Operational condition: Pressure, kPa = 20 (Liquid)
| Mole fraction of Octane (2) - Liquid | Mole fraction of Octane (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0420 | 0.0680 |
| 0.1280 | 0.1930 |
| 0.2020 | 0.2890 |
| 0.2790 | 0.3790 |
| 0.3620 | 0.4690 |
| 0.4310 | 0.5380 |
| 0.5050 | 0.6080 |
| 0.5780 | 0.6730 |
| 0.6540 | 0.7370 |
| 0.7330 | 0.8010 |
| 0.8190 | 0.8680 |
| 0.8820 | 0.9150 |
| 0.9480 | 0.9630 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Octane (2) - Liquid | Mole fraction of Octane (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0380 | 0.0640 |
| 0.1310 | 0.1910 |
| 0.2490 | 0.3380 |
| 0.3200 | 0.4130 |
| 0.3510 | 0.4380 |
| 0.4500 | 0.5400 |
| 0.5560 | 0.6320 |
| 0.6590 | 0.7180 |
| 0.7410 | 0.7830 |
| 0.8430 | 0.8690 |
| 0.9340 | 0.9480 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 20 (Liquid)
| Mole fraction of Octane (2) - Liquid | Mole fraction of Octane (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0420 | 0.0680 |
| 0.1280 | 0.1930 |
| 0.2020 | 0.2890 |
| 0.2790 | 0.3790 |
| 0.3620 | 0.4690 |
| 0.4310 | 0.5380 |
| 0.5050 | 0.6080 |
| 0.5780 | 0.6730 |
| 0.6540 | 0.7370 |
| 0.7330 | 0.8010 |
| 0.8190 | 0.8680 |
| 0.8820 | 0.9150 |
| 0.9480 | 0.9630 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Octane (2) - Liquid | Mole fraction of Octane (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0380 | 0.0640 |
| 0.1310 | 0.1910 |
| 0.2490 | 0.3380 |
| 0.3200 | 0.4130 |
| 0.3510 | 0.4380 |
| 0.4500 | 0.5400 |
| 0.5560 | 0.6320 |
| 0.6590 | 0.7180 |
| 0.7410 | 0.7830 |
| 0.8430 | 0.8690 |
| 0.9340 | 0.9480 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Octane (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 859.85 |
| 298.15 | 0.0664 | 845.86 |
| 298.15 | 0.1397 | 831.1 |
| 298.15 | 0.2052 | 818.49 |
| 298.15 | 0.2760 | 805.42 |
| 298.15 | 0.3230 | 797.05 |
| 298.15 | 0.3982 | 784.13 |
| 298.15 | 0.4618 | 773.65 |
| 298.15 | 0.5432 | 760.8 |
| 298.15 | 0.5993 | 752.28 |
| 298.15 | 0.6755 | 741.14 |
| 298.15 | 0.7284 | 733.68 |
| 298.15 | 0.7851 | 725.91 |
| 298.15 | 0.8583 | 716.27 |
| 298.15 | 0.9250 | 707.79 |
| 298.15 | 1.0000 | 698.63 |
| 308.15 | 0.0000 | 851.2 |
| 308.15 | 0.0664 | 837.23 |
| 308.15 | 0.1397 | 822.5 |
| 308.15 | 0.2052 | 809.92 |
| 308.15 | 0.2760 | 796.89 |
| 308.15 | 0.3230 | 788.53 |
| 308.15 | 0.3954 | 776.12 |
| 308.15 | 0.4618 | 765.21 |
| 308.15 | 0.5432 | 752.4 |
| 308.15 | 0.5993 | 743.9 |
| 308.15 | 0.6755 | 732.79 |
| 308.15 | 0.7284 | 725.36 |
| 308.15 | 0.7851 | 717.64 |
| 308.15 | 0.8583 | 708.01 |
| 308.15 | 0.9250 | 699.57 |
| 308.15 | 1.0000 | 690.43 |
| 318.15 | 0.0000 | 842.66 |
| 318.15 | 0.0687 | 828.23 |
| 318.15 | 0.1168 | 818.54 |
| 318.15 | 0.2070 | 801.13 |
| 318.15 | 0.2651 | 790.45 |
| 318.15 | 0.3289 | 779.13 |
| 318.15 | 0.4087 | 765.6 |
