Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Pressure, kPa - Gas | Mole fraction of Ethane, 1,2-dibromo- (1) - Gas |
0.0000 | 101.33 | 0.0000 |
0.0437 | 101.32 | 0.0646 |
0.1031 | 101.30 | 0.1472 |
0.1435 | 101.30 | 0.2008 |
0.2011 | 101.29 | 0.2733 |
0.2472 | 101.29 | 0.3280 |
0.2920 | 101.40 | 0.3796 |
0.3674 | 101.42 | 0.4622 |
0.4442 | 101.43 | 0.5411 |
0.5211 | 101.42 | 0.6159 |
0.5822 | 101.42 | 0.6717 |
0.6273 | 101.43 | 0.7119 |
0.7382 | 101.41 | 0.8051 |
0.8220 | 101.42 | 0.8711 |
0.8688 | 101.41 | 0.9064 |
0.9684 | 101.39 | 0.9782 |
1.0000 | 101.37 | 1.0000 |
Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Pressure, kPa - Gas | Mole fraction of Ethane, 1,2-dibromo- (1) - Gas |
0.0000 | 101.33 | 0.0000 |
0.0437 | 101.32 | 0.0646 |
0.1031 | 101.30 | 0.1472 |
0.1435 | 101.30 | 0.2008 |
0.2011 | 101.29 | 0.2733 |
0.2472 | 101.29 | 0.3280 |
0.2920 | 101.40 | 0.3796 |
0.3674 | 101.42 | 0.4622 |
0.4442 | 101.43 | 0.5411 |
0.5211 | 101.42 | 0.6159 |
0.5822 | 101.42 | 0.6717 |
0.6273 | 101.43 | 0.7119 |
0.7382 | 101.41 | 0.8051 |
0.8220 | 101.42 | 0.8711 |
0.8688 | 101.41 | 0.9064 |
0.9684 | 101.39 | 0.9782 |
1.0000 | 101.37 | 1.0000 |
Operational conditions:
Volume fraction of Ethane, 1,2-dibromo- (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1133.1 |
0.0736 | 1123.4 |
0.1308 | 1112.7 |
0.2625 | 1092.9 |
0.3958 | 1069.6 |
0.4864 | 1054.5 |
0.6302 | 1031.7 |
0.7156 | 1019.7 |
0.8950 | 995.0 |
1.0000 | 984.0 |
Operational conditions:
Volume fraction of Ethane, 1,2-dibromo- (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1133.1 |
0.0736 | 1123.4 |
0.1308 | 1112.7 |
0.2625 | 1092.9 |
0.3958 | 1069.6 |
0.4864 | 1054.5 |
0.6302 | 1031.7 |
0.7156 | 1019.7 |
0.8950 | 995.0 |
1.0000 | 984.0 |
Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Pressure, kPa - Liquid | Boiling temperature at pressure P, K - Liquid |
0.0000 | 101.33 | 418.60 |
0.0437 | 101.32 | 417.90 |
0.1031 | 101.30 | 416.80 |
0.1435 | 101.30 | 416.10 |
0.2011 | 101.29 | 415.10 |
0.2472 | 101.29 | 414.40 |
0.2920 | 101.40 | 414.00 |
0.3674 | 101.42 | 413.00 |
0.4442 | 101.43 | 411.80 |
0.5211 | 101.42 | 410.70 |
0.5822 | 101.42 | 409.90 |
0.6273 | 101.43 | 409.30 |
0.7382 | 101.41 | 407.80 |
0.8220 | 101.42 | 406.80 |
0.8688 | 101.41 | 406.10 |
0.9684 | 101.39 | 404.90 |
1.0000 | 101.37 | 404.40 |
Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Pressure, kPa - Liquid | Boiling temperature at pressure P, K - Liquid |
0.0000 | 101.33 | 418.60 |
0.0437 | 101.32 | 417.90 |
0.1031 | 101.30 | 416.80 |
0.1435 | 101.30 | 416.10 |
0.2011 | 101.29 | 415.10 |
0.2472 | 101.29 | 414.40 |
0.2920 | 101.40 | 414.00 |
0.3674 | 101.42 | 413.00 |
0.4442 | 101.43 | 411.80 |
0.5211 | 101.42 | 410.70 |
0.5822 | 101.42 | 409.90 |
0.6273 | 101.43 | 409.30 |
0.7382 | 101.41 | 407.80 |
0.8220 | 101.42 | 406.80 |
0.8688 | 101.41 | 406.10 |
0.9684 | 101.39 | 404.90 |
1.0000 | 101.37 | 404.40 |
Operational conditions:
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0885 | -5.2000e-08 |
0.1554 | -9.0000e-08 |
0.3032 | -1.5600e-07 |
0.4447 | -1.7100e-07 |
0.5365 | -1.5600e-07 |
0.6757 | -9.8000e-08 |
0.7546 | -5.9000e-08 |
0.9124 | -0.0000 |
Operational conditions:
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Excess molar volume, m3/mol - Liquid |
---|---|
0.0885 | -5.2000e-08 |
0.1554 | -9.0000e-08 |
0.3032 | -1.5600e-07 |
0.4447 | -1.7100e-07 |
0.5365 | -1.5600e-07 |
0.6757 | -9.8000e-08 |
0.7546 | -5.9000e-08 |
0.9124 | -0.0000 |