Datasets
-
Activity coefficient (2)
-
Mole fraction (4)
-
Excess molar enthalpy (molar enthalpy (2)
-
csound,fluid - Speed of Sound, m/s (2)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Excess molar volume, m3/mol (2)
Activity coefficient of n-Hexane (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of n-Hexane (1) - Liquid |
| 290.00 |
1.76 |
| 299.89 |
1.71 |
| 309.98 |
1.67 |
| 319.99 |
1.65 |
| 330.02 |
1.61 |
Activity coefficient of n-Hexane (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of n-Hexane (1) - Liquid |
| 290.00 |
1.76 |
| 299.89 |
1.71 |
| 309.98 |
1.67 |
| 319.99 |
1.65 |
| 330.02 |
1.61 |
Mole fraction of n-Hexane (1)
[ref]
| Fixed |
Measured |
| Mole fraction of n-Hexane (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of n-Hexane (1) - Gas |
| 0.0000 |
50.00 |
0.0000 |
| 0.0000 |
75.00 |
0.0000 |
| 0.0000 |
94.00 |
0.0000 |
| 0.0410 |
75.00 |
0.0990 |
| 0.0420 |
50.00 |
0.1080 |
| 0.0430 |
94.00 |
0.1030 |
| 0.0850 |
94.00 |
0.1880 |
| 0.0860 |
50.00 |
0.2040 |
| 0.0860 |
75.00 |
0.1960 |
| 0.1110 |
94.00 |
0.2310 |
| 0.1130 |
75.00 |
0.2430 |
| 0.1170 |
50.00 |
0.2600 |
| 0.1560 |
94.00 |
0.3030 |
| 0.1570 |
50.00 |
0.3300 |
| 0.1570 |
75.00 |
0.3120 |
| 0.1950 |
94.00 |
0.3590 |
| 0.1980 |
75.00 |
0.3710 |
| 0.2030 |
50.00 |
0.3880 |
| 0.2410 |
94.00 |
0.4130 |
| 0.2430 |
50.00 |
0.4320 |
| 0.2440 |
75.00 |
0.4250 |
| 0.2900 |
50.00 |
0.4830 |
| 0.2900 |
75.00 |
0.4730 |
| 0.2910 |
94.00 |
0.4680 |
| 0.3340 |
75.00 |
0.5150 |
| 0.3350 |
50.00 |
0.5260 |
| 0.3350 |
94.00 |
0.5110 |
| 0.3810 |
75.00 |
0.5550 |
| 0.3820 |
94.00 |
0.5510 |
| 0.3830 |
50.00 |
0.5690 |
| 0.4280 |
94.00 |
0.5940 |
| 0.4300 |
75.00 |
0.5960 |
| 0.4330 |
50.00 |
0.6080 |
| 0.4820 |
94.00 |
0.6330 |
| 0.4830 |
75.00 |
0.6390 |
| 0.4900 |
50.00 |
0.6510 |
| 0.5430 |
94.00 |
0.6790 |
| 0.5460 |
75.00 |
0.6860 |
| 0.5480 |
50.00 |
0.6930 |
| 0.5990 |
94.00 |
0.7200 |
| 0.6060 |
75.00 |
0.7280 |
| 0.6070 |
50.00 |
0.7330 |
| 0.6620 |
94.00 |
0.7630 |
| 0.6630 |
50.00 |
0.7700 |
| 0.6630 |
75.00 |
0.7650 |
| 0.7160 |
75.00 |
0.8020 |
| 0.7160 |
94.00 |
0.7990 |
| 0.7180 |
50.00 |
0.8060 |
| 0.7730 |
50.00 |
0.8420 |
| 0.7730 |
75.00 |
0.8390 |
| 0.7730 |
94.00 |
0.8380 |
| 0.8180 |
94.00 |
0.8690 |
| 0.8190 |
75.00 |
0.8710 |
| 0.8210 |
50.00 |
0.8730 |
| 0.8670 |
75.00 |
0.9040 |
| 0.8670 |
94.00 |
0.9020 |
| 0.8680 |
50.00 |
0.9050 |
| 0.9240 |
94.00 |
0.9430 |
| 0.9260 |
50.00 |
0.9460 |
| 0.9260 |
75.00 |
0.9450 |
| 1.0000 |
50.00 |
1.0000 |
