Datasets
-
Mole fraction (2)
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (2)
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 |
| 0.0450 |
94.00 |
0.1310 |
| 0.0470 |
50.00 |
0.1490 |
| 0.0470 |
75.00 |
0.1370 |
| 0.0910 |
75.00 |
0.2380 |
| 0.0920 |
94.00 |
0.2290 |
| 0.0960 |
50.00 |
0.2680 |
| 0.1420 |
50.00 |
0.3510 |
| 0.1420 |
75.00 |
0.3360 |
| 0.1420 |
94.00 |
0.3230 |
| 0.1920 |
50.00 |
0.4280 |
| 0.1940 |
75.00 |
0.4130 |
| 0.1940 |
94.00 |
0.4020 |
| 0.2400 |
94.00 |
0.4620 |
| 0.2410 |
50.00 |
0.4890 |
| 0.2410 |
75.00 |
0.4690 |
| 0.2850 |
94.00 |
0.5140 |
| 0.2880 |
50.00 |
0.5380 |
| 0.2880 |
75.00 |
0.5250 |
| 0.3380 |
50.00 |
0.5910 |
| 0.3390 |
94.00 |
0.5650 |
| 0.3420 |
75.00 |
0.5810 |
| 0.3850 |
94.00 |
0.6140 |
| 0.3890 |
75.00 |
0.6150 |
| 0.3900 |
50.00 |
0.6440 |
| 0.4400 |
75.00 |
0.6660 |
| 0.4410 |
50.00 |
0.6780 |
| 0.4440 |
94.00 |
0.6560 |
| 0.4790 |
50.00 |
0.6970 |
| 0.4850 |
75.00 |
0.6920 |
| 0.4890 |
94.00 |
0.6860 |
| 0.5300 |
50.00 |
0.7300 |
| 0.5400 |
75.00 |
0.7270 |
| 0.5400 |
94.00 |
0.7250 |
| 0.6040 |
94.00 |
0.7600 |
| 0.6080 |
75.00 |
0.7690 |
| 0.6160 |
50.00 |
0.7800 |
| 0.6610 |
94.00 |
0.7950 |
| 0.6620 |
75.00 |
0.8000 |
| 0.6630 |
50.00 |
0.8090 |
| 0.6990 |
75.00 |
0.8220 |
| 0.7010 |
94.00 |
0.8170 |
| 0.7070 |
75.00 |
0.8260 |
| 0.7080 |
50.00 |
0.8340 |
| 0.7570 |
94.00 |
0.8530 |
| 0.7600 |
50.00 |
0.8630 |
| 0.7890 |
75.00 |
0.8730 |
| 0.7900 |
50.00 |
0.8790 |
| 0.8030 |
94.00 |
0.8780 |
| 0.8110 |
75.00 |
0.8860 |
| 0.8520 |
94.00 |
0.9080 |
| 0.8530 |
75.00 |
0.9090 |
| 0.8550 |
50.00 |
0.9140 |
| 0.8950 |
75.00 |
0.9340 |
| 0.8950 |
94.00 |
0.9330 |
| 0.8960 |
50.00 |
0.9370 |
| 0.9370 |
94.00 |
0.9590 |
| 0.9390 |
75.00 |
0.9600 |
| 0.9400 |
50.00 |
0.9630 |
| 1.0000 |
50.00 |
1.0000 |
| 1.0000 |
75.00 |
1.0000 |
| 1.0000 |
94.00 |
1.0000 |
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 |
| 0.0450 |
94.00 |
0.1310 |
| 0.0470 |
50.00 |
0.1490 |
| 0.0470 |
75.00 |
0.1370 |
| 0.0910 |
75.00 |
0.2380 |
| 0.0920 |
94.00 |
0.2290 |
| 0.0960 |
50.00 |
0.2680 |
| 0.1420 |
50.00 |
0.3510 |
| 0.1420 |
75.00 |
0.3360 |
| 0.1420 |
94.00 |
