Datasets
-
Mole fraction (2)
-
ν - Kinematic viscosity, m2/s (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
Mole fraction of Tetrahydropyran (1)
[ref]
Fixed |
Measured |
Mole fraction of Tetrahydropyran (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Tetrahydropyran (1) - Gas |
0.0000 |
298.15 |
0.0000 |
0.0000 |
313.15 |
0.0000 |
0.0000 |
328.15 |
0.0000 |
0.0597 |
298.15 |
0.1174 |
0.0601 |
313.15 |
0.1144 |
0.0602 |
328.15 |
0.1051 |
0.1280 |
328.15 |
0.2209 |
0.1310 |
313.15 |
0.2296 |
0.1349 |
298.15 |
0.2396 |
0.2101 |
298.15 |
0.3667 |
0.2101 |
313.15 |
0.3547 |
0.2102 |
328.15 |
0.3352 |
0.2731 |
313.15 |
0.4476 |
0.2735 |
328.15 |
0.4170 |
0.2737 |
298.15 |
0.4370 |
0.3986 |
328.15 |
0.5709 |
0.4007 |
298.15 |
0.5973 |
0.4182 |
313.15 |
0.6082 |
0.5347 |
328.15 |
0.6971 |
0.5396 |
313.15 |
0.7242 |
0.5452 |
298.15 |
0.7512 |
0.6095 |
298.15 |
0.7902 |
0.6101 |
328.15 |
0.7677 |
0.6102 |
313.15 |
0.7764 |
0.6734 |
328.15 |
0.8162 |
0.6818 |
313.15 |
0.8241 |
0.6834 |
298.15 |
0.8400 |
0.7470 |
328.15 |
0.8674 |
0.7483 |
313.15 |
0.8736 |
0.7501 |
298.15 |
0.8834 |
0.8625 |
328.15 |
0.9375 |
0.8667 |
313.15 |
0.9403 |
0.8683 |
298.15 |
0.9483 |
0.9413 |
298.15 |
0.9862 |
0.9449 |
328.15 |
0.9770 |
0.9471 |
313.15 |
0.9822 |
1.0000 |
298.15 |
1.0000 |
1.0000 |
313.15 |
1.0000 |
1.0000 |
328.15 |
1.0000 |
Mole fraction of Tetrahydropyran (1)
[ref]
Fixed |
Measured |
Mole fraction of Tetrahydropyran (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Tetrahydropyran (1) - Gas |
0.0000 |
298.15 |
0.0000 |
0.0000 |
313.15 |
0.0000 |
0.0000 |
328.15 |
0.0000 |
0.0597 |
298.15 |
0.1174 |
0.0601 |
313.15 |
0.1144 |
0.0602 |
328.15 |
0.1051 |
0.1280 |
328.15 |
0.2209 |
0.1310 |
313.15 |
0.2296 |
0.1349 |
298.15 |
0.2396 |
0.2101 |
298.15 |
0.3667 |
0.2101 |
313.15 |
0.3547 |
0.2102 |
328.15 |
0.3352 |
0.2731 |
313.15 |
0.4476 |
0.2735 |
328.15 |
0.4170 |
0.2737 |
298.15 |
0.4370 |
0.3986 |
328.15 |
0.5709 |
0.4007 |
298.15 |
0.5973 |
0.4182 |
313.15 |
0.6082 |
0.5347 |
328.15 |
0.6971 |
0.5396 |
313.15 |
0.7242 |
0.5452 |
298.15 |
0.7512 |
0.6095 |
298.15 |
0.7902 |
0.6101 |
328.15 |
0.7677 |
0.6102 |
313.15 |
0.7764 |
0.6734 |
328.15 |
0.8162 |
0.6818 |
313.15 |
0.8241 |
0.6834 |
298.15 |
0.8400 |
0.7470 |
328.15 |
0.8674 |
0.7483 |
313.15 |
0.8736 |
0.7501 |
298.15 |
0.8834 |
0.8625 |
328.15 |
0.9375 |
0.8667 |
313.15 |
0.9403 |
0.8683 |
298.15 |
0.9483 |
0.9413 |
298.15 |
0.9862 |
0.9449 |
