Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Mass fraction of Water (3) - Liquid mixture 1 | Mass fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 2 | Mass fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 2 |
0.9210 | 0.0380 | 0.0170 | 0.9670 |
0.9070 | 0.0410 | 0.0190 | 0.9600 |
0.8780 | 0.0430 | 0.0220 | 0.9410 |
0.8510 | 0.0450 | 0.0350 | 0.9130 |
0.8230 | 0.0490 | 0.0420 | 0.8840 |
0.8140 | 0.0490 | 0.0470 | 0.8600 |
0.7920 | 0.0520 | 0.0590 | 0.8290 |
0.7730 | 0.0590 | 0.0800 | 0.7730 |
0.7520 | 0.0630 | 0.0960 | 0.7380 |
0.6940 | 0.0860 | 0.1610 | 0.6090 |
0.4070 | 0.2720 | 0.4070 | 0.2720 |
0.4200 | 0.2730 | 0.4200 | 0.2730 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 2 | Mole fraction of Ethanol (1) - Liquid mixture 2 |
288.15 | 0.9217 | 0.0000 | 0.0120 | 0.0000 |
288.15 | 0.8812 | 0.0304 | 0.0127 | 0.0231 |
288.15 | 0.8066 | 0.0744 | 0.0137 | 0.0466 |
288.15 | 0.6108 | 0.1702 | 0.0162 | 0.0786 |
288.15 | 0.3711 | 0.2184 | 0.0223 | 0.1045 |
288.15 | 0.2657 | 0.2243 | 0.0341 | 0.1224 |
288.15 | 0.1638 | 0.2009 | 0.0582 | 0.1471 |
298.15 | 0.9259 | 0.0000 | 0.0078 | 0.0000 |
298.15 | 0.8723 | 0.0382 | 0.0093 | 0.0223 |
298.15 | 0.7983 | 0.0845 | 0.0104 | 0.0445 |
298.15 | 0.5997 | 0.1849 | 0.0140 | 0.0787 |
298.15 | 0.3564 | 0.2316 | 0.0204 | 0.1058 |
298.15 | 0.1982 | 0.2312 | 0.0394 | 0.1331 |
Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Mass fraction of Water (3) - Liquid mixture 1 | Mass fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 2 | Mass fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 2 |
0.9210 | 0.0380 | 0.0170 | 0.9670 |
0.9070 | 0.0410 | 0.0190 | 0.9600 |
0.8780 | 0.0430 | 0.0220 | 0.9410 |
0.8510 | 0.0450 | 0.0350 | 0.9130 |
0.8230 | 0.0490 | 0.0420 | 0.8840 |
0.8140 | 0.0490 | 0.0470 | 0.8600 |
0.7920 | 0.0520 | 0.0590 | 0.8290 |
0.7730 | 0.0590 | 0.0800 | 0.7730 |
0.7520 | 0.0630 | 0.0960 | 0.7380 |
0.6940 | 0.0860 | 0.1610 | 0.6090 |
0.4070 | 0.2720 | 0.4070 | 0.2720 |
0.4200 | 0.2730 | 0.4200 | 0.2730 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 2 | Mole fraction of Ethanol (1) - Liquid mixture 2 |
288.15 | 0.9217 | 0.0000 | 0.0120 | 0.0000 |
288.15 | 0.8812 | 0.0304 | 0.0127 | 0.0231 |
288.15 | 0.8066 | 0.0744 | 0.0137 | 0.0466 |
288.15 | 0.6108 | 0.1702 | 0.0162 | 0.0786 |
288.15 | 0.3711 | 0.2184 | 0.0223 | 0.1045 |
288.15 | 0.2657 | 0.2243 | 0.0341 | 0.1224 |
288.15 | 0.1638 | 0.2009 | 0.0582 | 0.1471 |
298.15 | 0.9259 | 0.0000 | 0.0078 | 0.0000 |
298.15 | 0.8723 | 0.0382 | 0.0093 | 0.0223 |
298.15 | 0.7983 | 0.0845 | 0.0104 | 0.0445 |
298.15 | 0.5997 | 0.1849 | 0.0140 | 0.0787 |
298.15 | 0.3564 | 0.2316 | 0.0204 | 0.1058 |
298.15 | 0.1982 | 0.2312 | 0.0394 | 0.1331 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
288.15 | 0.1638 | 838.0 |
288.15 | 0.2657 | 806.0 |
288.15 | 0.3711 | 793.0 |
288.15 | 0.6108 | 770.0 |
288.15 | 0.8066 | 755.0 |
288.15 | 0.8812 | 742.0 |
288.15 | 0.9217 | 746.0 |
298.15 | 0.1982 | 822.4 |
298.15 | 0.3564 | 788.5 |
298.15 | 0.5997 | 760.4 |
298.15 | 0.7983 | 747.8 |
298.15 | 0.8723 | 741.6 |
298.15 | 0.9259 | 736.9 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
288.15 | 0.0120 | 979.0 |
288.15 | 0.0127 | 974.0 |
288.15 | 0.0137 | 967.0 |
288.15 | 0.0162 | 954.0 |
288.15 | 0.0223 | 898.0 |
288.15 | 0.0341 | 918.0 |
288.15 | 0.0582 | 936.0 |
298.15 | 0.0078 | 987.0 |
298.15 | 0.0093 | 974.0 |
298.15 | 0.0104 | 967.0 |
298.15 | 0.0140 | 954.0 |
298.15 | 0.0204 | 934.0 |
298.15 | 0.0394 | 910.0 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
288.15 | 0.1638 | 838.0 |
288.15 | 0.2657 | 806.0 |
288.15 | 0.3711 | 793.0 |
288.15 | 0.6108 | 770.0 |
288.15 | 0.8066 | 755.0 |
288.15 | 0.8812 | 742.0 |
288.15 | 0.9217 | 746.0 |
298.15 | 0.1982 | 822.4 |
298.15 | 0.3564 | 788.5 |
298.15 | 0.5997 | 760.4 |
298.15 | 0.7983 | 747.8 |
298.15 | 0.8723 | 741.6 |
298.15 | 0.9259 | 736.9 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
288.15 | 0.0120 | 979.0 |
288.15 | 0.0127 | 974.0 |
288.15 | 0.0137 | 967.0 |
288.15 | 0.0162 | 954.0 |
288.15 | 0.0223 | 898.0 |
288.15 | 0.0341 | 918.0 |
288.15 | 0.0582 | 936.0 |
298.15 | 0.0078 | 987.0 |
298.15 | 0.0093 | 974.0 |
298.15 | 0.0104 | 967.0 |
298.15 | 0.0140 | 954.0 |
298.15 | 0.0204 | 934.0 |
298.15 | 0.0394 | 910.0 |