| 318.15 | 0.4672 | 756.08 |
| 318.15 | 0.5321 | 745.88 |
| 318.15 | 0.6067 | 734.61 |
| 318.15 | 0.6634 | 726.39 |
| 318.15 | 0.7288 | 717.2 |
| 318.15 | 0.7923 | 708.59 |
| 318.15 | 0.8634 | 699.33 |
| 318.15 | 0.9502 | 688.48 |
| 318.15 | 1.0000 | 682.49 |
| 328.15 | 0.0000 | 834.13 |
| 328.15 | 0.0687 | 819.75 |
| 328.15 | 0.1168 | 810.1 |
| 328.15 | 0.2070 | 792.73 |
| 328.15 | 0.2651 | 782.09 |
| 328.15 | 0.3289 | 770.81 |
| 328.15 | 0.4087 | 757.32 |
| 328.15 | 0.4672 | 747.81 |
| 328.15 | 0.5287 | 738.2 |
| 328.15 | 0.6067 | 726.45 |
| 328.15 | 0.6634 | 718.26 |
| 328.15 | 0.7288 | 709.11 |
| 328.15 | 0.7923 | 700.55 |
| 328.15 | 0.8634 | 691.33 |
| 328.15 | 0.9502 | 680.52 |
| 328.15 | 1.0000 | 674.56 |
Operational conditions:
| Mole fraction of Benzene, 1,3-dimethyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.1000 | 714.96 |
| 0.2035 | 728.42 |
| 0.3029 | 742.19 |
| 0.4105 | 759.36 |
| 0.4990 | 771.74 |
| 0.6017 | 788.49 |
| 0.6969 | 804.93 |
| 0.7995 | 823.73 |
| 0.9001 | 843.33 |
| 1.0000 | 864.16 |
| 0.0000 | 702.93 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Octane (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 859.85 |
| 298.15 | 0.0664 | 845.86 |
| 298.15 | 0.1397 | 831.1 |
| 298.15 | 0.2052 | 818.49 |
| 298.15 | 0.2760 | 805.42 |
| 298.15 | 0.3230 | 797.05 |
| 298.15 | 0.3982 | 784.13 |
| 298.15 | 0.4618 | 773.65 |
| 298.15 | 0.5432 | 760.8 |
| 298.15 | 0.5993 | 752.28 |
| 298.15 | 0.6755 | 741.14 |
| 298.15 | 0.7284 | 733.68 |
| 298.15 | 0.7851 | 725.91 |
| 298.15 | 0.8583 | 716.27 |
| 298.15 | 0.9250 | 707.79 |
| 298.15 | 1.0000 | 698.63 |
| 308.15 | 0.0000 | 851.2 |
| 308.15 | 0.0664 | 837.23 |
| 308.15 | 0.1397 | 822.5 |
| 308.15 | 0.2052 | 809.92 |
| 308.15 | 0.2760 | 796.89 |
| 308.15 | 0.3230 | 788.53 |
| 308.15 | 0.3954 | 776.12 |
| 308.15 | 0.4618 | 765.21 |
| 308.15 | 0.5432 | 752.4 |
| 308.15 | 0.5993 | 743.9 |
| 308.15 | 0.6755 | 732.79 |
| 308.15 | 0.7284 | 725.36 |
| 308.15 | 0.7851 | 717.64 |
| 308.15 | 0.8583 | 708.01 |
| 308.15 | 0.9250 | 699.57 |
| 308.15 | 1.0000 | 690.43 |
| 318.15 | 0.0000 | 842.66 |
| 318.15 | 0.0687 | 828.23 |
| 318.15 | 0.1168 | 818.54 |
| 318.15 | 0.2070 | 801.13 |
| 318.15 | 0.2651 | 790.45 |
| 318.15 | 0.3289 | 779.13 |
| 318.15 | 0.4087 | 765.6 |
| 318.15 | 0.4672 | 756.08 |
| 318.15 | 0.5321 | 745.88 |
| 318.15 | 0.6067 | 734.61 |
| 318.15 | 0.6634 | 726.39 |
| 318.15 | 0.7288 | 717.2 |
| 318.15 | 0.7923 | 708.59 |
| 318.15 | 0.8634 | 699.33 |
| 318.15 | 0.9502 | 688.48 |
| 318.15 | 1.0000 | 682.49 |
| 328.15 | 0.0000 | 834.13 |
| 328.15 | 0.0687 | 819.75 |
| 328.15 | 0.1168 | 810.1 |
| 328.15 | 0.2070 | 792.73 |
| 328.15 | 0.2651 | 782.09 |
| 328.15 | 0.3289 | 770.81 |
| 328.15 | 0.4087 | 757.32 |
| 328.15 | 0.4672 | 747.81 |
| 328.15 | 0.5287 | 738.2 |
| 328.15 | 0.6067 | 726.45 |