328.15 |
0.9770 |
0.9471 |
313.15 |
0.9822 |
1.0000 |
298.15 |
1.0000 |
1.0000 |
313.15 |
1.0000 |
1.0000 |
328.15 |
1.0000 |
Kinematic viscosity, m2/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydropyran (1) - Liquid |
Kinematic viscosity, m2/s - Liquid |
283.15 |
0.0000 |
7.3160e-07 |
283.15 |
0.0539 |
7.4180e-07 |
283.15 |
0.1030 |
7.5180e-07 |
283.15 |
0.2061 |
7.7470e-07 |
283.15 |
0.3009 |
7.9800e-07 |
283.15 |
0.4041 |
8.2610e-07 |
283.15 |
0.5077 |
8.5800e-07 |
283.15 |
0.6028 |
8.9230e-07 |
283.15 |
0.6732 |
9.2080e-07 |
283.15 |
0.7873 |
9.7580e-07 |
283.15 |
0.9004 |
1.0441e-06 |
283.15 |
0.9488 |
1.0789e-06 |
283.15 |
1.0000 |
1.1205e-06 |
298.15 |
0.0000 |
6.2790e-07 |
298.15 |
0.0539 |
6.3550e-07 |
298.15 |
0.1030 |
6.4240e-07 |
298.15 |
0.2061 |
6.5990e-07 |
298.15 |
0.3009 |
6.7720e-07 |
298.15 |
0.4041 |
6.9850e-07 |
298.15 |
0.5077 |
7.2220e-07 |
298.15 |
0.6028 |
7.4730e-07 |
298.15 |
0.6732 |
7.6790e-07 |
298.15 |
0.7873 |
8.0740e-07 |
298.15 |
0.9004 |
8.5560e-07 |
298.15 |
0.9488 |
8.8060e-07 |
298.15 |
1.0000 |
9.1000e-07 |
313.15 |
0.0000 |
5.4210e-07 |
313.15 |
0.0539 |
5.4860e-07 |
313.15 |
0.1030 |
5.5420e-07 |
313.15 |
0.2061 |
5.6800e-07 |
313.15 |
0.3009 |
5.8150e-07 |
313.15 |
0.4041 |
5.9810e-07 |
313.15 |
0.5077 |
6.1690e-07 |
313.15 |
0.6028 |
6.3640e-07 |
313.15 |
0.6732 |
6.5250e-07 |
313.15 |
0.7873 |
6.8160e-07 |
313.15 |
0.9004 |
7.1840e-07 |
313.15 |
0.9488 |
7.3580e-07 |
313.15 |
1.0000 |
7.5710e-07 |
Kinematic viscosity, m2/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydropyran (1) - Liquid |
Kinematic viscosity, m2/s - Liquid |
283.15 |
0.0000 |
7.3160e-07 |
283.15 |
0.0539 |
7.4180e-07 |
283.15 |
0.1030 |
7.5180e-07 |
283.15 |
0.2061 |
7.7470e-07 |
283.15 |
0.3009 |
7.9800e-07 |
283.15 |
0.4041 |
8.2610e-07 |
283.15 |
0.5077 |
8.5800e-07 |
283.15 |
0.6028 |
8.9230e-07 |
283.15 |
0.6732 |
9.2080e-07 |
283.15 |
0.7873 |
9.7580e-07 |
283.15 |
0.9004 |
1.0441e-06 |
283.15 |
0.9488 |
1.0789e-06 |
283.15 |
1.0000 |
1.1205e-06 |
298.15 |
0.0000 |
6.2790e-07 |
298.15 |
0.0539 |
6.3550e-07 |
298.15 |
0.1030 |
6.4240e-07 |
298.15 |
0.2061 |
6.5990e-07 |
298.15 |
0.3009 |
6.7720e-07 |
298.15 |
0.4041 |
6.9850e-07 |
298.15 |
0.5077 |
7.2220e-07 |
298.15 |
0.6028 |
7.4730e-07 |
298.15 |
0.6732 |
7.6790e-07 |
298.15 |
0.7873 |
8.0740e-07 |
298.15 |
0.9004 |
8.5560e-07 |
298.15 |
0.9488 |
8.8060e-07 |
298.15 |
1.0000 |
9.1000e-07 |
313.15 |
0.0000 |
5.4210e-07 |
