Datasets
-
Molar enthalpy (4)
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Fixed |
Measured |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
0.0008 |
0.0032 |
-0.3963 |
0.0032 |
0.0057 |
-0.3917 |
0.0057 |
0.0081 |
-0.3838 |
0.0081 |
0.0106 |
-0.3784 |
0.0106 |
0.0130 |
-0.3648 |
0.0130 |
0.0153 |
-0.3604 |
0.0153 |
0.0177 |
-0.3531 |
0.0177 |
0.0200 |
-0.3469 |
0.0200 |
0.0223 |
-0.3396 |
0.0223 |
0.0245 |
-0.3352 |
0.0245 |
0.0268 |
-0.3290 |
0.0268 |
0.0290 |
-0.3205 |
0.0290 |
0.0312 |
-0.3164 |
0.0312 |
0.0333 |
-0.3108 |
0.0333 |
0.0355 |
-0.3058 |
0.0355 |
0.0376 |
-0.2980 |
0.0376 |
0.0397 |
-0.2944 |
0.0397 |
0.0418 |
-0.2877 |
0.0418 |
0.0438 |
-0.2825 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Fixed |
Measured |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
0.0008 |
0.0034 |
-0.4228 |
0.0034 |
0.0060 |
-0.4172 |
0.0060 |
0.0085 |
-0.4079 |
0.0085 |
0.0110 |
-0.4025 |
0.0110 |
0.0135 |
-0.3903 |
0.0135 |
0.0160 |
-0.3853 |
0.0160 |
0.0184 |
-0.3768 |
0.0184 |
0.0208 |
-0.3696 |
0.0208 |
0.0232 |
-0.3627 |
0.0232 |
0.0256 |
-0.3566 |
0.0256 |
0.0279 |
-0.3480 |
0.0279 |
0.0302 |
-0.3433 |
0.0302 |
0.0325 |
-0.3357 |
0.0325 |
0.0348 |
-0.3285 |
0.0348 |
0.0370 |
-0.3244 |
0.0370 |
0.0392 |
-0.3155 |
0.0392 |
0.0414 |
-0.3119 |
0.0414 |
0.0435 |
-0.3059 |
0.0435 |
0.0457 |
-0.2994 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Fixed |
Measured |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
0.0008 |
0.0032 |
-0.3963 |
0.0032 |
0.0057 |
-0.3917 |
0.0057 |
0.0081 |
-0.3838 |
0.0081 |
0.0106 |
-0.3784 |
0.0106 |
0.0130 |
-0.3648 |
0.0130 |
0.0153 |
-0.3604 |
0.0153 |
0.0177 |
-0.3531 |
0.0177 |
0.0200 |
-0.3469 |
0.0200 |
0.0223 |
-0.3396 |
0.0223 |
0.0245 |
-0.3352 |
0.0245 |
0.0268 |
-0.3290 |
0.0268 |
0.0290 |
-0.3205 |
0.0290 |
0.0312 |
-0.3164 |
0.0312 |
0.0333 |
-0.3108 |
0.0333 |
0.0355 |
-0.3058 |
0.0355 |
0.0376 |
-0.2980 |
0.0376 |
0.0397 |
-0.2944 |
0.0397 |
0.0418 |
-0.2877 |
0.0418 |
0.0438 |
-0.2825 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Fixed |
Measured |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
0.0008 |
0.0034 |
-0.4228 |
0.0034 |
0.0060 |
-0.4172 |
0.0060 |
0.0085 |
-0.4079 |
0.0085 |
0.0110 |
-0.4025 |
0.0110 |
0.0135 |
-0.3903 |
0.0135 |
0.0160 |
-0.3853 |
0.0160 |
0.0184 |
-0.3768 |
0.0184 |
0.0208 |
-0.3696 |
0.0208 |
0.0232 |
-0.3627 |
0.0232 |
0.0256 |
-0.3566 |
0.0256 |
0.0279 |
-0.3480 |
0.0279 |
0.0302 |
-0.3433 |
0.0302 |
0.0325 |
-0.3357 |
0.0325 |
0.0348 |
-0.3285 |
0.0348 |
0.0370 |
