Mixture of 1-Propanol, 2-methyl- + Ethylene
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρg - Mass density, kg/m3 (2)
-
ρl - Mass density, kg/m3 (2)
Mole fraction of Ethylene (2)
[ref]
Fixed |
Measured |
Mole fraction of Ethylene (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethylene (2) - Gas |
0.2320 |
283.65 |
0.9870 |
0.2340 |
288.15 |
0.9960 |
0.2750 |
278.15 |
0.9950 |
0.2940 |
288.15 |
0.9960 |
0.3630 |
283.65 |
0.9910 |
0.3770 |
288.15 |
0.9930 |
0.4000 |
278.15 |
0.9900 |
0.4390 |
288.15 |
0.9890 |
0.4700 |
278.15 |
0.9910 |
0.5080 |
283.65 |
0.9960 |
0.5440 |
288.15 |
0.9940 |
0.5840 |
278.15 |
0.9930 |
0.6300 |
283.65 |
0.9960 |
0.6540 |
288.15 |
0.9950 |
0.6680 |
278.15 |
0.9970 |
0.8090 |
283.65 |
0.9980 |
0.8370 |
288.15 |
0.9960 |
0.8410 |
278.15 |
0.9980 |
0.9410 |
278.15 |
0.9990 |
0.9550 |
283.65 |
0.9990 |
0.9620 |
288.15 |
0.9960 |
0.9880 |
278.15 |
0.9990 |
0.9900 |
283.65 |
0.9980 |
Mole fraction of Ethylene (2)
[ref]
Fixed |
Measured |
Mole fraction of Ethylene (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethylene (2) - Gas |
0.2320 |
283.65 |
0.9870 |
0.2340 |
288.15 |
0.9960 |
0.2750 |
278.15 |
0.9950 |
0.2940 |
288.15 |
0.9960 |
0.3630 |
283.65 |
0.9910 |
0.3770 |
288.15 |
0.9930 |
0.4000 |
278.15 |
0.9900 |
0.4390 |
288.15 |
0.9890 |
0.4700 |
278.15 |
0.9910 |
0.5080 |
283.65 |
0.9960 |
0.5440 |
288.15 |
0.9940 |
0.5840 |
278.15 |
0.9930 |
0.6300 |
283.65 |
0.9960 |
0.6540 |
288.15 |
0.9950 |
0.6680 |
278.15 |
0.9970 |
0.8090 |
283.65 |
0.9980 |
0.8370 |
288.15 |
0.9960 |
0.8410 |
278.15 |
0.9980 |
0.9410 |
278.15 |
0.9990 |
0.9550 |
283.65 |
0.9990 |
0.9620 |
288.15 |
0.9960 |
0.9880 |
278.15 |
0.9990 |
0.9900 |
283.65 |
0.9980 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethylene (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2320 |
283.65 |
2107.00 |
0.2340 |
288.15 |
2252.00 |
0.2750 |
278.15 |
2236.00 |
0.2940 |
288.15 |
2822.00 |
0.3630 |
283.65 |
3106.00 |
0.3770 |
288.15 |
3523.00 |
0.4000 |
278.15 |
3117.00 |
0.4390 |
288.15 |
4028.00 |
0.4700 |
278.15 |
3569.00 |
0.5080 |
283.65 |
4147.00 |
0.5440 |
288.15 |
4703.00 |
0.5840 |
278.15 |
4058.00 |
0.6300 |
283.65 |
4694.00 |
0.6540 |
288.15 |
5211.00 |
0.6680 |
278.15 |
4262.00 |
0.8090 |
283.65 |
4933.00 |
0.8370 |
288.15 |
5453.00 |
0.8410 |
278.15 |
4389.00 |
0.9410 |
278.15 |
4425.00 |
0.9550 |
283.65 |
4980.00 |
0.9620 |
288.15 |
5474.00 |
0.9880 |
278.15 |
4497.00 |
0.9900 |
283.65 |
5047.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethylene (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2320 |
283.65 |
2107.00 |
0.2340 |
288.15 |
2252.00 |
0.2750 |
278.15 |
2236.00 |
0.2940 |
288.15 |
2822.00 |
0.3630 |
283.65 |
3106.00 |
0.3770 |
288.15 |
3523.00 |
0.4000 |
278.15 |
3117.00 |
0.4390 |
288.15 |
4028.00 |
0.4700 |
278.15 |
3569.00 |
0.5080 |
283.65 |
4147.00 |
0.5440 |
288.15 |
4703.00 |
0.5840 |
278.15 |
4058.00 |
0.6300 |
283.65 |
4694.00 |
0.6540 |
288.15 |
5211.00 |
0.6680 |
278.15 |
4262.00 |
0.8090 |