313.15 |
0.0539 |
5.4860e-07 |
313.15 |
0.1030 |
5.5420e-07 |
313.15 |
0.2061 |
5.6800e-07 |
313.15 |
0.3009 |
5.8150e-07 |
313.15 |
0.4041 |
5.9810e-07 |
313.15 |
0.5077 |
6.1690e-07 |
313.15 |
0.6028 |
6.3640e-07 |
313.15 |
0.6732 |
6.5250e-07 |
313.15 |
0.7873 |
6.8160e-07 |
313.15 |
0.9004 |
7.1840e-07 |
313.15 |
0.9488 |
7.3580e-07 |
313.15 |
1.0000 |
7.5710e-07 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Tetrahydropyran (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
298.15 |
4.05 |
0.0000 |
313.15 |
8.45 |
0.0000 |
328.15 |
16.40 |
0.0597 |
298.15 |
4.32 |
0.0601 |
313.15 |
8.97 |
0.0602 |
328.15 |
17.25 |
0.1280 |
328.15 |
18.25 |
0.1310 |
313.15 |
9.64 |
0.1349 |
298.15 |
4.67 |
0.2101 |
298.15 |
5.04 |
0.2101 |
313.15 |
10.34 |
0.2102 |
328.15 |
19.48 |
0.2731 |
313.15 |
10.93 |
0.2735 |
328.15 |
20.50 |
0.2737 |
298.15 |
5.36 |
0.3986 |
328.15 |
22.63 |
0.4007 |
298.15 |
6.04 |
0.4182 |
313.15 |
12.42 |
0.5347 |
328.15 |
24.81 |
0.5396 |
313.15 |
13.70 |
0.5452 |
298.15 |
6.96 |
0.6095 |
298.15 |
7.25 |
0.6101 |
328.15 |
26.42 |
0.6102 |
313.15 |
14.37 |
0.6734 |
328.15 |
27.58 |
0.6818 |
313.15 |
15.04 |
0.6834 |
298.15 |
7.59 |
0.7470 |
328.15 |
29.09 |
0.7483 |
313.15 |
15.86 |
0.7501 |
298.15 |
8.10 |
0.8625 |
328.15 |
31.32 |
0.8667 |
313.15 |
17.09 |
0.8683 |
298.15 |
8.74 |
0.9413 |
298.15 |
9.22 |
0.9449 |
328.15 |
33.16 |
0.9471 |
313.15 |
18.08 |
1.0000 |
298.15 |
9.56 |
1.0000 |
313.15 |
18.66 |
1.0000 |
328.15 |
33.95 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Tetrahydropyran (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
298.15 |
4.05 |
0.0000 |
313.15 |
8.45 |
0.0000 |
328.15 |
16.40 |
0.0597 |
298.15 |
4.32 |
0.0601 |
313.15 |
8.97 |
0.0602 |
328.15 |
17.25 |
0.1280 |
328.15 |
18.25 |
0.1310 |
313.15 |
9.64 |
0.1349 |
298.15 |
4.67 |
0.2101 |
298.15 |
5.04 |
0.2101 |
313.15 |
10.34 |
0.2102 |
328.15 |
19.48 |
0.2731 |
313.15 |
10.93 |
0.2735 |
328.15 |
20.50 |
0.2737 |
298.15 |
5.36 |
0.3986 |
328.15 |
22.63 |
0.4007 |
298.15 |
6.04 |
0.4182 |
313.15 |
12.42 |
0.5347 |
328.15 |
24.81 |
0.5396 |
313.15 |
13.70 |
0.5452 |
298.15 |
6.96 |
0.6095 |
298.15 |
7.25 |
0.6101 |
328.15 |
26.42 |
0.6102 |
313.15 |
14.37 |
0.6734 |
328.15 |
27.58 |
0.6818 |
313.15 |
15.04 |
0.6834 |
298.15 |
7.59 |
0.7470 |
328.15 |
29.09 |
0.7483 |
313.15 |
15.86 |
0.7501 |
298.15 |
8.10 |
0.8625 |
328.15 |
31.32 |
0.8667 |
313.15 |
17.09 |
0.8683 |
298.15 |
8.74 |
0.9413 |