-0.3244 |
0.0370 |
0.0392 |
-0.3155 |
0.0392 |
0.0414 |
-0.3119 |
0.0414 |
0.0435 |
-0.3059 |
0.0435 |
0.0457 |
-0.2994 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2,5-Hexanediol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
283.15 |
999.7 |
0.0008 |
283.15 |
999.67 |
0.0020 |
283.15 |
999.6 |
0.0037 |
283.15 |
999.53 |
0.0073 |
283.15 |
999.48 |
0.0090 |
283.15 |
999.54 |
0.0102 |
283.15 |
999.61 |
0.0123 |
283.15 |
999.75 |
0.0142 |
283.15 |
999.92 |
0.0159 |
283.15 |
1000.08 |
0.0177 |
283.15 |
1000.27 |
0.0263 |
283.15 |
1001.32 |
0.0353 |
283.15 |
1002.49 |
0.0516 |
283.15 |
1004.41 |
0.0672 |
283.15 |
1005.71 |
0.0688 |
283.15 |
1005.83 |
0.0821 |
283.15 |
1006.35 |
0.0980 |
283.15 |
1006.33 |
0.1120 |
283.15 |
1005.71 |
0.0000 |
288.15 |
999.1 |
0.0008 |
288.15 |
999.06 |
0.0020 |
288.15 |
998.98 |
0.0037 |
288.15 |
998.88 |
0.0073 |
288.15 |
998.82 |
0.0090 |
288.15 |
998.85 |
0.0102 |
288.15 |
998.88 |
0.0123 |
288.15 |
998.97 |
0.0142 |
288.15 |
999.08 |
0.0159 |
288.15 |
999.2 |
0.0177 |
288.15 |
999.34 |
0.0263 |
288.15 |
1000.14 |
0.0353 |
288.15 |
1001.07 |
0.0516 |
288.15 |
1002.55 |
0.0672 |
288.15 |
1003.37 |
0.0688 |
288.15 |
1003.42 |
0.0821 |
288.15 |
1003.53 |
0.0980 |
288.15 |
1003.14 |
0.1120 |
288.15 |
1002.53 |
0.0000 |
293.15 |
998.21 |
0.0008 |
293.15 |
998.13 |
0.0020 |
293.15 |
998.04 |
0.0037 |
293.15 |
997.94 |
0.0073 |
293.15 |
997.86 |
0.0090 |
293.15 |
997.84 |
0.0102 |
293.15 |
997.84 |
0.0123 |
293.15 |
997.89 |
0.0142 |
293.15 |
997.96 |
0.0159 |
293.15 |
998.04 |
0.0177 |
293.15 |
998.14 |
0.0263 |
293.15 |
998.73 |
0.0353 |
293.15 |
999.39 |
0.0516 |
293.15 |
1000.35 |
0.0672 |
293.15 |
1000.75 |
0.0688 |
293.15 |
1000.76 |
0.0821 |
293.15 |
1000.63 |
0.0980 |
293.15 |
1000.02 |
0.1120 |
293.15 |
999.19 |
0.0000 |
298.15 |
997.04 |
0.0008 |
298.15 |
996.94 |
0.0020 |
298.15 |
996.84 |
0.0037 |
298.15 |
996.73 |
0.0073 |
298.15 |
996.6 |
0.0090 |
298.15 |
996.58 |
0.0102 |
298.15 |
996.58 |
0.0123 |
298.15 |
996.6 |
0.0142 |
298.15 |
996.64 |
0.0159 |
298.15 |
996.68 |
0.0177 |
298.15 |
996.74 |
0.0263 |
298.15 |
997.13 |
0.0353 |
298.15 |
997.56 |
0.0516 |
298.15 |
998.09 |
0.0672 |
298.15 |
998.16 |
0.0688 |
298.15 |
998.14 |
0.0821 |
298.15 |
997.8 |
0.0980 |
298.15 |
996.97 |
0.1120 |
298.15 |
996.16 |
0.0000 |
303.15 |
995.65 |
0.0008 |
303.15 |
995.52 |
0.0020 |
303.15 |
995.4 |
0.0037 |
303.15 |
995.27 |
0.0073 |
303.15 |
995.14 |
0.0090 |
303.15 |
995.09 |
0.0102 |
303.15 |
995.07 |
0.0123 |
303.15 |
995.05 |
0.0142 |
303.15 |
