Datasets
-
Osmotic coefficient (2)
-
Molar enthalpy (2)
-
Eutectic temperature, K (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (6)
-
γ - Surface tension liquid-gas, N/m (4)
-
Tfus - Solid-liquid equilibrium temperature, K (4)
Osmotic coefficient
[ref]
Operational conditions:
- Pressure, kPa = 20 (Liquid)
- Temperature, K = 298.1 (Liquid)
| Molality, mol/kg of Butanoic acid (1) - Liquid |
Osmotic coefficient - Liquid |
| 0.2966 |
1.0514 |
| 0.3972 |
1.033 |
| 0.7027 |
0.9809 |
| 0.9898 |
0.9364 |
| 1.5391 |
0.8612 |
| 2.5005 |
0.7547 |
| 2.6522 |
0.7403 |
| 4.544 |
0.5981 |
| 5.3528 |
0.5533 |
| 6.3643 |
0.5064 |
| 7.7774 |
0.4537 |
| 9.5981 |
0.4015 |
| 11.9952 |
0.3508 |
| 15.2898 |
0.3019 |
| 17.5977 |
0.2780 |
Osmotic coefficient
[ref]
Operational conditions:
- Pressure, kPa = 20 (Liquid)
- Temperature, K = 298.1 (Liquid)
| Molality, mol/kg of Butanoic acid (1) - Liquid |
Osmotic coefficient - Liquid |
| 0.2966 |
1.0514 |
| 0.3972 |
1.033 |
| 0.7027 |
0.9809 |
| 0.9898 |
0.9364 |
| 1.5391 |
0.8612 |
| 2.5005 |
0.7547 |
| 2.6522 |
0.7403 |
| 4.544 |
0.5981 |
| 5.3528 |
0.5533 |
| 6.3643 |
0.5064 |
| 7.7774 |
0.4537 |
| 9.5981 |
0.4015 |
| 11.9952 |
0.3508 |
| 15.2898 |
0.3019 |
| 17.5977 |
0.2780 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
| 293.15 |
0.8641 |
0.4494 |
-0.5037 |
| 293.15 |
1.1245 |
0.5799 |
-0.6725 |
| 293.15 |
1.645 |
0.8340 |
-0.9279 |
| 293.15 |
2.1366 |
1.0665 |
-1.0655 |
| 293.15 |
2.5106 |
1.2385 |
-1.0078 |
| 293.15 |
2.6387 |
1.2965 |
-0.9692 |
| 293.15 |
3.6188 |
1.7253 |
-0.7210 |
| 293.15 |
3.9851 |
1.8791 |
-0.6363 |
| 293.15 |
4.6798 |
2.1617 |
-0.4527 |
| 293.15 |
4.8952 |
2.247 |
-0.4016 |
| 293.15 |
5.2893 |
2.4004 |
-0.3123 |
| 293.15 |
5.6397 |
2.5339 |
-0.2323 |
| 298.15 |
0.8641 |
0.4494 |
-0.4831 |
| 298.15 |
1.1245 |
0.5799 |
-0.6480 |
| 298.15 |
1.645 |
0.8340 |
-0.9101 |
| 298.15 |
2.1366 |
1.0665 |
-1.0273 |
| 298.15 |
2.5106 |
1.2385 |
-0.9657 |
| 298.15 |
2.6387 |
1.2965 |
-0.9271 |
| 298.15 |
3.6188 |
1.7253 |
-0.6547 |
| 298.15 |
3.9851 |
1.8791 |
-0.5675 |
| 298.15 |
4.6798 |
2.1617 |
-0.4026 |
| 298.15 |
4.8952 |
2.247 |
-0.3585 |
| 298.15 |
5.2893 |
2.4004 |
-0.2837 |
| 298.15 |
5.6397 |
2.5339 |
-0.2195 |
| 303.15 |
0.8641 |
0.4494 |
-0.4653 |
| 303.15 |
1.1245 |