298.15 |
9.22 |
0.9449 |
328.15 |
33.16 |
0.9471 |
313.15 |
18.08 |
1.0000 |
298.15 |
9.56 |
1.0000 |
313.15 |
18.66 |
1.0000 |
328.15 |
33.95 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydropyran (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
892.29 |
283.15 |
0.0539 |
892.29 |
283.15 |
0.1030 |
892.39 |
283.15 |
0.2061 |
892.47 |
283.15 |
0.3009 |
892.73 |
283.15 |
0.4041 |
892.75 |
283.15 |
0.5077 |
893.01 |
283.15 |
0.6028 |
893.09 |
283.15 |
0.6732 |
893.25 |
283.15 |
0.7873 |
893.32 |
283.15 |
0.9004 |
893.5 |
283.15 |
0.9488 |
893.6 |
283.15 |
1.0000 |
893.62 |
298.15 |
0.0000 |
877.05 |
298.15 |
0.0539 |
877.1 |
298.15 |
0.1030 |
877.18 |
298.15 |
0.2061 |
877.41 |
298.15 |
0.3009 |
877.44 |
298.15 |
0.4041 |
877.59 |
298.15 |
0.5077 |
877.73 |
298.15 |
0.6028 |
877.83 |
298.15 |
0.6732 |
877.98 |
298.15 |
0.7873 |
878.13 |
298.15 |
0.9004 |
878.33 |
298.15 |
0.9488 |
878.49 |
298.15 |
1.0000 |
878.79 |
313.15 |
0.0000 |
861.46 |
313.15 |
0.0539 |
861.65 |
313.15 |
0.1030 |
861.78 |
313.15 |
0.2061 |
861.97 |
313.15 |
0.3009 |
862.25 |
313.15 |
0.4041 |
862.4 |
313.15 |
0.5077 |
862.7 |
313.15 |
0.6028 |
862.82 |
313.15 |
0.6732 |
862.99 |
313.15 |
0.7873 |
863.26 |
313.15 |
0.9004 |
863.45 |
313.15 |
0.9488 |
863.55 |
313.15 |
1.0000 |
863.69 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydropyran (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
892.29 |
283.15 |
0.0539 |
892.29 |
283.15 |
0.1030 |
892.39 |
283.15 |
0.2061 |
892.47 |
283.15 |
0.3009 |
892.73 |
283.15 |
0.4041 |
892.75 |
283.15 |
0.5077 |
893.01 |
283.15 |
0.6028 |
893.09 |
283.15 |
0.6732 |
893.25 |
283.15 |
0.7873 |
893.32 |
283.15 |
0.9004 |
893.5 |
283.15 |
0.9488 |
893.6 |
283.15 |
1.0000 |
893.62 |
298.15 |
0.0000 |
877.05 |
298.15 |
0.0539 |
877.1 |
298.15 |
0.1030 |
877.18 |
298.15 |
0.2061 |
877.41 |
298.15 |
0.3009 |
877.44 |
298.15 |
0.4041 |
877.59 |
298.15 |
0.5077 |
877.73 |
298.15 |
0.6028 |
877.83 |
298.15 |
0.6732 |
877.98 |
298.15 |
0.7873 |
878.13 |
298.15 |
0.9004 |
878.33 |
298.15 |
0.9488 |
878.49 |
298.15 |
1.0000 |
878.79 |
313.15 |
0.0000 |
861.46 |
313.15 |
0.0539 |
861.65 |
313.15 |
0.1030 |
861.78 |
313.15 |
0.2061 |
861.97 |
313.15 |
0.3009 |
862.25 |
313.15 |
0.4041 |
862.4 |
313.15 |
0.5077 |
862.7 |
313.15 |
0.6028 |
862.82 |
313.15 |
0.6732 |
862.99 |
313.15 |
0.7873 |
863.26 |
313.15 |
0.9004 |
863.45 |
313.15 |
0.9488 |
863.55 |
313.15 |
1.0000 |
863.69 |
Sources