Datasets
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Mole fraction (2)
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Pvap - Vapor or sublimation pressure, kPa (8)
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Vapor or sublimation pressure, kPa (2)
Mole fraction of 1-Decanol (2)
[ref]
Operational condition: Temperature, K =
323 (Gas)
| Pressure, kPa - Gas |
Mole fraction of 1-Decanol (2) - Gas |
| 9000.00 |
0.0011 |
| 10000.00 |
0.0016 |
| 11000.00 |
0.0105 |
| 12000.00 |
0.0118 |
| 13000.00 |
0.0131 |
| 16000.00 |
0.0165 |
| 18000.00 |
0.0188 |
Mole fraction of 1-Decanol (2)
[ref]
Operational condition: Temperature, K =
323 (Gas)
| Pressure, kPa - Gas |
Mole fraction of 1-Decanol (2) - Gas |
| 9000.00 |
0.0011 |
| 10000.00 |
0.0016 |
| 11000.00 |
0.0105 |
| 12000.00 |
0.0118 |
| 13000.00 |
0.0131 |
| 16000.00 |
0.0165 |
| 18000.00 |
0.0188 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mass fraction =
0.302 (Liquid)
| Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 314.80 |
27540.00 |
| 319.70 |
24330.00 |
| 328.20 |
21720.00 |
| 338.30 |
21040.00 |
| 348.30 |
21460.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 303.20 |
0.2010 |
1850.00 |
| 303.20 |
0.1990 |
2010.00 |
| 303.20 |
0.2450 |
2750.00 |
| 303.20 |
0.2770 |
2830.00 |
| 303.20 |
0.3550 |
4010.00 |
| 303.20 |
0.4990 |
5660.00 |
| 303.20 |
0.5390 |
6190.00 |
| 303.20 |
0.5570 |
6450.00 |
| 303.20 |
0.5570 |
6450.00 |
| 308.20 |
0.1150 |
1680.00 |
| 308.20 |
0.1860 |
2560.00 |
| 308.20 |
0.2340 |
3160.00 |
| 308.20 |
0.2380 |
3220.00 |
| 308.20 |
0.2420 |
3300.00 |
| 308.20 |
0.2660 |
3660.00 |
| 308.20 |
0.2870 |
3840.00 |
| 308.20 |
0.3200 |
4400.00 |
| 308.20 |
0.3250 |
4410.00 |
| 308.20 |
0.3430 |
4640.00 |
| 308.20 |
0.4050 |
5560.00 |
| 323.20 |
0.1640 |
2360.00 |
| 323.20 |
0.2250 |
3300.00 |
| 323.20 |
0.2870 |
4070.00 |
| 323.20 |
0.3320 |
4910.00 |
| 323.20 |
0.4120 |
6180.00 |
| 323.20 |
0.4750 |
7360.00 |
| 323.20 |
0.5090 |
8120.00 |
| 323.20 |
0.5580 |
9030.00 |
| 323.20 |
0.6080 |
10150.00 |
| 323.20 |
0.6450 |
11240.00 |
| 323.20 |
0.6600 |
12080.00 |
| 333.20 |
0.1420 |
2300.00 |
| 333.20 |
0.1880 |
2990.00 |
| 333.20 |
0.2290 |
3890.00 |
| 333.20 |
0.2830 |
4800.00 |
| 333.20 |
0.3110 |
5150.00 |
| 333.20 |
0.3880 |
6320.00 |
| 333.20 |
0.4280 |
7380.00 |
| 333.20 |
0.4920 |
8380.00 |
| 333.20 |
0.5140 |
9400.00 |
| 333.20 |
0.5360 |
9860.00 |
| 333.20 |
0.5520 |
10210.00 |
| 333.20 |
0.5820 |
11180.00 |
| 333.20 |
0.6350 |
12830.00 |
| 333.20 |
0.6500 |
13260.00 |
| 343.20 |
0.1250 |
1920.00 |
| 343.20 |
0.1840 |
2950.00 |
| 343.20 |
0.2370 |
3960.00 |
| 343.20 |
0.2950 |
5130.00 |
| 343.20 |
0.3450 |
6030.00 |
| 343.20 |
0.3890 |
7140.00 |
| 343.20 |
0.4330 |
7970.00 |
| 343.20 |
0.4970 |
9350.00 |
| 343.20 |
0.5430 |
10390.00 |
| 343.20 |
0.5710 |
11490.00 |
| 343.20 |
0.6070 |
12630.00 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 289.50 |
5110.00 |
| 290.30 |
5260.00 |
| 291.20 |
5330.00 |
| 292.20 |
5470.00 |
| 292.90 |
5570.00 |
| 293.70 |
5710.00 |
| 295.40 |
5970.00 |
| 296.40 |
6120.00 |
| 298.10 |
6370.00 |
| 299.80 |
6630.00 |
| 301.40 |
6870.00 |
| 301.50 |
6880.00 |
| 303.20 |
7170.00 |
| 304.20 |
7320.00 |
| 306.10 |
7650.00 |
| 306.20 |
7670.00 |
| 306.40 |
7710.00 |
| 307.00 |
7810.00 |
| 307.10 |
7820.00 |
| 307.20 |
7840.00 |
| 307.30 |
7860.00 |
| 307.90 |