| 1.0000 |
75.00 |
1.0000 |
| 1.0000 |
94.00 |
1.0000 |
Henry's Law constant (mole fraction scale), kPa of n-Hexane (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of n-Hexane (1) - Liquid |
| 290.00 |
24.5 |
| 299.89 |
36.7 |
| 309.98 |
54.0 |
| 319.99 |
78.0 |
| 330.02 |
107.0 |
Mole fraction of n-Hexane (1)
[ref]
| Fixed |
Measured |
| Mole fraction of n-Hexane (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of n-Hexane (1) - Gas |
| 0.0000 |
50.00 |
0.0000 |
| 0.0000 |
75.00 |
0.0000 |
| 0.0000 |
94.00 |
0.0000 |
| 0.0410 |
75.00 |
0.0990 |
| 0.0420 |
50.00 |
0.1080 |
| 0.0430 |
94.00 |
0.1030 |
| 0.0850 |
94.00 |
0.1880 |
| 0.0860 |
50.00 |
0.2040 |
| 0.0860 |
75.00 |
0.1960 |
| 0.1110 |
94.00 |
0.2310 |
| 0.1130 |
75.00 |
0.2430 |
| 0.1170 |
50.00 |
0.2600 |
| 0.1560 |
94.00 |
0.3030 |
| 0.1570 |
50.00 |
0.3300 |
| 0.1570 |
75.00 |
0.3120 |
| 0.1950 |
94.00 |
0.3590 |
| 0.1980 |
75.00 |
0.3710 |
| 0.2030 |
50.00 |
0.3880 |
| 0.2410 |
94.00 |
0.4130 |
| 0.2430 |
50.00 |
0.4320 |
| 0.2440 |
75.00 |
0.4250 |
| 0.2900 |
50.00 |
0.4830 |
| 0.2900 |
75.00 |
0.4730 |
| 0.2910 |
94.00 |
0.4680 |
| 0.3340 |
75.00 |
0.5150 |
| 0.3350 |
50.00 |
0.5260 |
| 0.3350 |
94.00 |
0.5110 |
| 0.3810 |
75.00 |
0.5550 |
| 0.3820 |
94.00 |
0.5510 |
| 0.3830 |
50.00 |
0.5690 |
| 0.4280 |
94.00 |
0.5940 |
| 0.4300 |
75.00 |
0.5960 |
| 0.4330 |
50.00 |
0.6080 |
| 0.4820 |
94.00 |
0.6330 |
| 0.4830 |
75.00 |
0.6390 |
| 0.4900 |
50.00 |
0.6510 |
| 0.5430 |
94.00 |
0.6790 |
| 0.5460 |
75.00 |
0.6860 |
| 0.5480 |
50.00 |
0.6930 |
| 0.5990 |
94.00 |
0.7200 |
| 0.6060 |
75.00 |
0.7280 |
| 0.6070 |
50.00 |
0.7330 |
| 0.6620 |
94.00 |
0.7630 |
| 0.6630 |
50.00 |
0.7700 |
| 0.6630 |
75.00 |
0.7650 |
| 0.7160 |
75.00 |
0.8020 |
| 0.7160 |
94.00 |
0.7990 |
| 0.7180 |
50.00 |
0.8060 |
| 0.7730 |
50.00 |
0.8420 |
| 0.7730 |
75.00 |
0.8390 |
| 0.7730 |
94.00 |
0.8380 |
| 0.8180 |
94.00 |
0.8690 |
| 0.8190 |
75.00 |
0.8710 |
| 0.8210 |
50.00 |
0.8730 |
| 0.8670 |
75.00 |
0.9040 |
| 0.8670 |
94.00 |
0.9020 |
| 0.8680 |
50.00 |
0.9050 |
| 0.9240 |
94.00 |
0.9430 |
| 0.9260 |
50.00 |
0.9460 |
| 0.9260 |
75.00 |
0.9450 |
| 1.0000 |
50.00 |
1.0000 |
| 1.0000 |
75.00 |
1.0000 |
| 1.0000 |
94.00 |
1.0000 |
Henry's Law constant (mole fraction scale), kPa of n-Hexane (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of n-Hexane (1) - Liquid |
| 290.00 |
24.5 |
| 299.89 |
36.7 |
| 309.98 |
54.0 |
| 319.99 |
78.0 |
| 330.02 |
107.0 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 308.15 (Liquid)
