 |
| 303.15 |
0.0687 |
998.668 |
| 303.15 |
0.0753 |
998.953 |
| 303.15 |
0.0856 |
999.401 |
| 303.15 |
0.1047 |
1000.223 |
| 308.15 |
0.0000 |
994.02 |
| 308.15 |
0.0192 |
994.857 |
| 308.15 |
0.0461 |
996.027 |
| 308.15 |
0.0687 |
996.999 |
| 308.15 |
0.0753 |
997.28 |
| 308.15 |
0.0856 |
997.722 |
| 308.15 |
0.1047 |
998.531 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Frequency, MHz = 3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Speed of sound, m/s - Liquid |
| 293.15 |
0.0000 |
1483.6 |
| 293.15 |
0.0249 |
1488.8 |
| 293.15 |
0.0498 |
1493.0 |
| 293.15 |
0.0749 |
1496.2 |
| 293.15 |
0.0999 |
1498.3 |
| 293.15 |
0.1250 |
1499.4 |
| 293.15 |
0.1499 |
1499.4 |
| 298.15 |
0.0000 |
1496.9 |
| 298.15 |
0.0249 |
1501.9 |
| 298.15 |
0.0498 |
1505.9 |
| 298.15 |
0.0749 |
1509.0 |
| 298.15 |
0.0999 |
1511.0 |
| 298.15 |
0.1250 |
1512.0 |
| 298.15 |
0.1499 |
1511.9 |
| 303.15 |
0.0000 |
1508.4 |
| 303.15 |
0.0249 |
1513.1 |
| 303.15 |
0.0498 |
1516.8 |
| 303.15 |
0.0749 |
1519.5 |
| 303.15 |
0.0999 |
1521.2 |
| 303.15 |
0.1250 |
1521.8 |
| 303.15 |
0.1499 |
1521.3 |
| 308.15 |
0.0000 |
1519.8 |
| 308.15 |
0.0249 |
1524.1 |
| 308.15 |
0.0498 |
1527.4 |
| 308.15 |
0.0749 |
1529.8 |
| 308.15 |
0.0999 |
1531.1 |
| 308.15 |
0.1250 |
1531.4 |
| 308.15 |
0.1499 |
1530.6 |
| 313.15 |
0.0000 |
1526.8 |
| 313.15 |
0.0249 |
1530.8 |
| 313.15 |
0.0498 |
1533.8 |
| 313.15 |
0.0749 |
1535.8 |
| 313.15 |
0.0999 |
1536.8 |
| 313.15 |
0.1250 |
1536.7 |
| 313.15 |
0.1499 |
1535.7 |
| 318.15 |
0.0000 |
1533.0 |
| 318.15 |
0.0249 |
1536.5 |
| 318.15 |
0.0498 |
1539.1 |
| 318.15 |
0.0749 |
1540.8 |
| 318.15 |
0.0999 |
1541.5 |
| 318.15 |
0.1250 |
1541.3 |
| 318.15 |
0.1499 |
1540.0 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Speed of sound, m/s - Liquid |
| 293.15 |
0.0000 |
1482.98 |
| 293.15 |
0.0192 |
1485.3 |
| 293.15 |
0.0461 |
1488.56 |
| 293.15 |
0.0687 |
1491.3 |
| 293.15 |
0.0753 |
1492.08 |
| 293.15 |
0.0856 |
1493.33 |
| 293.15 |
0.1047 |
1495.63 |
| 298.15 |
0.0000 |
1497.2 |
| 298.15 |
0.0192 |
1499.39 |
| 298.15 |
0.0461 |
1502.47 |
| 298.15 |
0.0687 |
1505.05 |
| 298.15 |
0.0753 |
1505.78 |
| 298.15 |
0.0856 |
1506.95 |
| 298.15 |
0.1047 |
1509.09 |
| 303.15 |
0.0000 |
1509.46 |
| 303.15 |
0.0192 |
1511.52 |
| 303.15 |
0.0461 |
1514.42 |
| 303.15 |
0.0687 |
1516.85 |
| 303.15 |
0.0753 |
1517.54 |
| 303.15 |
0.0856 |
1518.62 |
| 303.15 |
0.1047 |
1520.65 |
| 308.15 |
0.0000 |
1519.91 |
| 308.15 |
0.0192 |
1521.85 |
| 308.15 |
0.0461 |
1524.58 |
| 308.15 |
0.0687 |
1526.87 |
| 308.15 |
0.0753 |
1527.52 |
| 308.15 |
0.0856 |
1528.55 |
| 308.15 |
0.1047 |
1530.46 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Molality, mol/kg of L-Phenylalanine (1) - Liquid |
Temperature, K - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0000 |
293.15 |
0.0727 |
| 0.0505 |
293.15 |
0.0724 |
| 0.0759 |
293.15 |
0.0719 |
| 0.1015 |
293.15 |
0.0710 |
| 0.1273 |
293.15 |
0.0706 |
| 0.1532 |
293.15 |
0.0701 |
| 0.0000 |
298.15 |
0.0720 |
| 0.0505 |
298.15 |
0.0711 |
| 0.0759 |
298.15 |
0.0707 |
| 0.1015 |
298.15 |
0.0697 |
| 0.1273 |
298.15 |
0.0684 |
| 0.1532 |
298.15 |
0.0669 |
| 0.0000 |
303.15 |
0.0712 |
| 0.0505 |
303.15 |
0.0708 |
| 0.0759 |
303.15 |
0.0699 |
| 0.1015 |
303.15 |
0.0685 |
| 0.1273 |
303.15 |
0.0666 |
| 0.1532 |
303.15 |
0.0645 |
| 0.0000 |
308.15 |
0.0704 |
| 0.0505 |
308.15 |
0.0700 |
| 0.0759 |
308.15 |
0.0690 |
| 0.1015 |
308.15 |
0.0666 |
| 0.1273 |
308.15 |
0.0652 |
| 0.1532 |
308.15 |
0.0634 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
| 298.20 |
0.0000 |
| 303.20 |
0.0000 |
| 313.20 |
0.0000 |
Sources
Note: These property values are available through the Cheméo API. A free account gives you an access key.