7900.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
303.2 (Liquid mixture 1)
| Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 0.5920 |
7650.00 |
| 0.6080 |
10030.00 |
| 0.6260 |
12630.00 |
| 0.6300 |
15080.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mass fraction =
0.302 (Liquid)
| Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 314.80 |
27540.00 |
| 319.70 |
24330.00 |
| 328.20 |
21720.00 |
| 338.30 |
21040.00 |
| 348.30 |
21460.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 303.20 |
0.2010 |
1850.00 |
| 303.20 |
0.1990 |
2010.00 |
| 303.20 |
0.2450 |
2750.00 |
| 303.20 |
0.2770 |
2830.00 |
| 303.20 |
0.3550 |
4010.00 |
| 303.20 |
0.4990 |
5660.00 |
| 303.20 |
0.5390 |
6190.00 |
| 303.20 |
0.5570 |
6450.00 |
| 303.20 |
0.5570 |
6450.00 |
| 308.20 |
0.1150 |
1680.00 |
| 308.20 |
0.1860 |
2560.00 |
| 308.20 |
0.2340 |
3160.00 |
| 308.20 |
0.2380 |
3220.00 |
| 308.20 |
0.2420 |
3300.00 |
| 308.20 |
0.2660 |
3660.00 |
| 308.20 |
0.2870 |
3840.00 |
| 308.20 |
0.3200 |
4400.00 |
| 308.20 |
0.3250 |
4410.00 |
| 308.20 |
0.3430 |
4640.00 |
| 308.20 |
0.4050 |
5560.00 |
| 323.20 |
0.1640 |
2360.00 |
| 323.20 |
0.2250 |
3300.00 |
| 323.20 |
0.2870 |
4070.00 |
| 323.20 |
0.3320 |
4910.00 |
| 323.20 |
0.4120 |
6180.00 |
| 323.20 |
0.4750 |
7360.00 |
| 323.20 |
0.5090 |
8120.00 |
| 323.20 |
0.5580 |
9030.00 |
| 323.20 |
0.6080 |
10150.00 |
| 323.20 |
0.6450 |
11240.00 |
| 323.20 |
0.6600 |
12080.00 |
| 333.20 |
0.1420 |
2300.00 |
| 333.20 |
0.1880 |
2990.00 |
| 333.20 |
0.2290 |
3890.00 |
| 333.20 |
0.2830 |
4800.00 |
| 333.20 |
0.3110 |
5150.00 |
| 333.20 |
0.3880 |
6320.00 |
| 333.20 |
0.4280 |
7380.00 |
| 333.20 |
0.4920 |
8380.00 |
| 333.20 |
0.5140 |
9400.00 |
| 333.20 |
0.5360 |
9860.00 |
| 333.20 |
0.5520 |
10210.00 |
| 333.20 |
0.5820 |
11180.00 |
| 333.20 |
0.6350 |
12830.00 |
| 333.20 |
0.6500 |
13260.00 |
| 343.20 |
0.1250 |
1920.00 |
| 343.20 |
0.1840 |
2950.00 |
| 343.20 |
0.2370 |
3960.00 |
| 343.20 |
0.2950 |
5130.00 |
| 343.20 |
0.3450 |
6030.00 |
| 343.20 |
0.3890 |
7140.00 |
| 343.20 |
0.4330 |
7970.00 |
| 343.20 |
0.4970 |
9350.00 |
| 343.20 |
0.5430 |
10390.00 |
| 343.20 |
0.5710 |
11490.00 |
| 343.20 |
0.6070 |
12630.00 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 289.50 |
5110.00 |
| 290.30 |
5260.00 |
| 291.20 |
5330.00 |
| 292.20 |
5470.00 |
| 292.90 |
5570.00 |
| 293.70 |
5710.00 |
| 295.40 |
5970.00 |
| 296.40 |
6120.00 |
| 298.10 |
6370.00 |
| 299.80 |
6630.00 |
| 301.40 |
6870.00 |
| 301.50 |
6880.00 |
| 303.20 |
7170.00 |
| 304.20 |
7320.00 |
| 306.10 |
7650.00 |
| 306.20 |
7670.00 |
| 306.40 |
7710.00 |
| 307.00 |
7810.00 |
| 307.10 |
7820.00 |
| 307.20 |
7840.00 |
| 307.30 |
7860.00 |
| 307.90 |
7900.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
303.2 (Liquid mixture 1)
| Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 0.5920 |
7650.00 |
| 0.6080 |
10030.00 |
| 0.6260 |
12630.00 |
| 0.6300 |
15080.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mass fraction =
0.114 (Gas)
| Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 313.80 |
22060.00 |
| 318.50 |
20850.00 |
| 328.00 |
18800.00 |
| 338.20 |
19160.00 |
| 348.50 |
19940.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mass fraction =
0.114 (Gas)
| Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 313.80 |
22060.00 |
| 318.50 |
20850.00 |
| 328.00 |
18800.00 |
| 338.20 |
19160.00 |
| 348.50 |
19940.00 |
Sources