| 328.15 | 0.6634 | 718.26 |
| 328.15 | 0.7288 | 709.11 |
| 328.15 | 0.7923 | 700.55 |
| 328.15 | 0.8634 | 691.33 |
| 328.15 | 0.9502 | 680.52 |
| 328.15 | 1.0000 | 674.56 |
Operational conditions:
| Mole fraction of Benzene, 1,3-dimethyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.1000 | 714.96 |
| 0.2035 | 728.42 |
| 0.3029 | 742.19 |
| 0.4105 | 759.36 |
| 0.4990 | 771.74 |
| 0.6017 | 788.49 |
| 0.6969 | 804.93 |
| 0.7995 | 823.73 |
| 0.9001 | 843.33 |
| 1.0000 | 864.16 |
| 0.0000 | 702.93 |
Operational condition: Temperature, K = 293.15 (Liquid)
| Mole fraction of Benzene, 1,3-dimethyl- (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.1000 | 0.0220 |
| 0.2035 | 0.0224 |
| 0.3029 | 0.0228 |
| 0.4105 | 0.0233 |
| 0.4990 | 0.0239 |
| 0.6017 | 0.0245 |
| 0.6969 | 0.0253 |
| 0.7995 | 0.0263 |
| 0.9001 | 0.0274 |
| 1.0000 | 0.0287 |
| 0.0000 | 0.0217 |
Operational condition: Temperature, K = 293.15 (Liquid)
| Mole fraction of Benzene, 1,3-dimethyl- (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.1000 | 0.0220 |
| 0.2035 | 0.0224 |
| 0.3029 | 0.0228 |
| 0.4105 | 0.0233 |
| 0.4990 | 0.0239 |
| 0.6017 | 0.0245 |
| 0.6969 | 0.0253 |
| 0.7995 | 0.0263 |
| 0.9001 | 0.0274 |
| 1.0000 | 0.0287 |
| 0.0000 | 0.0217 |
Operational condition: Pressure, kPa = 20 (Liquid)
| Mole fraction of Octane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 360.59 |
| 0.0420 | 359.83 |
| 0.1280 | 358.41 |
| 0.2020 | 357.31 |
| 0.2790 | 356.27 |
| 0.3620 | 355.23 |
| 0.4310 | 354.43 |
| 0.5050 | 353.62 |
| 0.5780 | 352.87 |
| 0.6540 | 352.13 |
| 0.7330 | 351.39 |
| 0.8190 | 350.63 |
| 0.8820 | 350.09 |
| 0.9480 | 349.55 |
| 1.0000 | 349.13 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Octane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 412.30 |
| 0.0380 | 411.40 |
| 0.1310 | 409.80 |
| 0.2490 | 407.30 |
| 0.3200 | 406.20 |
| 0.3510 | 405.50 |
| 0.4500 | 403.90 |
| 0.5560 | 402.50 |
| 0.6590 | 401.60 |
| 0.7410 | 400.90 |
| 0.8430 | 400.00 |
| 0.9340 | 399.20 |
| 1.0000 | 398.80 |
Operational condition: Pressure, kPa = 20 (Liquid)
| Mole fraction of Octane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 360.59 |
| 0.0420 | 359.83 |
| 0.1280 | 358.41 |
| 0.2020 | 357.31 |
| 0.2790 | 356.27 |
| 0.3620 | 355.23 |
| 0.4310 | 354.43 |
| 0.5050 | 353.62 |
| 0.5780 | 352.87 |
| 0.6540 | 352.13 |
| 0.7330 | 351.39 |
| 0.8190 | 350.63 |
| 0.8820 | 350.09 |
| 0.9480 | 349.55 |
| 1.0000 | 349.13 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Octane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 412.30 |
| 0.0380 | 411.40 |
| 0.1310 | 409.80 |
| 0.2490 | 407.30 |
| 0.3200 | 406.20 |
| 0.3510 | 405.50 |
| 0.4500 | 403.90 |
| 0.5560 | 402.50 |
| 0.6590 | 401.60 |
| 0.7410 | 400.90 |
| 0.8430 | 400.00 |
| 0.9340 | 399.20 |
| 1.0000 | 398.80 |