995.05 |
0.0159 |
303.15 |
995.06 |
0.0177 |
303.15 |
995.07 |
0.0263 |
303.15 |
995.23 |
0.0353 |
303.15 |
995.43 |
0.0516 |
303.15 |
995.59 |
0.0672 |
303.15 |
995.35 |
0.0688 |
303.15 |
995.31 |
0.0821 |
303.15 |
994.75 |
0.0980 |
303.15 |
993.8 |
0.1120 |
303.15 |
992.78 |
0.0000 |
308.15 |
994.03 |
0.0008 |
308.15 |
993.87 |
0.0020 |
308.15 |
993.73 |
0.0037 |
308.15 |
993.58 |
0.0073 |
308.15 |
993.42 |
0.0090 |
308.15 |
993.35 |
0.0102 |
308.15 |
993.31 |
0.0123 |
308.15 |
993.25 |
0.0142 |
308.15 |
993.21 |
0.0159 |
308.15 |
993.19 |
0.0177 |
308.15 |
993.17 |
0.0263 |
308.15 |
993.17 |
0.0353 |
308.15 |
993.19 |
0.0516 |
308.15 |
993.0 |
0.0672 |
308.15 |
992.44 |
0.0688 |
308.15 |
992.36 |
0.0821 |
308.15 |
991.62 |
0.0980 |
308.15 |
990.55 |
0.1120 |
308.15 |
989.51 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2,5-Hexanediol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
283.15 |
999.7 |
0.0008 |
283.15 |
999.67 |
0.0020 |
283.15 |
999.6 |
0.0037 |
283.15 |
999.53 |
0.0073 |
283.15 |
999.48 |
0.0090 |
283.15 |
999.54 |
0.0102 |
283.15 |
999.61 |
0.0123 |
283.15 |
999.75 |
0.0142 |
283.15 |
999.92 |
0.0159 |
283.15 |
1000.08 |
0.0177 |
283.15 |
1000.27 |
0.0263 |
283.15 |
1001.32 |
0.0353 |
283.15 |
1002.49 |
0.0516 |
283.15 |
1004.41 |
0.0672 |
283.15 |
1005.71 |
0.0688 |
283.15 |
1005.83 |
0.0821 |
283.15 |
1006.35 |
0.0980 |
283.15 |
1006.33 |
0.1120 |
283.15 |
1005.71 |
0.0000 |
288.15 |
999.1 |
0.0008 |
288.15 |
999.06 |
0.0020 |
288.15 |
998.98 |
0.0037 |
288.15 |
998.88 |
0.0073 |
288.15 |
998.82 |
0.0090 |
288.15 |
998.85 |
0.0102 |
288.15 |
998.88 |
0.0123 |
288.15 |
998.97 |
0.0142 |
288.15 |
999.08 |
0.0159 |
288.15 |
999.2 |
0.0177 |
288.15 |
999.34 |
0.0263 |
288.15 |
1000.14 |
0.0353 |
288.15 |
1001.07 |
0.0516 |
288.15 |
1002.55 |
0.0672 |
288.15 |
1003.37 |
0.0688 |
288.15 |
1003.42 |
0.0821 |
288.15 |
1003.53 |
0.0980 |
288.15 |
1003.14 |
0.1120 |
288.15 |
1002.53 |
0.0000 |
293.15 |
998.21 |
0.0008 |
293.15 |
998.13 |
0.0020 |
293.15 |
998.04 |
0.0037 |
293.15 |
997.94 |
0.0073 |
293.15 |
997.86 |
0.0090 |
293.15 |
997.84 |
0.0102 |
293.15 |
997.84 |
0.0123 |
293.15 |
997.89 |
0.0142 |
293.15 |
997.96 |
0.0159 |
293.15 |
998.04 |
0.0177 |
293.15 |
998.14 |
0.0263 |
293.15 |
998.73 |
0.0353 |
293.15 |
999.39 |
0.0516 |
293.15 |
1000.35 |
0.0672 |
293.15 |
1000.75 |
0.0688 |
293.15 |
1000.76 |
0.0821 |
293.15 |
1000.63 |
0.0980 |
293.15 |
1000.02 |
0.1120 |
293.15 |
999.19 |
0.0000 |
298.15 |
997.04 |
0.0008 |
298.15 |
996.94 |
0.0020 |
298.15 |
996.84 |