0.5799 |
-0.6267 |
| 303.15 |
1.645 |
0.8340 |
-0.8947 |
| 303.15 |
2.1366 |
1.0665 |
-0.9940 |
| 303.15 |
2.5106 |
1.2385 |
-0.9290 |
| 303.15 |
2.6387 |
1.2965 |
-0.8904 |
| 303.15 |
3.6188 |
1.7253 |
-0.5969 |
| 303.15 |
3.9851 |
1.8791 |
-0.5075 |
| 303.15 |
4.6798 |
2.1617 |
-0.3589 |
| 303.15 |
4.8952 |
2.247 |
-0.3210 |
| 303.15 |
5.2893 |
2.4004 |
-0.2589 |
| 303.15 |
5.6397 |
2.5339 |
-0.2083 |
| 308.15 |
0.8641 |
0.4494 |
-0.4435 |
| 308.15 |
1.1245 |
0.5799 |
-0.6006 |
| 308.15 |
1.645 |
0.8340 |
-0.8757 |
| 308.15 |
2.1366 |
1.0665 |
-0.9532 |
| 308.15 |
2.5106 |
1.2385 |
-0.8841 |
| 308.15 |
2.6387 |
1.2965 |
-0.8455 |
| 308.15 |
3.6188 |
1.7253 |
-0.5263 |
| 308.15 |
3.9851 |
1.8791 |
-0.4343 |
| 308.15 |
4.6798 |
2.1617 |
-0.3055 |
| 308.15 |
4.8952 |
2.247 |
-0.2752 |
| 308.15 |
5.2893 |
2.4004 |
-0.2285 |
| 308.15 |
5.6397 |
2.5339 |
-0.1946 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
| 293.15 |
0.8641 |
0.4494 |
-0.5037 |
| 293.15 |
1.1245 |
0.5799 |
-0.6725 |
| 293.15 |
1.645 |
0.8340 |
-0.9279 |
| 293.15 |
2.1366 |
1.0665 |
-1.0655 |
| 293.15 |
2.5106 |
1.2385 |
-1.0078 |
| 293.15 |
2.6387 |
1.2965 |
-0.9692 |
| 293.15 |
3.6188 |
1.7253 |
-0.7210 |
| 293.15 |
3.9851 |
1.8791 |
-0.6363 |
| 293.15 |
4.6798 |
2.1617 |
-0.4527 |
| 293.15 |
4.8952 |
2.247 |
-0.4016 |
| 293.15 |
5.2893 |
2.4004 |
-0.3123 |
| 293.15 |
5.6397 |
2.5339 |
-0.2323 |
| 298.15 |
0.8641 |
0.4494 |
-0.4831 |
| 298.15 |
1.1245 |
0.5799 |
-0.6480 |
| 298.15 |
1.645 |
0.8340 |
-0.9101 |
| 298.15 |
2.1366 |
1.0665 |
-1.0273 |
| 298.15 |
2.5106 |
1.2385 |
-0.9657 |
| 298.15 |
2.6387 |
1.2965 |
-0.9271 |
| 298.15 |
3.6188 |
1.7253 |
-0.6547 |
| 298.15 |
3.9851 |
1.8791 |
-0.5675 |
| 298.15 |
4.6798 |
2.1617 |
-0.4026 |
| 298.15 |
4.8952 |
2.247 |
-0.3585 |
| 298.15 |
5.2893 |
2.4004 |
-0.2837 |
| 298.15 |
5.6397 |
2.5339 |
-0.2195 |
| 303.15 |
0.8641 |
0.4494 |
-0.4653 |
| 303.15 |
1.1245 |
0.5799 |
-0.6267 |
| 303.15 |
1.645 |
0.8340 |
-0.8947 |
| 303.15 |
2.1366 |
1.0665 |
-0.9940 |
| 303.15 |
2.5106 |
1.2385 |
-0.9290 |
| 303.15 |
2.6387 |
1.2965 |
-0.8904 |
| 303.15 |
3.6188 |
1.7253 |
-0.5969 |
| 303.15 |
3.9851 |
1.8791 |
-0.5075 |
| 303.15 |
4.6798 |
2.1617 |
-0.3589 |
| 303.15 |
4.8952 |
2.247 |
-0.3210 |
| 303.15 |
5.2893 |
2.4004 |