0.3230 |
| 0.1920 |
50.00 |
0.4280 |
| 0.1940 |
75.00 |
0.4130 |
| 0.1940 |
94.00 |
0.4020 |
| 0.2400 |
94.00 |
0.4620 |
| 0.2410 |
50.00 |
0.4890 |
| 0.2410 |
75.00 |
0.4690 |
| 0.2850 |
94.00 |
0.5140 |
| 0.2880 |
50.00 |
0.5380 |
| 0.2880 |
75.00 |
0.5250 |
| 0.3380 |
50.00 |
0.5910 |
| 0.3390 |
94.00 |
0.5650 |
| 0.3420 |
75.00 |
0.5810 |
| 0.3850 |
94.00 |
0.6140 |
| 0.3890 |
75.00 |
0.6150 |
| 0.3900 |
50.00 |
0.6440 |
| 0.4400 |
75.00 |
0.6660 |
| 0.4410 |
50.00 |
0.6780 |
| 0.4440 |
94.00 |
0.6560 |
| 0.4790 |
50.00 |
0.6970 |
| 0.4850 |
75.00 |
0.6920 |
| 0.4890 |
94.00 |
0.6860 |
| 0.5300 |
50.00 |
0.7300 |
| 0.5400 |
75.00 |
0.7270 |
| 0.5400 |
94.00 |
0.7250 |
| 0.6040 |
94.00 |
0.7600 |
| 0.6080 |
75.00 |
0.7690 |
| 0.6160 |
50.00 |
0.7800 |
| 0.6610 |
94.00 |
0.7950 |
| 0.6620 |
75.00 |
0.8000 |
| 0.6630 |
50.00 |
0.8090 |
| 0.6990 |
75.00 |
0.8220 |
| 0.7010 |
94.00 |
0.8170 |
| 0.7070 |
75.00 |
0.8260 |
| 0.7080 |
50.00 |
0.8340 |
| 0.7570 |
94.00 |
0.8530 |
| 0.7600 |
50.00 |
0.8630 |
| 0.7890 |
75.00 |
0.8730 |
| 0.7900 |
50.00 |
0.8790 |
| 0.8030 |
94.00 |
0.8780 |
| 0.8110 |
75.00 |
0.8860 |
| 0.8520 |
94.00 |
0.9080 |
| 0.8530 |
75.00 |
0.9090 |
| 0.8550 |
50.00 |
0.9140 |
| 0.8950 |
75.00 |
0.9340 |
| 0.8950 |
94.00 |
0.9330 |
| 0.8960 |
50.00 |
0.9370 |
| 0.9370 |
94.00 |
0.9590 |
| 0.9390 |
75.00 |
0.9600 |
| 0.9400 |
50.00 |
0.9630 |
| 1.0000 |
50.00 |
1.0000 |
| 1.0000 |
75.00 |
1.0000 |
| 1.0000 |
94.00 |
1.0000 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
895.7 |
| 0.0580 |
878.43 |
| 0.1030 |
865.07 |
| 0.1690 |
846.48 |
| 0.2110 |
834.86 |
| 0.2840 |
815.33 |
| 0.3260 |
804.35 |
| 0.3730 |
792.42 |
| 0.4250 |
779.22 |
| 0.4740 |
767.35 |
| 0.5230 |
755.53 |
| 0.5770 |
743.04 |
| 0.6710 |
722.12 |
| 0.7300 |
709.38 |
| 0.8540 |
683.63 |
| 0.9150 |
671.56 |
| 0.9790 |
659.09 |
| 1.0000 |
655.17 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
895.7 |
| 0.0580 |
878.43 |
| 0.1030 |
865.07 |
| 0.1690 |
846.48 |
| 0.2110 |
834.86 |
| 0.2840 |
815.33 |
| 0.3260 |
804.35 |
| 0.3730 |
792.42 |
| 0.4250 |
779.22 |
| 0.4740 |
767.35 |
| 0.5230 |
755.53 |
| 0.5770 |
743.04 |