0.0037 |
298.15 |
996.73 |
0.0073 |
298.15 |
996.6 |
0.0090 |
298.15 |
996.58 |
0.0102 |
298.15 |
996.58 |
0.0123 |
298.15 |
996.6 |
0.0142 |
298.15 |
996.64 |
0.0159 |
298.15 |
996.68 |
0.0177 |
298.15 |
996.74 |
0.0263 |
298.15 |
997.13 |
0.0353 |
298.15 |
997.56 |
0.0516 |
298.15 |
998.09 |
0.0672 |
298.15 |
998.16 |
0.0688 |
298.15 |
998.14 |
0.0821 |
298.15 |
997.8 |
0.0980 |
298.15 |
996.97 |
0.1120 |
298.15 |
996.16 |
0.0000 |
303.15 |
995.65 |
0.0008 |
303.15 |
995.52 |
0.0020 |
303.15 |
995.4 |
0.0037 |
303.15 |
995.27 |
0.0073 |
303.15 |
995.14 |
0.0090 |
303.15 |
995.09 |
0.0102 |
303.15 |
995.07 |
0.0123 |
303.15 |
995.05 |
0.0142 |
303.15 |
995.05 |
0.0159 |
303.15 |
995.06 |
0.0177 |
303.15 |
995.07 |
0.0263 |
303.15 |
995.23 |
0.0353 |
303.15 |
995.43 |
0.0516 |
303.15 |
995.59 |
0.0672 |
303.15 |
995.35 |
0.0688 |
303.15 |
995.31 |
0.0821 |
303.15 |
994.75 |
0.0980 |
303.15 |
993.8 |
0.1120 |
303.15 |
992.78 |
0.0000 |
308.15 |
994.03 |
0.0008 |
308.15 |
993.87 |
0.0020 |
308.15 |
993.73 |
0.0037 |
308.15 |
993.58 |
0.0073 |
308.15 |
993.42 |
0.0090 |
308.15 |
993.35 |
0.0102 |
308.15 |
993.31 |
0.0123 |
308.15 |
993.25 |
0.0142 |
308.15 |
993.21 |
0.0159 |
308.15 |
993.19 |
0.0177 |
308.15 |
993.17 |
0.0263 |
308.15 |
993.17 |
0.0353 |
308.15 |
993.19 |
0.0516 |
308.15 |
993.0 |
0.0672 |
308.15 |
992.44 |
0.0688 |
308.15 |
992.36 |
0.0821 |
308.15 |
991.62 |
0.0980 |
308.15 |
990.55 |
0.1120 |
308.15 |
989.51 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 2,5-Hexanediol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0741 |
283.15 |
0.0010 |
0.0685 |
283.15 |
0.0027 |
0.0602 |
283.15 |
0.0037 |
0.0569 |
283.15 |
0.0068 |
0.0535 |
283.15 |
0.0088 |
0.0516 |
283.15 |
0.0103 |
0.0500 |
283.15 |
0.0135 |
0.0479 |
283.15 |
0.0168 |
0.0461 |
283.15 |
0.0263 |
0.0434 |
283.15 |
0.0370 |
0.0415 |
283.15 |
0.0462 |
0.0404 |
283.15 |
0.0630 |
0.0391 |
283.15 |
0.0808 |
0.0385 |
283.15 |
0.0960 |
0.0383 |
283.15 |
0.1117 |
0.0377 |
283.15 |
1.0000 |
0.0323 |
288.15 |
0.0000 |
0.0734 |
288.15 |
0.0010 |
0.0679 |
288.15 |
0.0027 |
0.0596 |
288.15 |
0.0037 |
0.0563 |
288.15 |
0.0068 |
0.0529 |
288.15 |
0.0088 |
0.0510 |
288.15 |
0.0103 |
0.0494 |
288.15 |
0.0135 |
0.0475 |
288.15 |
0.0168 |
0.0457 |
288.15 |
0.0263 |
0.0432 |
288.15 |
0.0370 |
0.0411 |
288.15 |
0.0462 |
0.0401 |
288.15 |
0.0630 |
0.0386 |
288.15 |
0.0808 |
0.0380 |
288.15 |
0.0960 |
0.0378 |
288.15 |
0.1117 |
0.0372 |
288.15 |
1.0000 |
0.0320 |
293.15 |
0.0000 |
0.0726 |
293.15 |
0.0010 |
0.0677 |
293.15 |