-0.2589 |
| 303.15 |
5.6397 |
2.5339 |
-0.2083 |
| 308.15 |
0.8641 |
0.4494 |
-0.4435 |
| 308.15 |
1.1245 |
0.5799 |
-0.6006 |
| 308.15 |
1.645 |
0.8340 |
-0.8757 |
| 308.15 |
2.1366 |
1.0665 |
-0.9532 |
| 308.15 |
2.5106 |
1.2385 |
-0.8841 |
| 308.15 |
2.6387 |
1.2965 |
-0.8455 |
| 308.15 |
3.6188 |
1.7253 |
-0.5263 |
| 308.15 |
3.9851 |
1.8791 |
-0.4343 |
| 308.15 |
4.6798 |
2.1617 |
-0.3055 |
| 308.15 |
4.8952 |
2.247 |
-0.2752 |
| 308.15 |
5.2893 |
2.4004 |
-0.2285 |
| 308.15 |
5.6397 |
2.5339 |
-0.1946 |
Eutectic temperature, K
[ref]
| Eutectic temperature, K - Liquid |
| 259.83 |
Eutectic temperature, K
[ref]
| Eutectic temperature, K - Liquid |
| 259.83 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.3326 |
| 0.0001 |
1.3326 |
| 0.0006 |
1.3328 |
| 0.0016 |
1.3333 |
| 0.0056 |
1.3351 |
| 0.0136 |
1.3388 |
| 0.0201 |
1.3406 |
| 0.0299 |
1.3451 |
| 0.0480 |
1.3506 |
| 0.0596 |
1.3536 |
| 0.0865 |
1.3596 |
| 0.1034 |
1.3628 |
| 0.2033 |
1.3769 |
| 0.2997 |
1.3852 |
| 0.3810 |
1.3892 |
| 0.5038 |
1.3933 |
| 0.5763 |
1.3947 |
| 0.7036 |
1.3962 |
| 0.8019 |
1.3967 |
| 0.9189 |
1.3965 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.3326 |
| 0.0001 |
1.3326 |
| 0.0006 |
1.3328 |
| 0.0016 |
1.3333 |
| 0.0056 |
1.3351 |
| 0.0136 |
1.3388 |
| 0.0201 |
1.3406 |
| 0.0299 |
1.3451 |
| 0.0480 |
1.3506 |
| 0.0596 |
1.3536 |
| 0.0865 |
1.3596 |
| 0.1034 |
1.3628 |
| 0.2033 |
1.3769 |
| 0.2997 |
1.3852 |
| 0.3810 |
1.3892 |
| 0.5038 |
1.3933 |
| 0.5763 |
1.3947 |
| 0.7036 |
1.3962 |
| 0.8019 |
1.3967 |
| 0.9189 |
1.3965 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mass fraction of Butanoic acid (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
997.04 |
| 0.0001 |
997.07 |
| 0.0002 |
997.07 |
| 0.0004 |
997.09 |
| 0.0006 |
997.08 |
| 0.0008 |
997.12 |
| 0.0021 |
997.2 |
| 0.0023 |
997.22 |
| 0.0043 |
997.33 |
| 0.0070 |
997.57 |
| 0.0076 |
997.62 |
| 0.0151 |
998.25 |
| 0.0157 |
998.3 |
| 0.0285 |
999.62 |
| 0.0453 |
1001.89 |
| 0.0508 |
1002.79 |
| 0.0589 |
1004.25 |
| 0.0730 |
1000.5 |
| 0.0870 |
1001.01 |
| 0.0974 |
1014.17 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
997.14 |
| 0.0001 |
997.28 |
| 0.0006 |
997.35 |
| 0.0016 |
997.39 |
| 0.0056 |
998.24 |
| 0.0136 |
999.83 |
| 0.0201 |
1000.84 |
| 0.0299 |