| Mole fraction of Tetrahydropyran (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0581 |
0.1031 |
| 0.1073 |
0.1841 |
| 0.1962 |
0.3136 |
| 0.2274 |
0.3533 |
| 0.3276 |
0.4579 |
| 0.3888 |
0.5032 |
| 0.4395 |
0.5292 |
| 0.4968 |
0.5452 |
| 0.5220 |
0.5477 |
| 0.5931 |
0.5387 |
| 0.6634 |
0.5061 |
| 0.7514 |
0.4307 |
| 0.8124 |
0.3551 |
| 0.8997 |
0.2131 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 308.15 (Liquid)
| Mole fraction of Tetrahydropyran (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0581 |
0.1031 |
| 0.1073 |
0.1841 |
| 0.1962 |
0.3136 |
| 0.2274 |
0.3533 |
| 0.3276 |
0.4579 |
| 0.3888 |
0.5032 |
| 0.4395 |
0.5292 |
| 0.4968 |
0.5452 |
| 0.5220 |
0.5477 |
| 0.5931 |
0.5387 |
| 0.6634 |
0.5061 |
| 0.7514 |
0.4307 |
| 0.8124 |
0.3551 |
| 0.8997 |
0.2131 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 308.15 (Liquid)
| Mole fraction of Tetrahydropyran (2) - Liquid |
Speed of sound, m/s - Liquid |
| 0.0981 |
1054.0 |
| 0.1578 |
1067.0 |
| 0.1965 |
1075.0 |
| 0.2955 |
1093.0 |
| 0.3313 |
1099.0 |
| 0.3955 |
1110.0 |
| 0.4469 |
1118.0 |
| 0.4947 |
1126.0 |
| 0.5211 |
1130.0 |
| 0.5955 |
1143.0 |
| 0.6955 |
1161.0 |
| 0.7311 |
1168.0 |
| 0.7965 |
1181.0 |
| 0.8992 |
1203.0 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 308.15 (Liquid)
| Mole fraction of Tetrahydropyran (2) - Liquid |
Speed of sound, m/s - Liquid |
| 0.0981 |
1054.0 |
| 0.1578 |
1067.0 |
| 0.1965 |
1075.0 |
| 0.2955 |
1093.0 |
| 0.3313 |
1099.0 |
| 0.3955 |
1110.0 |
| 0.4469 |
1118.0 |
| 0.4947 |
1126.0 |
| 0.5211 |
1130.0 |
| 0.5955 |
1143.0 |
| 0.6955 |
1161.0 |
| 0.7311 |
1168.0 |
| 0.7965 |
1181.0 |
| 0.8992 |
1203.0 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
303.15 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0000 |
0.0271 |
| 0.0450 |
0.0265 |
| 0.0900 |
0.0256 |
| 0.1810 |
0.0244 |
| 0.2820 |
0.0232 |
| 0.3830 |
0.0220 |
| 0.4870 |
0.0211 |
| 0.5890 |
0.0204 |
| 0.6740 |
0.0195 |
| 0.7860 |
0.0188 |
| 0.8990 |
0.0181 |
| 0.9640 |
0.0175 |
| 1.0000 |
0.0174 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
303.15 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0000 |
0.0271 |
| 0.0450 |
0.0265 |
| 0.0900 |
0.0256 |
| 0.1810 |
0.0244 |
| 0.2820 |
0.0232 |
| 0.3830 |
0.0220 |
| 0.4870 |
0.0211 |
| 0.5890 |
0.0204 |
| 0.6740 |
0.0195 |
| 0.7860 |
0.0188 |
| 0.8990 |
0.0181 |
| 0.9640 |
0.0175 |
| 1.0000 |
0.0174 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of n-Hexane (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