0.0027 |
0.0591 |
293.15 |
0.0037 |
0.0556 |
293.15 |
0.0068 |
0.0523 |
293.15 |
0.0088 |
0.0503 |
293.15 |
0.0103 |
0.0492 |
293.15 |
0.0135 |
0.0472 |
293.15 |
0.0168 |
0.0455 |
293.15 |
0.0263 |
0.0427 |
293.15 |
0.0370 |
0.0404 |
293.15 |
0.0462 |
0.0397 |
293.15 |
0.0630 |
0.0381 |
293.15 |
0.0808 |
0.0375 |
293.15 |
0.0960 |
0.0373 |
293.15 |
0.1117 |
0.0369 |
293.15 |
1.0000 |
0.0319 |
298.15 |
0.0000 |
0.0718 |
298.15 |
0.0010 |
0.0672 |
298.15 |
0.0027 |
0.0586 |
298.15 |
0.0037 |
0.0552 |
298.15 |
0.0068 |
0.0516 |
298.15 |
0.0088 |
0.0495 |
298.15 |
0.0103 |
0.0487 |
298.15 |
0.0135 |
0.0468 |
298.15 |
0.0168 |
0.0452 |
298.15 |
0.0263 |
0.0421 |
298.15 |
0.0370 |
0.0400 |
298.15 |
0.0462 |
0.0390 |
298.15 |
0.0630 |
0.0374 |
298.15 |
0.0808 |
0.0370 |
298.15 |
0.0960 |
0.0368 |
298.15 |
0.1117 |
0.0362 |
298.15 |
1.0000 |
0.0316 |
303.15 |
0.0000 |
0.0710 |
303.15 |
0.0010 |
0.0666 |
303.15 |
0.0027 |
0.0579 |
303.15 |
0.0037 |
0.0547 |
303.15 |
0.0068 |
0.0512 |
303.15 |
0.0088 |
0.0486 |
303.15 |
0.0103 |
0.0482 |
303.15 |
0.0135 |
0.0463 |
303.15 |
0.0168 |
0.0449 |
303.15 |
0.0263 |
0.0416 |
303.15 |
0.0370 |
0.0397 |
303.15 |
0.0462 |
0.0387 |
303.15 |
0.0630 |
0.0371 |
303.15 |
0.0808 |
0.0365 |
303.15 |
0.0960 |
0.0363 |
303.15 |
0.1117 |
0.0359 |
303.15 |
1.0000 |
0.0313 |
308.15 |
0.0000 |
0.0702 |
308.15 |
0.0010 |
0.0659 |
308.15 |
0.0027 |
0.0573 |
308.15 |
0.0037 |
0.0542 |
308.15 |
0.0068 |
0.0507 |
308.15 |
0.0088 |
0.0480 |
308.15 |
0.0103 |
0.0478 |
308.15 |
0.0135 |
0.0458 |
308.15 |
0.0168 |
0.0446 |
308.15 |
0.0263 |
0.0413 |
308.15 |
0.0370 |
0.0392 |
308.15 |
0.0462 |
0.0382 |
308.15 |
0.0630 |
0.0366 |
308.15 |
0.0808 |
0.0362 |
308.15 |
0.0960 |
0.0360 |
308.15 |
0.1117 |
0.0356 |
308.15 |
1.0000 |
0.0310 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 2,5-Hexanediol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0741 |
283.15 |
0.0010 |
0.0685 |
283.15 |
0.0027 |
0.0602 |
283.15 |
0.0037 |
0.0569 |
283.15 |
0.0068 |
0.0535 |
283.15 |
0.0088 |
0.0516 |
283.15 |
0.0103 |
0.0500 |
283.15 |
0.0135 |
0.0479 |
283.15 |
0.0168 |
0.0461 |
283.15 |
0.0263 |
0.0434 |
283.15 |
0.0370 |
0.0415 |
283.15 |
0.0462 |
0.0404 |
283.15 |
0.0630 |
0.0391 |
283.15 |
0.0808 |
0.0385 |
283.15 |
0.0960 |
0.0383 |
283.15 |
0.1117 |
0.0377 |
283.15 |
1.0000 |
0.0323 |
288.15 |
0.0000 |
0.0734 |
288.15 |
0.0010 |
0.0679 |
288.15 |
0.0027 |
0.0596 |
288.15 |
0.0037 |
0.0563 |
288.15 |
0.0068 |
0.0529 |
288.15 |
0.0088 |
0.0510 |
288.15 |
0.0103 |
0.0494 |
288.15 |