1001.79 |
| 0.0480 |
1001.61 |
| 0.0596 |
1000.55 |
| 0.0865 |
998.76 |
| 0.1034 |
997.68 |
| 0.2033 |
992.5 |
| 0.2997 |
987.71 |
| 0.3810 |
983.12 |
| 0.5038 |
977.2 |
| 0.5763 |
973.62 |
| 0.7036 |
967.47 |
| 0.8019 |
962.35 |
| 0.9189 |
957.18 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Butanoic acid (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 293.15 |
0.0000 |
998.18 |
| 293.15 |
0.0165 |
1002.55 |
| 293.15 |
0.0214 |
1003.38 |
| 293.15 |
0.0335 |
1004.38 |
| 293.15 |
0.0373 |
1004.49 |
| 293.15 |
0.0452 |
1004.3 |
| 293.15 |
0.0500 |
1004.13 |
| 293.15 |
0.0583 |
1003.61 |
| 293.15 |
0.0696 |
1002.83 |
| 293.15 |
0.0772 |
1002.34 |
| 293.15 |
0.0900 |
1001.61 |
| 293.15 |
0.0995 |
1001.12 |
| 293.15 |
0.1172 |
1000.27 |
| 293.15 |
0.1310 |
999.59 |
| 293.15 |
0.1443 |
998.82 |
| 293.15 |
0.1767 |
997.16 |
| 298.15 |
0.0000 |
997.01 |
| 298.15 |
0.0165 |
1000.29 |
| 298.15 |
0.0214 |
1001.03 |
| 298.15 |
0.0335 |
1001.93 |
| 298.15 |
0.0373 |
1001.94 |
| 298.15 |
0.0452 |
1001.66 |
| 298.15 |
0.0500 |
1001.39 |
| 298.15 |
0.0583 |
1000.77 |
| 298.15 |
0.0696 |
999.9 |
| 298.15 |
0.0772 |
999.13 |
| 298.15 |
0.0900 |
998.48 |
| 298.15 |
0.0995 |
997.91 |
| 298.15 |
0.1172 |
996.95 |
| 298.15 |
0.1310 |
996.11 |
| 298.15 |
0.1443 |
995.31 |
| 298.15 |
0.1767 |
993.56 |
| 303.15 |
0.0000 |
995.61 |
| 303.15 |
0.0165 |
998.03 |
| 303.15 |
0.0214 |
998.67 |
| 303.15 |
0.0335 |
999.47 |
| 303.15 |
0.0373 |
999.38 |
| 303.15 |
0.0452 |
999.01 |
| 303.15 |
0.0500 |
998.64 |
| 303.15 |
0.0583 |
997.92 |
| 303.15 |
0.0696 |
996.96 |
| 303.15 |
0.0772 |
995.79 |
| 303.15 |
0.0900 |
995.24 |
| 303.15 |
0.0995 |
994.7 |
| 303.15 |
0.1172 |
993.63 |
| 303.15 |
0.1310 |
992.63 |
| 303.15 |
0.1443 |
991.8 |
| 303.15 |
0.1767 |
989.96 |
| 308.15 |
0.0000 |
994.0 |
| 308.15 |
0.0165 |
995.86 |
| 308.15 |
0.0214 |
996.41 |
| 308.15 |
0.0335 |
997.11 |
| 308.15 |
0.0373 |
996.93 |
| 308.15 |
0.0452 |
996.46 |
| 308.15 |
0.0500 |
995.99 |
| 308.15 |
0.0583 |
995.18 |
| 308.15 |
0.0696 |
994.11 |
| 308.15 |
0.0772 |
992.85 |
| 308.15 |
0.0900 |
991.96 |
| 308.15 |
0.0995 |
991.51 |
| 308.15 |
0.1172 |
990.42 |
| 308.15 |
0.1310 |
989.31 |
| 308.15 |
0.1443 |
988.32 |
| 308.15 |
0.1767 |