283.65 |
4933.00 |
0.8370 |
288.15 |
5453.00 |
0.8410 |
278.15 |
4389.00 |
0.9410 |
278.15 |
4425.00 |
0.9550 |
283.65 |
4980.00 |
0.9620 |
288.15 |
5474.00 |
0.9880 |
278.15 |
4497.00 |
0.9900 |
283.65 |
5047.00 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Gas |
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
2107.00 |
283.65 |
29.9 |
2236.00 |
278.15 |
33.8 |
2252.00 |
288.15 |
32.6 |
2822.00 |
288.15 |
43.1 |
3106.00 |
283.65 |
49.6 |
3117.00 |
278.15 |
52.6 |
3523.00 |
288.15 |
58.9 |
3569.00 |
278.15 |
65.4 |
4028.00 |
288.15 |
72.2 |
4058.00 |
278.15 |
88.0 |
4147.00 |
283.65 |
81.8 |
4262.00 |
278.15 |
96.7 |
4389.00 |
278.15 |
105.3 |
4425.00 |
278.15 |
108.1 |
4497.00 |
278.15 |
114.6 |
4694.00 |
283.65 |
108.8 |
4703.00 |
288.15 |
99.4 |
4933.00 |
283.65 |
130.3 |
4980.00 |
283.65 |
137.2 |
5047.00 |
283.65 |
151.8 |
5211.00 |
288.15 |
131.5 |
5453.00 |
288.15 |
173.3 |
5474.00 |
288.15 |
183.4 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Gas |
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
2107.00 |
283.65 |
29.9 |
2236.00 |
278.15 |
33.8 |
2252.00 |
288.15 |
32.6 |
2822.00 |
288.15 |
43.1 |
3106.00 |
283.65 |
49.6 |
3117.00 |
278.15 |
52.6 |
3523.00 |
288.15 |
58.9 |
3569.00 |
278.15 |
65.4 |
4028.00 |
288.15 |
72.2 |
4058.00 |
278.15 |
88.0 |
4147.00 |
283.65 |
81.8 |
4262.00 |
278.15 |
96.7 |
4389.00 |
278.15 |
105.3 |
4425.00 |
278.15 |
108.1 |
4497.00 |
278.15 |
114.6 |
4694.00 |
283.65 |
108.8 |
4703.00 |
288.15 |
99.4 |
4933.00 |
283.65 |
130.3 |
4980.00 |
283.65 |
137.2 |
5047.00 |
283.65 |
151.8 |
5211.00 |
288.15 |
131.5 |
5453.00 |
288.15 |
173.3 |
5474.00 |
288.15 |
183.4 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
2107.00 |
283.65 |
759.0 |
2236.00 |
278.15 |
753.2 |
2252.00 |
288.15 |
755.4 |
2822.00 |
288.15 |
739.3 |
3106.00 |
283.65 |
725.9 |
3117.00 |
278.15 |
717.1 |
3523.00 |
288.15 |
715.8 |
3569.00 |
278.15 |
691.1 |
4028.00 |
288.15 |
695.0 |
4058.00 |
278.15 |
639.8 |
4147.00 |
283.65 |
674.4 |
4262.00 |
278.15 |
604.1 |
4389.00 |
278.15 |
495.9 |
4425.00 |
278.15 |
402.3 |
4497.00 |
278.15 |
340.4 |
4694.00 |
283.65 |
617.8 |
4703.00 |
288.15 |
656.2 |
4933.00 |
283.65 |
512.8 |
4980.00 |
283.65 |
361.3 |
5047.00 |
283.65 |
303.3 |
5211.00 |
288.15 |
602.1 |
5453.00 |
288.15 |
479.3 |
5474.00 |
288.15 |
340.7 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
2107.00 |
283.65 |
759.0 |
2236.00 |
278.15 |
753.2 |
2252.00 |
288.15 |
755.4 |
2822.00 |
288.15 |
739.3 |
3106.00 |
283.65 |
725.9 |
3117.00 |
278.15 |
717.1 |
3523.00 |
288.15 |
715.8 |
3569.00 |
278.15 |
691.1 |
4028.00 |
288.15 |
695.0 |
4058.00 |
278.15 |
639.8 |
4147.00 |
283.65 |
674.4 |
4262.00 |
278.15 |
604.1 |
4389.00 |
278.15 |
495.9 |
4425.00 |
278.15 |
402.3 |
4497.00 |
278.15 |
340.4 |
4694.00 |
283.65 |
617.8 |
4703.00 |
288.15 |
656.2 |
4933.00 |
283.65 |
512.8 |
4980.00 |
283.65 |
361.3 |
5047.00 |
283.65 |
303.3 |
5211.00 |
288.15 |
602.1 |
5453.00 |
288.15 |
479.3 |
5474.00 |
288.15 |
340.7 |
Sources