0.0135 |
0.0475 |
288.15 |
0.0168 |
0.0457 |
288.15 |
0.0263 |
0.0432 |
288.15 |
0.0370 |
0.0411 |
288.15 |
0.0462 |
0.0401 |
288.15 |
0.0630 |
0.0386 |
288.15 |
0.0808 |
0.0380 |
288.15 |
0.0960 |
0.0378 |
288.15 |
0.1117 |
0.0372 |
288.15 |
1.0000 |
0.0320 |
293.15 |
0.0000 |
0.0726 |
293.15 |
0.0010 |
0.0677 |
293.15 |
0.0027 |
0.0591 |
293.15 |
0.0037 |
0.0556 |
293.15 |
0.0068 |
0.0523 |
293.15 |
0.0088 |
0.0503 |
293.15 |
0.0103 |
0.0492 |
293.15 |
0.0135 |
0.0472 |
293.15 |
0.0168 |
0.0455 |
293.15 |
0.0263 |
0.0427 |
293.15 |
0.0370 |
0.0404 |
293.15 |
0.0462 |
0.0397 |
293.15 |
0.0630 |
0.0381 |
293.15 |
0.0808 |
0.0375 |
293.15 |
0.0960 |
0.0373 |
293.15 |
0.1117 |
0.0369 |
293.15 |
1.0000 |
0.0319 |
298.15 |
0.0000 |
0.0718 |
298.15 |
0.0010 |
0.0672 |
298.15 |
0.0027 |
0.0586 |
298.15 |
0.0037 |
0.0552 |
298.15 |
0.0068 |
0.0516 |
298.15 |
0.0088 |
0.0495 |
298.15 |
0.0103 |
0.0487 |
298.15 |
0.0135 |
0.0468 |
298.15 |
0.0168 |
0.0452 |
298.15 |
0.0263 |
0.0421 |
298.15 |
0.0370 |
0.0400 |
298.15 |
0.0462 |
0.0390 |
298.15 |
0.0630 |
0.0374 |
298.15 |
0.0808 |
0.0370 |
298.15 |
0.0960 |
0.0368 |
298.15 |
0.1117 |
0.0362 |
298.15 |
1.0000 |
0.0316 |
303.15 |
0.0000 |
0.0710 |
303.15 |
0.0010 |
0.0666 |
303.15 |
0.0027 |
0.0579 |
303.15 |
0.0037 |
0.0547 |
303.15 |
0.0068 |
0.0512 |
303.15 |
0.0088 |
0.0486 |
303.15 |
0.0103 |
0.0482 |
303.15 |
0.0135 |
0.0463 |
303.15 |
0.0168 |
0.0449 |
303.15 |
0.0263 |
0.0416 |
303.15 |
0.0370 |
0.0397 |
303.15 |
0.0462 |
0.0387 |
303.15 |
0.0630 |
0.0371 |
303.15 |
0.0808 |
0.0365 |
303.15 |
0.0960 |
0.0363 |
303.15 |
0.1117 |
0.0359 |
303.15 |
1.0000 |
0.0313 |
308.15 |
0.0000 |
0.0702 |
308.15 |
0.0010 |
0.0659 |
308.15 |
0.0027 |
0.0573 |
308.15 |
0.0037 |
0.0542 |
308.15 |
0.0068 |
0.0507 |
308.15 |
0.0088 |
0.0480 |
308.15 |
0.0103 |
0.0478 |
308.15 |
0.0135 |
0.0458 |
308.15 |
0.0168 |
0.0446 |
308.15 |
0.0263 |
0.0413 |
308.15 |
0.0370 |
0.0392 |
308.15 |
0.0462 |
0.0382 |
308.15 |
0.0630 |
0.0366 |
308.15 |
0.0808 |
0.0362 |
308.15 |
0.0960 |
0.0360 |
308.15 |
0.1117 |
0.0356 |
308.15 |
1.0000 |
0.0310 |
Sources
-
Effect of temperature on the surface tension of diluted aqueous solutions of 1,2-hexanediol, 1,5-hexanediol, 1,6-hexanediol and 2,5-hexanediol
-
Effect of temperature on the volumetric properties of dilute aqueous solutions of 1,2-hexanediol, 1,5-hexanediol, 1,6-hexanediol, and 2,5-hexanediol
-
Enthalpic Pairwise Interactions of Isomers of 2,4-pentanediol and 2,5-hexanediol in Dimethylsulfoxide + Water Mixtures at 298.15 K