986.45 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mass fraction of Butanoic acid (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
997.04 |
| 0.0001 |
997.07 |
| 0.0002 |
997.07 |
| 0.0004 |
997.09 |
| 0.0006 |
997.08 |
| 0.0008 |
997.12 |
| 0.0021 |
997.2 |
| 0.0023 |
997.22 |
| 0.0043 |
997.33 |
| 0.0070 |
997.57 |
| 0.0076 |
997.62 |
| 0.0151 |
998.25 |
| 0.0157 |
998.3 |
| 0.0285 |
999.62 |
| 0.0453 |
1001.89 |
| 0.0508 |
1002.79 |
| 0.0589 |
1004.25 |
| 0.0730 |
1000.5 |
| 0.0870 |
1001.01 |
| 0.0974 |
1014.17 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
997.14 |
| 0.0001 |
997.28 |
| 0.0006 |
997.35 |
| 0.0016 |
997.39 |
| 0.0056 |
998.24 |
| 0.0136 |
999.83 |
| 0.0201 |
1000.84 |
| 0.0299 |
1001.79 |
| 0.0480 |
1001.61 |
| 0.0596 |
1000.55 |
| 0.0865 |
998.76 |
| 0.1034 |
997.68 |
| 0.2033 |
992.5 |
| 0.2997 |
987.71 |
| 0.3810 |
983.12 |
| 0.5038 |
977.2 |
| 0.5763 |
973.62 |
| 0.7036 |
967.47 |
| 0.8019 |
962.35 |
| 0.9189 |
957.18 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Butanoic acid (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 293.15 |
0.0000 |
998.18 |
| 293.15 |
0.0165 |
1002.55 |
| 293.15 |
0.0214 |
1003.38 |
| 293.15 |
0.0335 |
1004.38 |
| 293.15 |
0.0373 |
1004.49 |
| 293.15 |
0.0452 |
1004.3 |
| 293.15 |
0.0500 |
1004.13 |
| 293.15 |
0.0583 |
1003.61 |
| 293.15 |
0.0696 |
1002.83 |
| 293.15 |
0.0772 |
1002.34 |
| 293.15 |
0.0900 |
1001.61 |
| 293.15 |
0.0995 |
1001.12 |
| 293.15 |
0.1172 |
1000.27 |
| 293.15 |
0.1310 |
999.59 |
| 293.15 |
0.1443 |
998.82 |
| 293.15 |
0.1767 |
997.16 |
| 298.15 |
0.0000 |
997.01 |
| 298.15 |
0.0165 |
1000.29 |
| 298.15 |
0.0214 |
1001.03 |
| 298.15 |
0.0335 |
1001.93 |
| 298.15 |
0.0373 |
1001.94 |
| 298.15 |
0.0452 |
1001.66 |
| 298.15 |
0.0500 |
1001.39 |
| 298.15 |
0.0583 |
1000.77 |
| 298.15 |
0.0696 |
999.9 |
| 298.15 |
0.0772 |
999.13 |
| 298.15 |
0.0900 |
998.48 |
| 298.15 |
0.0995 |
997.91 |
| 298.15 |
0.1172 |
996.95 |
| 298.15 |
0.1310 |
996.11 |
| 298.15 |
0.1443 |
995.31 |
| 298.15 |
0.1767 |
993.56 |
| 303.15 |
0.0000 |
995.61 |
| 303.15 |
0.0165 |
998.03 |
| 303.15 |
0.0214 |
998.67 |
| 303.15 |
0.0335 |
999.47 |
| 303.15 |
0.0373 |
999.38 |
| 303.15 |
0.0452 |
999.01 |
| 303.15 |
0.0500 |
998.64 |
| 303.15 |
0.0583 |
997.92 |
| 303.15 |
0.0696 |
996.96 |
| 303.15 |
0.0772 |