50.00 |
339.33 |
| 0.0000 |
75.00 |
351.53 |
| 0.0000 |
94.00 |
358.85 |
| 0.0410 |
75.00 |
349.63 |
| 0.0420 |
50.00 |
337.38 |
| 0.0430 |
94.00 |
356.39 |
| 0.0850 |
94.00 |
354.78 |
| 0.0860 |
50.00 |
335.21 |
| 0.0860 |
75.00 |
347.45 |
| 0.1110 |
94.00 |
353.96 |
| 0.1130 |
75.00 |
346.64 |
| 0.1170 |
50.00 |
334.32 |
| 0.1560 |
94.00 |
352.27 |
| 0.1570 |
50.00 |
332.83 |
| 0.1570 |
75.00 |
345.04 |
| 0.1950 |
94.00 |
351.11 |
| 0.1980 |
75.00 |
343.86 |
| 0.2030 |
50.00 |
331.63 |
| 0.2410 |
94.00 |
349.92 |
| 0.2430 |
50.00 |
330.60 |
| 0.2440 |
75.00 |
342.67 |
| 0.2900 |
50.00 |
329.54 |
| 0.2900 |
75.00 |
341.57 |
| 0.2910 |
94.00 |
348.76 |
| 0.3340 |
75.00 |
340.34 |
| 0.3350 |
50.00 |
328.26 |
| 0.3350 |
94.00 |
347.61 |
| 0.3810 |
75.00 |
339.54 |
| 0.3820 |
94.00 |
346.69 |
| 0.3830 |
50.00 |
327.38 |
| 0.4280 |
94.00 |
345.86 |
| 0.4300 |
75.00 |
338.70 |
| 0.4330 |
50.00 |
326.67 |
| 0.4820 |
94.00 |
345.01 |
| 0.4830 |
75.00 |
337.86 |
| 0.4900 |
50.00 |
325.86 |
| 0.5430 |
94.00 |
344.14 |
| 0.5460 |
75.00 |
336.95 |
| 0.5480 |
50.00 |
325.10 |
| 0.5990 |
94.00 |
343.38 |
| 0.6060 |
75.00 |
336.15 |
| 0.6070 |
50.00 |
324.31 |
| 0.6620 |
94.00 |
342.61 |
| 0.6630 |
50.00 |
323.75 |
| 0.6630 |
75.00 |
335.54 |
| 0.7160 |
75.00 |
334.97 |
| 0.7160 |
94.00 |
342.02 |
| 0.7180 |
50.00 |
323.17 |
| 0.7730 |
50.00 |
322.76 |
| 0.7730 |
75.00 |
334.46 |
| 0.7730 |
94.00 |
341.43 |
| 0.8180 |
94.00 |
340.97 |
| 0.8190 |
75.00 |
334.04 |
| 0.8210 |
50.00 |
322.34 |
| 0.8670 |
75.00 |
333.63 |
| 0.8670 |
94.00 |
340.54 |
| 0.8680 |
50.00 |
321.95 |
| 0.9240 |
94.00 |
340.06 |
| 0.9260 |
50.00 |
321.49 |
| 0.9260 |
75.00 |
333.13 |
| 1.0000 |
50.00 |
321.03 |
| 1.0000 |
75.00 |
332.65 |
| 1.0000 |
94.00 |
339.57 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of n-Hexane (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
50.00 |
339.33 |
| 0.0000 |
75.00 |
351.53 |
| 0.0000 |
94.00 |
358.85 |
| 0.0410 |
75.00 |
349.63 |
| 0.0420 |
50.00 |
337.38 |
| 0.0430 |
94.00 |
356.39 |
| 0.0850 |
94.00 |
354.78 |
| 0.0860 |
50.00 |
335.21 |
| 0.0860 |
75.00 |
347.45 |
| 0.1110 |
94.00 |
353.96 |
| 0.1130 |
75.00 |
346.64 |
| 0.1170 |
50.00 |
334.32 |
| 0.1560 |
94.00 |
352.27 |
| 0.1570 |
50.00 |
332.83 |
| 0.1570 |
75.00 |
345.04 |
| 0.1950 |
94.00 |
351.11 |
| 0.1980 |
75.00 |
343.86 |
| 0.2030 |
50.00 |
331.63 |
| 0.2410 |
94.00 |
349.92 |
| 0.2430 |
50.00 |
330.60 |
| 0.2440 |
75.00 |
342.67 |
| 0.2900 |
50.00 |
329.54 |