| 0.6710 |
722.12 |
| 0.7300 |
709.38 |
| 0.8540 |
683.63 |
| 0.9150 |
671.56 |
| 0.9790 |
659.09 |
| 1.0000 |
655.17 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0000 |
0.0236 |
| 0.0480 |
0.0223 |
| 0.0950 |
0.0216 |
| 0.1890 |
0.0208 |
| 0.2950 |
0.0201 |
| 0.3970 |
0.0194 |
| 0.5020 |
0.0191 |
| 0.6060 |
0.0187 |
| 0.7230 |
0.0184 |
| 0.8110 |
0.0181 |
| 0.9150 |
0.0178 |
| 0.9700 |
0.0175 |
| 1.0000 |
0.0174 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0000 |
0.0236 |
| 0.0480 |
0.0223 |
| 0.0950 |
0.0216 |
| 0.1890 |
0.0208 |
| 0.2950 |
0.0201 |
| 0.3970 |
0.0194 |
| 0.5020 |
0.0191 |
| 0.6060 |
0.0187 |
| 0.7230 |
0.0184 |
| 0.8110 |
0.0181 |
| 0.9150 |
0.0178 |
| 0.9700 |
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 |
345.24 |
| 0.0000 |
75.00 |
357.21 |
| 0.0000 |
94.00 |
364.37 |
| 0.0450 |
94.00 |
361.54 |
| 0.0470 |
50.00 |
342.40 |
| 0.0470 |
75.00 |
354.35 |
| 0.0910 |
75.00 |
352.01 |
| 0.0920 |
94.00 |
359.14 |
| 0.0960 |
50.00 |
339.73 |
| 0.1420 |
50.00 |
337.71 |
| 0.1420 |
75.00 |
349.69 |
| 0.1420 |
94.00 |
356.83 |
| 0.1920 |
50.00 |
335.71 |
| 0.1940 |
75.00 |
347.71 |
| 0.1940 |
94.00 |
354.81 |
| 0.2400 |
94.00 |
353.25 |
| 0.2410 |
50.00 |
334.11 |
| 0.2410 |
75.00 |
346.06 |
| 0.2850 |
94.00 |
351.86 |
| 0.2880 |
50.00 |
332.73 |
| 0.2880 |
75.00 |
344.66 |
| 0.3380 |
50.00 |
331.38 |
| 0.3390 |
94.00 |
350.40 |
| 0.3420 |
75.00 |
343.16 |
| 0.3850 |
94.00 |
349.11 |
| 0.3890 |
75.00 |
342.12 |
| 0.3900 |
50.00 |
330.04 |
| 0.4400 |
75.00 |
340.75 |
| 0.4410 |
50.00 |
328.89 |
| 0.4440 |
94.00 |
347.80 |
| 0.4790 |
50.00 |
328.23 |
| 0.4850 |
75.00 |
339.96 |
| 0.4890 |
94.00 |
346.99 |
| 0.5300 |
50.00 |
327.31 |
| 0.5400 |
75.00 |
338.93 |
| 0.5400 |
94.00 |
345.84 |
| 0.6040 |
94.00 |
344.84 |
| 0.6080 |
75.00 |
337.68 |
| 0.6160 |
50.00 |
325.72 |
| 0.6610 |
94.00 |
343.96 |
| 0.6620 |
75.00 |
336.84 |
| 0.6630 |
50.00 |
325.00 |
| 0.6990 |
75.00 |
336.30 |
| 0.7010 |
94.00 |
343.36 |
| 0.7070 |
75.00 |
336.20 |
| 0.7080 |
50.00 |
324.36 |
| 0.7570 |
94.00 |
342.57 |
| 0.7600 |
50.00 |
323.60 |
| 0.7890 |
75.00 |
335.07 |
| 0.7900 |
50.00 |
323.26 |