995.79 |
| 303.15 |
0.0900 |
995.24 |
| 303.15 |
0.0995 |
994.7 |
| 303.15 |
0.1172 |
993.63 |
| 303.15 |
0.1310 |
992.63 |
| 303.15 |
0.1443 |
991.8 |
| 303.15 |
0.1767 |
989.96 |
| 308.15 |
0.0000 |
994.0 |
| 308.15 |
0.0165 |
995.86 |
| 308.15 |
0.0214 |
996.41 |
| 308.15 |
0.0335 |
997.11 |
| 308.15 |
0.0373 |
996.93 |
| 308.15 |
0.0452 |
996.46 |
| 308.15 |
0.0500 |
995.99 |
| 308.15 |
0.0583 |
995.18 |
| 308.15 |
0.0696 |
994.11 |
| 308.15 |
0.0772 |
992.85 |
| 308.15 |
0.0900 |
991.96 |
| 308.15 |
0.0995 |
991.51 |
| 308.15 |
0.1172 |
990.42 |
| 308.15 |
0.1310 |
989.31 |
| 308.15 |
0.1443 |
988.32 |
| 308.15 |
0.1767 |
986.45 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0000 |
0.0711 |
| 0.0001 |
0.0705 |
| 0.0006 |
0.0663 |
| 0.0016 |
0.0603 |
| 0.0028 |
0.0551 |
| 0.0056 |
0.0463 |
| 0.0075 |
0.0421 |
| 0.0136 |
0.0359 |
| 0.0201 |
0.0319 |
| 0.0299 |
0.0292 |
| 0.0480 |
0.0285 |
| 0.0596 |
0.0284 |
| 0.0865 |
0.0282 |
| 0.1034 |
0.0282 |
| 0.2033 |
0.0279 |
| 0.2997 |
0.0277 |
| 0.3810 |
0.0277 |
| 0.5038 |
0.0276 |
| 0.5763 |
0.0274 |
| 0.7036 |
0.0271 |
| 0.8019 |
0.0269 |
| 0.9189 |
0.0265 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Butanoic acid (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 293.15 |
0.0000 |
0.0726 |
| 293.15 |
0.0047 |
0.0505 |
| 293.15 |
0.0066 |
0.0459 |
| 293.15 |
0.0090 |
0.0416 |
| 293.15 |
0.0100 |
0.0403 |
| 293.15 |
0.0127 |
0.0374 |
| 293.15 |
0.0143 |
0.0361 |
| 293.15 |
0.0165 |
0.0346 |
| 293.15 |
0.0335 |
0.0293 |
| 293.15 |
0.0452 |
0.0285 |
| 293.15 |
0.0583 |
0.0285 |
| 293.15 |
0.0872 |
0.0286 |
| 293.15 |
0.0995 |
0.0285 |
| 293.15 |
0.1147 |
0.0284 |
| 293.15 |
0.1340 |
0.0282 |
| 293.15 |
0.1428 |
0.0282 |
| 293.15 |
0.1767 |
0.0282 |
| 298.15 |
0.0000 |
0.0718 |
| 298.15 |
0.0047 |
0.0500 |
| 298.15 |
0.0066 |
0.0453 |
| 298.15 |
0.0090 |
0.0410 |
| 298.15 |
0.0100 |
0.0397 |
| 298.15 |
0.0127 |
0.0368 |
| 298.15 |
0.0143 |
0.0356 |
| 298.15 |
0.0165 |
0.0342 |
| 298.15 |
0.0335 |
0.0289 |
| 298.15 |
0.0452 |
0.0283 |
| 298.15 |
0.0583 |
0.0284 |
| 298.15 |
0.0872 |
0.0283 |
| 298.15 |
0.0995 |
0.0282 |
| 298.15 |
0.1147 |
0.0282 |
| 298.15 |
0.1340 |
0.0281 |
| 298.15 |
0.1428 |
0.0281 |
| 298.15 |
0.1767 |
0.0280 |
| 303.15 |
0.0000 |
0.0710 |
| 303.15 |
