Datasets
-
Mole fraction (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
n0 - Refractive index (Na D-line)
-
ρl - Mass density, kg/m3 (2)
-
Tboil(P) - Boiling temperature at pressure P, K
-
Vapor or sublimation pressure, kPa
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Water (2) - Gas |
| 1.0000 |
373.20 |
1.0000 |
| 0.9986 |
373.20 |
0.9991 |
| 0.9983 |
373.20 |
0.9990 |
| 0.9967 |
373.20 |
0.9980 |
| 0.9917 |
373.20 |
0.9953 |
| 0.9891 |
373.20 |
0.9940 |
| 0.9862 |
373.20 |
0.9931 |
| 0.9849 |
373.20 |
0.9926 |
| 0.9815 |
373.20 |
0.9917 |
| 0.9775 |
373.30 |
0.9905 |
| 0.9720 |
373.40 |
0.9887 |
| 0.9275 |
373.70 |
0.9845 |
| 0.8270 |
374.10 |
0.9813 |
| 0.7943 |
374.20 |
0.9811 |
| 0.7222 |
374.50 |
0.9801 |
| 0.6641 |
375.00 |
0.9791 |
| 0.5990 |
375.50 |
0.9789 |
| 0.4780 |
377.60 |
0.9751 |
| 0.4481 |
378.50 |
0.9749 |
| 0.0000 |
480.20 |
0.0000 |
| 1.0000 |
354.80 |
1.0000 |
| 0.9866 |
354.90 |
0.9930 |
| 0.9579 |
354.90 |
0.9868 |
| 0.9567 |
355.00 |
0.9867 |
| 0.8030 |
355.50 |
0.9826 |
| 0.7801 |
355.80 |
0.9824 |
| 0.4952 |
357.30 |
0.9775 |
| 0.4575 |
359.20 |
0.9753 |
| 0.3252 |
361.80 |
0.9720 |
| 0.1983 |
372.40 |
0.9526 |
| 0.0000 |
451.50 |
0.0000 |
| 1.0000 |
319.60 |
1.0000 |
| 0.9967 |
319.60 |
0.9986 |
| 0.9826 |
319.80 |
0.9947 |
| 0.9361 |
320.00 |
0.9889 |
| 0.7984 |
320.30 |
0.9823 |
| 0.7509 |
320.30 |
0.9839 |
| 0.4994 |
321.20 |
0.9832 |
| 0.3052 |
323.10 |
0.9767 |
| 0.1853 |
329.80 |
0.9686 |
| 0.1099 |
340.10 |
0.9389 |
| 0.0000 |
401.40 |
0.0000 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Water (2) - Gas |
| 0.0000 |
350.18 |
0.0000 |
| 0.0510 |
350.18 |
0.8800 |
| 0.0970 |
350.19 |
0.9300 |
| 0.2000 |
350.19 |
0.9600 |
| 0.3010 |
350.19 |
0.9700 |
| 0.3960 |
350.19 |
0.9800 |
| 0.5010 |
350.20 |
0.9800 |
| 0.5510 |
350.19 |
0.9800 |
| 0.5930 |
350.24 |
0.9800 |
| 0.6060 |
350.19 |
0.9800 |
| 0.6930 |
350.24 |
0.9810 |
| 0.7960 |
350.24 |
0.9810 |
| 0.8980 |
350.23 |
0.9810 |
| 0.9688 |
350.23 |
0.9870 |
| 0.9878 |
350.21 |
0.9940 |
| 1.0000 |
350.12 |
1.0000 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2(3H)-Furanone, dihydro-5-methyl- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 288.15 |
0.0057 |
-0.0273 |
| 288.15 |
0.0047 |
-0.0231 |
| 288.15 |
0.0038 |
-0.0187 |
| 288.15 |
0.0028 |
-0.0143 |
| 288.15 |
0.0019 |
-0.0096 |
| 288.15 |
0.0009 |
-0.0049 |
| 298.15 |
0.0057 |
-0.0200 |
| 298.15 |
0.0057 |
-0.0201 |
| 298.15 |
0.0047 |
-0.0170 |
| 298.15 |
0.0047 |
-0.0170 |
| 298.15 |
0.0038 |
-0.0138 |
| 298.15 |
0.0038 |
-0.0139 |
| 298.15 |
0.0028 |
-0.0106 |
| 298.15 |
0.0028 |
-0.0106 |
| 298.15 |
0.0019 |
-0.0072 |
| 298.15 |
0.0019 |
-0.0072 |
| 298.15 |
0.0009 |
-0.0037 |
| 298.15 |
0.0009 |
-0.0037 |
| 308.15 |
0.0057 |
-0.0128 |
| 308.15 |
0.0057 |
-0.0129 |
| 308.15 |
0.0047 |
-0.0109 |
| 308.15 |
0.0047 |
-0.0110 |
| 308.15 |
0.0038 |
-0.0090 |
| 308.15 |
0.0038 |
-0.0090 |
| 308.15 |
0.0028 |
-0.0069 |
| 308.15 |
0.0028 |
-0.0069 |
| 308.15 |
0.0019 |
-0.0047 |
| 308.15 |