| 0.8030 |
94.00 |
341.87 |
| 0.8110 |
75.00 |
334.79 |
| 0.8520 |
94.00 |
341.23 |
| 0.8530 |
75.00 |
334.25 |
| 0.8550 |
50.00 |
322.46 |
| 0.8950 |
75.00 |
333.69 |
| 0.8950 |
94.00 |
340.69 |
| 0.8960 |
50.00 |
321.97 |
| 0.9370 |
94.00 |
340.17 |
| 0.9390 |
75.00 |
333.21 |
| 0.9400 |
50.00 |
321.55 |
| 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 |
345.24 |
| 0.0000 |
75.00 |
357.21 |
| 0.0000 |
94.00 |
364.37 |
| 0.0450 |
94.00 |
361.54 |
| 0.0470 |
50.00 |
342.40 |
| 0.0470 |
75.00 |
354.35 |
| 0.0910 |
75.00 |
352.01 |
| 0.0920 |
94.00 |
359.14 |
| 0.0960 |
50.00 |
339.73 |
| 0.1420 |
50.00 |
337.71 |
| 0.1420 |
75.00 |
349.69 |
| 0.1420 |
94.00 |
356.83 |
| 0.1920 |
50.00 |
335.71 |
| 0.1940 |
75.00 |
347.71 |
| 0.1940 |
94.00 |
354.81 |
| 0.2400 |
94.00 |
353.25 |
| 0.2410 |
50.00 |
334.11 |
| 0.2410 |
75.00 |
346.06 |
| 0.2850 |
94.00 |
351.86 |
| 0.2880 |
50.00 |
332.73 |
| 0.2880 |
75.00 |
344.66 |
| 0.3380 |
50.00 |
331.38 |
| 0.3390 |
94.00 |
350.40 |
| 0.3420 |
75.00 |
343.16 |
| 0.3850 |
94.00 |
349.11 |
| 0.3890 |
75.00 |
342.12 |
| 0.3900 |
50.00 |
330.04 |
| 0.4400 |
75.00 |
340.75 |
| 0.4410 |
50.00 |
328.89 |
| 0.4440 |
94.00 |
347.80 |
| 0.4790 |
50.00 |
328.23 |
| 0.4850 |
75.00 |
339.96 |
| 0.4890 |
94.00 |
346.99 |
| 0.5300 |
50.00 |
327.31 |
| 0.5400 |
75.00 |
338.93 |
| 0.5400 |
94.00 |
345.84 |
| 0.6040 |
94.00 |
344.84 |
| 0.6080 |
75.00 |
337.68 |
| 0.6160 |
50.00 |
325.72 |
| 0.6610 |
94.00 |
343.96 |
| 0.6620 |
75.00 |
336.84 |
| 0.6630 |
50.00 |
325.00 |
| 0.6990 |
75.00 |
336.30 |
| 0.7010 |
94.00 |
343.36 |
| 0.7070 |
75.00 |
336.20 |
| 0.7080 |
50.00 |
324.36 |
| 0.7570 |
94.00 |
342.57 |
| 0.7600 |
50.00 |
323.60 |
| 0.7890 |
75.00 |
335.07 |
| 0.7900 |
50.00 |
323.26 |
| 0.8030 |
94.00 |
341.87 |
| 0.8110 |
75.00 |
334.79 |
| 0.8520 |
94.00 |
341.23 |
| 0.8530 |
75.00 |
334.25 |
| 0.8550 |
50.00 |
322.46 |
| 0.8950 |
75.00 |
333.69 |
| 0.8950 |
94.00 |
340.69 |
| 0.8960 |
50.00 |
321.97 |
| 0.9370 |
94.00 |
340.17 |
| 0.9390 |
75.00 |
333.21 |
| 0.9400 |
50.00 |
321.55 |
| 1.0000 |
50.00 |
321.03 |
| 1.0000 |
75.00 |
332.65 |
| 1.0000 |
94.00 |
339.57 |
Sources