0.0047 |
0.0491 |
| 303.15 |
0.0066 |
0.0447 |
| 303.15 |
0.0090 |
0.0404 |
| 303.15 |
0.0100 |
0.0391 |
| 303.15 |
0.0127 |
0.0362 |
| 303.15 |
0.0143 |
0.0350 |
| 303.15 |
0.0165 |
0.0336 |
| 303.15 |
0.0335 |
0.0286 |
| 303.15 |
0.0452 |
0.0281 |
| 303.15 |
0.0583 |
0.0281 |
| 303.15 |
0.0872 |
0.0279 |
| 303.15 |
0.0995 |
0.0279 |
| 303.15 |
0.1147 |
0.0278 |
| 303.15 |
0.1340 |
0.0278 |
| 303.15 |
0.1428 |
0.0278 |
| 303.15 |
0.1767 |
0.0278 |
| 308.15 |
0.0000 |
0.0702 |
| 308.15 |
0.0047 |
0.0486 |
| 308.15 |
0.0066 |
0.0440 |
| 308.15 |
0.0090 |
0.0397 |
| 308.15 |
0.0100 |
0.0385 |
| 308.15 |
0.0127 |
0.0357 |
| 308.15 |
0.0143 |
0.0345 |
| 308.15 |
0.0165 |
0.0332 |
| 308.15 |
0.0335 |
0.0284 |
| 308.15 |
0.0452 |
0.0279 |
| 308.15 |
0.0583 |
0.0279 |
| 308.15 |
0.0872 |
0.0277 |
| 308.15 |
0.0995 |
0.0277 |
| 308.15 |
0.1147 |
0.0276 |
| 308.15 |
0.1340 |
0.0276 |
| 308.15 |
0.1428 |
0.0276 |
| 308.15 |
0.1767 |
0.0275 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0000 |
0.0711 |
| 0.0001 |
0.0705 |
| 0.0006 |
0.0663 |
| 0.0016 |
0.0603 |
| 0.0028 |
0.0551 |
| 0.0056 |
0.0463 |
| 0.0075 |
0.0421 |
| 0.0136 |
0.0359 |
| 0.0201 |
0.0319 |
| 0.0299 |
0.0292 |
| 0.0480 |
0.0285 |
| 0.0596 |
0.0284 |
| 0.0865 |
0.0282 |
| 0.1034 |
0.0282 |
| 0.2033 |
0.0279 |
| 0.2997 |
0.0277 |
| 0.3810 |
0.0277 |
| 0.5038 |
0.0276 |
| 0.5763 |
0.0274 |
| 0.7036 |
0.0271 |
| 0.8019 |
0.0269 |
| 0.9189 |
0.0265 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Butanoic acid (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 293.15 |
0.0000 |
0.0726 |
| 293.15 |
0.0047 |
0.0505 |
| 293.15 |
0.0066 |
0.0459 |
| 293.15 |
0.0090 |
0.0416 |
| 293.15 |
0.0100 |
0.0403 |
| 293.15 |
0.0127 |
0.0374 |
| 293.15 |
0.0143 |
0.0361 |
| 293.15 |
0.0165 |
0.0346 |
| 293.15 |
0.0335 |
0.0293 |
| 293.15 |
0.0452 |
0.0285 |
| 293.15 |
0.0583 |
0.0285 |
| 293.15 |
0.0872 |
0.0286 |
| 293.15 |
0.0995 |
0.0285 |
| 293.15 |
0.1147 |
0.0284 |
| 293.15 |
0.1340 |
0.0282 |
| 293.15 |
0.1428 |
0.0282 |
| 293.15 |
0.1767 |
0.0282 |
| 298.15 |
0.0000 |
0.0718 |
| 298.15 |
0.0047 |
0.0500 |
| 298.15 |
0.0066 |
0.0453 |
| 298.15 |
0.0090 |
0.0410 |
| 298.15 |
0.0100 |
0.0397 |
| 298.15 |
0.0127 |
0.0368 |
| 298.15 |
0.0143 |
0.0356 |
| 298.15 |
0.0165 |
0.0342 |