0.0019 |
-0.0047 |
| 308.15 |
0.0009 |
-0.0024 |
| 308.15 |
0.0009 |
-0.0024 |
| 318.15 |
0.0057 |
-0.0055 |
| 318.15 |
0.0057 |
-0.0055 |
| 318.15 |
0.0047 |
-0.0048 |
| 318.15 |
0.0047 |
-0.0048 |
| 318.15 |
0.0038 |
-0.0040 |
| 318.15 |
0.0038 |
-0.0041 |
| 318.15 |
0.0028 |
-0.0032 |
| 318.15 |
0.0028 |
-0.0032 |
| 318.15 |
0.0019 |
-0.0022 |
| 318.15 |
0.0019 |
-0.0022 |
| 318.15 |
0.0009 |
-0.0011 |
| 318.15 |
0.0009 |
-0.0011 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
130 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 322.60 |
0.2040 |
0.8640 |
| 322.60 |
0.4010 |
1.043 |
| 322.60 |
0.5030 |
0.9690 |
| 322.60 |
0.6020 |
0.8230 |
| 322.60 |
0.6020 |
0.8260 |
| 322.60 |
0.7000 |
0.6350 |
| 322.60 |
0.8010 |
0.4060 |
| 322.60 |
0.9000 |
0.1680 |
| 322.60 |
0.9500 |
0.0484 |
| 303.20 |
0.0970 |
0.5200 |
| 303.20 |
0.2030 |
0.8260 |
| 303.20 |
0.3030 |
0.9280 |
| 303.20 |
0.4000 |
0.9070 |
| 303.20 |
0.5140 |
0.8120 |
| 303.20 |
0.6010 |
0.6290 |
| 303.20 |
0.7000 |
0.4460 |
| 303.20 |
0.8010 |
0.2430 |
| 303.20 |
0.9000 |
0.0430 |
| 303.20 |
0.8410 |
0.1620 |
| 303.20 |
0.8940 |
0.0530 |
| 303.20 |
0.9140 |
0.0129 |
| 303.20 |
0.9140 |
0.0100 |
| 303.20 |
0.9300 |
-0.0183 |
| 303.20 |
0.9460 |
-0.0410 |
| 303.20 |
0.9815 |
-0.0760 |
| 303.20 |
0.9906 |
-0.0430 |
| 303.20 |
0.9962 |
-0.0174 |
| 303.20 |
0.9981 |
-0.0088 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2(3H)-Furanone, dihydro-5-methyl- (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 293.20 |
0.0000 |
1.3332 |
| 293.20 |
0.0158 |
1.342 |
| 293.20 |
0.0318 |
1.3505 |
| 293.20 |
0.0532 |
1.3591 |
| 293.20 |
0.0789 |
1.3682 |
| 293.20 |
0.1066 |
1.3761 |
| 293.20 |
0.1405 |
1.3837 |
| 293.20 |
0.1855 |
1.3913 |
| 293.20 |
0.2295 |
1.3987 |
| 293.20 |
0.2964 |
1.4062 |
| 293.20 |
0.3833 |
1.4135 |
| 293.20 |
0.5097 |
1.4204 |
| 293.20 |
0.7092 |
1.4273 |
| 293.20 |
1.0000 |
1.4339 |
| 298.20 |
0.0000 |
1.3327 |
| 298.20 |
0.0158 |
1.3411 |
| 298.20 |
0.0318 |
1.3499 |
| 298.20 |
0.0532 |
1.3585 |
| 298.20 |
0.0789 |
1.3671 |
| 298.20 |
0.1066 |
1.3751 |
| 298.20 |
0.1405 |
1.3826 |
| 298.20 |
0.1855 |
1.39 |
| 298.20 |
0.2295 |
1.397 |
| 298.20 |
0.2964 |
1.4046 |
| 298.20 |
0.3833 |
1.4119 |
| 298.20 |
0.5097 |
1.4186 |
| 298.20 |
0.7092 |
1.4259 |
| 298.20 |
1.0000 |
1.4316 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2(3H)-Furanone, dihydro-5-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.0057 |
1002.113 |
| 288.15 |
0.0047 |
1001.619 |
| 288.15 |
0.0038 |
1001.124 |
| 288.15 |
0.0028 |
1000.622 |
| 288.15 |
0.0019 |
1000.117 |
| 288.15 |
0.0009 |
999.61 |
| 298.15 |
0.0057 |
999.717 |
| 298.15 |
0.0057 |
999.723 |
| 298.15 |
0.0047 |
999.28 |
| 298.15 |
0.0047 |
999.282 |
| 298.15 |
0.0038 |
998.843 |
| 298.15 |
0.0038 |
998.844 |
| 298.15 |
0.0028 |
998.399 |
| 298.15 |
0.0028 |
998.397 |
| 298.15 |
0.0019 |
997.952 |
| 298.15 |
0.0019 |
997.948 |
| 298.15 |
0.0009 |
997.5 |
| 298.15 |
0.0009 |
997.5 |
| 308.15 |
0.0057 |
996.412 |
| 308.15 |
0.0057 |
