Operational condition: Pressure, kPa = 60 (Liquid)
Mole fraction of Butane, 1-ethoxy- (1) - Liquid | Mole fraction of Butane, 1-ethoxy- (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0000 | 0.0000 |
0.0260 | 0.0350 |
0.0350 | 0.0490 |
0.0710 | 0.0950 |
0.0820 | 0.1110 |
0.1210 | 0.1600 |
0.1270 | 0.1660 |
0.1690 | 0.2120 |
0.1970 | 0.2450 |
0.1950 | 0.2480 |
0.2360 | 0.2930 |
0.2500 | 0.3050 |
0.2850 | 0.3440 |
0.2890 | 0.3480 |
0.3360 | 0.3950 |
0.3460 | 0.4000 |
0.3570 | 0.4130 |
0.3810 | 0.4360 |
0.4030 | 0.4590 |
0.4100 | 0.4660 |
0.4230 | 0.4790 |
0.4440 | 0.5040 |
0.4550 | 0.5110 |
0.4720 | 0.5250 |
0.4750 | 0.5280 |
0.4900 | 0.5430 |
0.4880 | 0.5460 |
0.5280 | 0.5790 |
0.5650 | 0.6150 |
0.6030 | 0.6440 |
0.6440 | 0.6800 |
0.6840 | 0.7160 |
0.7210 | 0.7490 |
0.7600 | 0.7830 |
0.7900 | 0.8110 |
0.8350 | 0.8510 |
0.8670 | 0.8790 |
0.9210 | 0.9270 |
0.9600 | 0.9630 |
0.9840 | 0.9850 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 60 (Liquid)
Mole fraction of Butane, 1-ethoxy- (1) - Liquid | Mole fraction of Butane, 1-ethoxy- (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0000 | 0.0000 |
0.0260 | 0.0350 |
0.0350 | 0.0490 |
0.0710 | 0.0950 |
0.0820 | 0.1110 |
0.1210 | 0.1600 |
0.1270 | 0.1660 |
0.1690 | 0.2120 |
0.1970 | 0.2450 |
0.1950 | 0.2480 |
0.2360 | 0.2930 |
0.2500 | 0.3050 |
0.2850 | 0.3440 |
0.2890 | 0.3480 |
0.3360 | 0.3950 |
0.3460 | 0.4000 |
0.3570 | 0.4130 |
0.3810 | 0.4360 |
0.4030 | 0.4590 |
0.4100 | 0.4660 |
0.4230 | 0.4790 |
0.4440 | 0.5040 |
0.4550 | 0.5110 |
0.4720 | 0.5250 |
0.4750 | 0.5280 |
0.4900 | 0.5430 |
0.4880 | 0.5460 |
0.5280 | 0.5790 |
0.5650 | 0.6150 |
0.6030 | 0.6440 |
0.6440 | 0.6800 |
0.6840 | 0.7160 |
0.7210 | 0.7490 |
0.7600 | 0.7830 |
0.7900 | 0.8110 |
0.8350 | 0.8510 |
0.8670 | 0.8790 |
0.9210 | 0.9270 |
0.9600 | 0.9630 |
0.9840 | 0.9850 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 60 (Liquid)
Mole fraction of Butane, 1-ethoxy- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 354.63 |
0.0000 | 354.63 |
0.0260 | 354.37 |
0.0350 | 354.22 |
0.0710 | 353.87 |
0.0820 | 353.79 |
0.1210 | 353.41 |
0.1270 | 353.34 |
0.1690 | 352.90 |
0.1970 | 352.71 |
0.1950 | 352.68 |
0.2360 | 352.43 |
0.2500 | 352.32 |
0.2850 | 352.06 |
0.2890 | 352.00 |
0.3360 | 351.62 |
0.3460 | 351.59 |
0.3570 | 351.50 |
0.3810 | 351.39 |
0.4030 | 351.29 |
0.4100 | 351.17 |
0.4230 | 351.19 |
0.4440 | 351.05 |
0.4550 | 350.96 |
0.4720 | 350.89 |
0.4750 | 350.77 |
0.4900 | 350.73 |
0.4880 | 350.78 |
0.5280 | 350.51 |
0.5650 | 350.35 |
0.6030 | 350.22 |
0.6440 | 349.98 |
0.6840 | 349.85 |
0.7210 | 349.71 |
0.7600 | 349.55 |
0.7900 | 349.32 |
0.8350 | 349.25 |
0.8670 | 349.12 |
0.9210 | 349.01 |
0.9600 | 348.93 |
0.9840 | 348.89 |
1.0000 | 348.84 |
Operational condition: Pressure, kPa = 60 (Liquid)
Mole fraction of Butane, 1-ethoxy- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 354.63 |
0.0000 | 354.63 |
0.0260 | 354.37 |
0.0350 | 354.22 |
0.0710 | 353.87 |
0.0820 | 353.79 |
0.1210 | 353.41 |
0.1270 | 353.34 |
0.1690 | 352.90 |
0.1970 | 352.71 |
0.1950 | 352.68 |
0.2360 | 352.43 |
0.2500 | 352.32 |
0.2850 | 352.06 |
0.2890 | 352.00 |
0.3360 | 351.62 |
0.3460 | 351.59 |
0.3570 | 351.50 |
0.3810 | 351.39 |
0.4030 | 351.29 |
0.4100 | 351.17 |
0.4230 | 351.19 |
0.4440 | 351.05 |
0.4550 | 350.96 |
0.4720 | 350.89 |
0.4750 | 350.77 |
0.4900 | 350.73 |
0.4880 | 350.78 |
0.5280 | 350.51 |
0.5650 | 350.35 |
0.6030 | 350.22 |
0.6440 | 349.98 |
0.6840 | 349.85 |
0.7210 | 349.71 |
0.7600 | 349.55 |
0.7900 | 349.32 |
0.8350 | 349.25 |
0.8670 | 349.12 |
0.9210 | 349.01 |
0.9600 | 348.93 |
0.9840 | 348.89 |
1.0000 | 348.84 |