| 298.15 |
0.0335 |
0.0289 |
| 298.15 |
0.0452 |
0.0283 |
| 298.15 |
0.0583 |
0.0284 |
| 298.15 |
0.0872 |
0.0283 |
| 298.15 |
0.0995 |
0.0282 |
| 298.15 |
0.1147 |
0.0282 |
| 298.15 |
0.1340 |
0.0281 |
| 298.15 |
0.1428 |
0.0281 |
| 298.15 |
0.1767 |
0.0280 |
| 303.15 |
0.0000 |
0.0710 |
| 303.15 |
0.0047 |
0.0491 |
| 303.15 |
0.0066 |
0.0447 |
| 303.15 |
0.0090 |
0.0404 |
| 303.15 |
0.0100 |
0.0391 |
| 303.15 |
0.0127 |
0.0362 |
| 303.15 |
0.0143 |
0.0350 |
| 303.15 |
0.0165 |
0.0336 |
| 303.15 |
0.0335 |
0.0286 |
| 303.15 |
0.0452 |
0.0281 |
| 303.15 |
0.0583 |
0.0281 |
| 303.15 |
0.0872 |
0.0279 |
| 303.15 |
0.0995 |
0.0279 |
| 303.15 |
0.1147 |
0.0278 |
| 303.15 |
0.1340 |
0.0278 |
| 303.15 |
0.1428 |
0.0278 |
| 303.15 |
0.1767 |
0.0278 |
| 308.15 |
0.0000 |
0.0702 |
| 308.15 |
0.0047 |
0.0486 |
| 308.15 |
0.0066 |
0.0440 |
| 308.15 |
0.0090 |
0.0397 |
| 308.15 |
0.0100 |
0.0385 |
| 308.15 |
0.0127 |
0.0357 |
| 308.15 |
0.0143 |
0.0345 |
| 308.15 |
0.0165 |
0.0332 |
| 308.15 |
0.0335 |
0.0284 |
| 308.15 |
0.0452 |
0.0279 |
| 308.15 |
0.0583 |
0.0279 |
| 308.15 |
0.0872 |
0.0277 |
| 308.15 |
0.0995 |
0.0277 |
| 308.15 |
0.1147 |
0.0276 |
| 308.15 |
0.1340 |
0.0276 |
| 308.15 |
0.1428 |
0.0276 |
| 308.15 |
0.1767 |
0.0275 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
| 0.9790 |
268.65 |
| 0.9130 |
266.15 |
| 0.8510 |
265.35 |
| 0.8110 |
263.85 |
| 0.7630 |
263.15 |
| 0.7120 |
261.55 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
| 0.6160 |
260.85 |
| 0.5420 |
261.25 |
| 0.5010 |
262.05 |
| 0.4420 |
263.55 |
| 0.4090 |
264.05 |
| 0.3450 |
265.75 |
| 0.2730 |
267.25 |
| 0.2320 |
268.05 |
| 0.1670 |
269.15 |
| 0.1190 |
269.95 |
| 0.0490 |
271.65 |
| 0.0000 |
273.15 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
| 0.9790 |
268.65 |
| 0.9130 |
266.15 |
| 0.8510 |
265.35 |
| 0.8110 |
263.85 |
| 0.7630 |
263.15 |
| 0.7120 |
261.55 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
| Mole fraction of Butanoic acid (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
| 0.6160 |
260.85 |
| 0.5420 |
261.25 |
| 0.5010 |
262.05 |
| 0.4420 |
263.55 |
| 0.4090 |
264.05 |
| 0.3450 |
265.75 |
| 0.2730 |
267.25 |
| 0.2320 |
268.05 |
| 0.1670 |
269.15 |
| 0.1190 |
269.95 |
| 0.0490 |
271.65 |
| 0.0000 |
273.15 |
Sources