996.415 |
| 308.15 |
0.0047 |
996.023 |
| 308.15 |
0.0047 |
996.023 |
| 308.15 |
0.0038 |
995.634 |
| 308.15 |
0.0038 |
995.637 |
| 308.15 |
0.0028 |
995.239 |
| 308.15 |
0.0028 |
995.239 |
| 308.15 |
0.0019 |
994.839 |
| 308.15 |
0.0019 |
994.839 |
| 308.15 |
0.0009 |
994.435 |
| 308.15 |
0.0009 |
994.435 |
| 318.15 |
0.0057 |
992.329 |
| 318.15 |
0.0057 |
992.332 |
| 318.15 |
0.0047 |
991.985 |
| 318.15 |
0.0047 |
991.983 |
| 318.15 |
0.0038 |
991.641 |
| 318.15 |
0.0038 |
991.639 |
| 318.15 |
0.0028 |
991.289 |
| 318.15 |
0.0028 |
991.289 |
| 318.15 |
0.0019 |
990.933 |
| 318.15 |
0.0019 |
990.933 |
| 318.15 |
0.0009 |
990.572 |
| 318.15 |
0.0009 |
990.573 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
298.1 (Liquid)
| Fixed |
Measured |
| Mass fraction of Water (2) - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
| 1.0000 |
109.00 |
997.0 |
| 0.8997 |
109.00 |
1005.5 |
| 0.7999 |
109.00 |
1013.8 |
| 0.6999 |
108.00 |
1021.1 |
| 0.6000 |
107.00 |
1027.1 |
| 0.5000 |
107.00 |
1032.9 |
| 0.4000 |
107.00 |
1037.6 |
| 0.3025 |
107.00 |
1041.7 |
| 0.2005 |
107.00 |
1044.9 |
| 0.1004 |
107.00 |
1047.0 |
| 0.0000 |
107.00 |
1048.8 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 101.33 |
1.0000 |
373.20 |
| 101.33 |
0.9986 |
373.20 |
| 101.33 |
0.9983 |
373.20 |
| 101.33 |
0.9967 |
373.20 |
| 101.33 |
0.9917 |
373.20 |
| 101.33 |
0.9891 |
373.20 |
| 101.33 |
0.9862 |
373.20 |
| 101.33 |
0.9849 |
373.20 |
| 101.33 |
0.9815 |
373.20 |
| 101.33 |
0.9775 |
373.30 |
| 101.33 |
0.9720 |
373.40 |
| 101.33 |
0.9275 |
373.70 |
| 101.33 |
0.8270 |
374.10 |
| 101.33 |
0.7943 |
374.20 |
| 101.33 |
0.7222 |
374.50 |
| 101.33 |
0.6641 |
375.00 |
| 101.33 |
0.5990 |
375.50 |
| 101.33 |
0.4780 |
377.60 |
| 101.33 |
0.4481 |
378.50 |
| 101.33 |
0.0000 |
480.20 |
| 50.60 |
1.0000 |
354.80 |
| 50.60 |
0.9866 |
354.90 |
| 50.60 |
0.9579 |
354.90 |
| 50.60 |
0.9567 |
355.00 |
| 50.60 |
0.8030 |
355.50 |
| 50.60 |
0.7801 |
355.80 |
| 50.60 |
0.4952 |
357.30 |
| 50.60 |
0.4575 |
359.20 |
| 50.60 |
0.3252 |
361.80 |
| 50.60 |
0.1983 |
372.40 |
| 50.60 |
0.0000 |
451.50 |
| 10.10 |
1.0000 |
319.60 |
| 10.10 |
0.9967 |
319.60 |
| 10.10 |
0.9826 |
319.80 |
| 10.10 |
0.9361 |
320.00 |
| 10.10 |
0.7984 |
320.30 |
| 10.10 |
0.7509 |
320.30 |
| 10.10 |
0.4994 |
321.20 |
| 10.10 |
0.3052 |
323.10 |
| 10.10 |
0.1853 |
329.80 |
| 10.10 |
0.1099 |
340.10 |
| 10.10 |
0.0000 |
401.40 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 0.0000 |
350.18 |
1.20 |
| 0.0510 |
350.18 |
9.50 |
| 0.0970 |
350.19 |
15.50 |
| 0.2000 |
350.19 |
25.60 |
| 0.3010 |
350.19 |
31.90 |
| 0.3960 |
350.19 |
35.80 |
| 0.5010 |
350.20 |
38.50 |
| 0.5510 |
350.19 |
39.40 |
| 0.5930 |
350.24 |
40.10 |
| 0.6060 |
350.19 |
40.40 |
| 0.6930 |
350.24 |
40.60 |
| 0.7960 |
350.24 |
40.90 |
| 0.8980 |
350.23 |
41.20 |
| 0.9688 |
350.23 |
41.70 |
| 0.9878 |
350.21 |
41.80 |
| 1.0000 |
350.12 |
41.90 |
Sources
Note: These property values are available through the Cheméo API. A free account gives you an access key.