| 0.2900 |
75.00 |
341.57 |
| 0.2910 |
94.00 |
348.76 |
| 0.3340 |
75.00 |
340.34 |
| 0.3350 |
50.00 |
328.26 |
| 0.3350 |
94.00 |
347.61 |
| 0.3810 |
75.00 |
339.54 |
| 0.3820 |
94.00 |
346.69 |
| 0.3830 |
50.00 |
327.38 |
| 0.4280 |
94.00 |
345.86 |
| 0.4300 |
75.00 |
338.70 |
| 0.4330 |
50.00 |
326.67 |
| 0.4820 |
94.00 |
345.01 |
| 0.4830 |
75.00 |
337.86 |
| 0.4900 |
50.00 |
325.86 |
| 0.5430 |
94.00 |
344.14 |
| 0.5460 |
75.00 |
336.95 |
| 0.5480 |
50.00 |
325.10 |
| 0.5990 |
94.00 |
343.38 |
| 0.6060 |
75.00 |
336.15 |
| 0.6070 |
50.00 |
324.31 |
| 0.6620 |
94.00 |
342.61 |
| 0.6630 |
50.00 |
323.75 |
| 0.6630 |
75.00 |
335.54 |
| 0.7160 |
75.00 |
334.97 |
| 0.7160 |
94.00 |
342.02 |
| 0.7180 |
50.00 |
323.17 |
| 0.7730 |
50.00 |
322.76 |
| 0.7730 |
75.00 |
334.46 |
| 0.7730 |
94.00 |
341.43 |
| 0.8180 |
94.00 |
340.97 |
| 0.8190 |
75.00 |
334.04 |
| 0.8210 |
50.00 |
322.34 |
| 0.8670 |
75.00 |
333.63 |
| 0.8670 |
94.00 |
340.54 |
| 0.8680 |
50.00 |
321.95 |
| 0.9240 |
94.00 |
340.06 |
| 0.9260 |
50.00 |
321.49 |
| 0.9260 |
75.00 |
333.13 |
| 1.0000 |
50.00 |
321.03 |
| 1.0000 |
75.00 |
332.65 |
| 1.0000 |
94.00 |
339.57 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 308.15 (Liquid)
| Mole fraction of Tetrahydropyran (2) - Liquid |
Excess molar volume, m3/mol - Liquid |
| 0.0328 |
1.4000e-08 |
| 0.0459 |
1.9000e-08 |
| 0.0694 |
2.7000e-08 |
| 0.0785 |
3.0000e-08 |
| 0.1294 |
4.4000e-08 |
| 0.1561 |
4.9000e-08 |
| 0.2753 |
6.4000e-08 |
| 0.3262 |
6.6000e-08 |
| 0.4629 |
6.2000e-08 |
| 0.5150 |
5.8000e-08 |
| 0.6692 |
4.2000e-08 |
| 0.7837 |
2.8000e-08 |
| 0.8461 |
2.0000e-08 |
| 0.9239 |
1.0000e-08 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 308.15 (Liquid)
| Mole fraction of Tetrahydropyran (2) - Liquid |
Excess molar volume, m3/mol - Liquid |
| 0.0328 |
1.4000e-08 |
| 0.0459 |
1.9000e-08 |
| 0.0694 |
2.7000e-08 |
| 0.0785 |
3.0000e-08 |
| 0.1294 |
4.4000e-08 |
| 0.1561 |
4.9000e-08 |
| 0.2753 |
6.4000e-08 |
| 0.3262 |
6.6000e-08 |
| 0.4629 |
6.2000e-08 |
| 0.5150 |
5.8000e-08 |
| 0.6692 |
4.2000e-08 |
| 0.7837 |
2.8000e-08 |
| 0.8461 |
2.0000e-08 |
| 0.9239 |
1.0000e-08 |
Sources
-
Experimental determination and theoretical modeling of the vapor-liquid equilibrium and surface tensions of hexane + tetrahydro-2H-pyran
-
Thermodynamic properties of binary mixtures containing Tetrahydropyran: Excess molar volumes, Excess molar enthalpies and isentropic compressibilities changes of mixing
-
Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
