Datasets
-
η - Viscosity, Pa*s (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
-
λ - Thermal conductivity, W/m/K (2)
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.2500 |
295.05 |
0.0223 |
0.2500 |
313.05 |
0.0091 |
0.2500 |
333.10 |
0.0043 |
0.2500 |
353.10 |
0.0024 |
0.2500 |
368.25 |
0.0017 |
0.2500 |
378.75 |
0.0014 |
0.2500 |
397.45 |
0.0010 |
0.2500 |
411.35 |
0.0008 |
0.2500 |
429.75 |
0.0006 |
0.2500 |
447.65 |
0.0005 |
0.5000 |
293.40 |
0.0599 |
0.5000 |
313.05 |
0.0186 |
0.5000 |
333.10 |
0.0077 |
0.5000 |
353.10 |
0.0039 |
0.5000 |
372.20 |
0.0023 |
0.5000 |
382.50 |
0.0019 |
0.5000 |
392.40 |
0.0015 |
0.5000 |
395.75 |
0.0014 |
0.5000 |
410.85 |
0.0011 |
0.5000 |
429.35 |
0.0008 |
0.5000 |
448.25 |
0.0006 |
0.7500 |
293.90 |
0.0885 |
0.7500 |
313.05 |
0.0258 |
0.7500 |
333.10 |
0.0097 |
0.7500 |
353.10 |
0.0047 |
0.7500 |
372.20 |
0.0027 |
0.7500 |
382.50 |
0.0021 |
0.7500 |
392.30 |
0.0017 |
0.7500 |
402.30 |
0.0014 |
0.7500 |
406.85 |
0.0013 |
0.7500 |
421.35 |
0.0010 |
0.7500 |
440.25 |
0.0008 |
0.7500 |
458.15 |
0.0006 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.2500 |
295.05 |
0.0223 |
0.2500 |
313.05 |
0.0091 |
0.2500 |
333.10 |
0.0043 |
0.2500 |
353.10 |
0.0024 |
0.2500 |
368.25 |
0.0017 |
0.2500 |
378.75 |
0.0014 |
0.2500 |
397.45 |
0.0010 |
0.2500 |
411.35 |
0.0008 |
0.2500 |
429.75 |
0.0006 |
0.2500 |
447.65 |
0.0005 |
0.5000 |
293.40 |
0.0599 |
0.5000 |
313.05 |
0.0186 |
0.5000 |
333.10 |
0.0077 |
0.5000 |
353.10 |
0.0039 |
0.5000 |
372.20 |
0.0023 |
0.5000 |
382.50 |
0.0019 |
0.5000 |
392.40 |
0.0015 |
0.5000 |
395.75 |
0.0014 |
0.5000 |
410.85 |
0.0011 |
0.5000 |
429.35 |
0.0008 |
0.5000 |
448.25 |
0.0006 |
0.7500 |
293.90 |
0.0885 |
0.7500 |
313.05 |
0.0258 |
0.7500 |
333.10 |
0.0097 |
0.7500 |
353.10 |
0.0047 |
0.7500 |
372.20 |
0.0027 |
0.7500 |
382.50 |
0.0021 |
0.7500 |
392.30 |
0.0017 |
0.7500 |
402.30 |
0.0014 |
0.7500 |
406.85 |
0.0013 |
0.7500 |
421.35 |
0.0010 |
0.7500 |
440.25 |
0.0008 |
0.7500 |
458.15 |
0.0006 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mass fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2000 |
303.15 |
4.11 |
0.2000 |
313.15 |
7.12 |
0.2000 |
323.15 |
11.93 |
0.2000 |
333.15 |
19.34 |
0.2000 |
343.15 |
30.36 |
0.4000 |
303.15 |
3.97 |
0.4000 |
313.15 |
6.90 |
0.4000 |
323.15 |
11.50 |
0.4000 |
333.15 |
18.56 |
0.4000 |
343.15 |
29.11 |
0.6000 |
303.15 |
3.69 |
0.6000 |
313.15 |
6.45 |
0.6000 |
323.15 |
10.66 |
0.6000 |
333.15 |
17.12 |
0.6000 |
343.15 |
26.86 |
0.8000 |
303.15 |
2.87 |
0.8000 |
313.15 |
5.13 |
0.8000 |
323.15 |
8.51 |
0.8000 |
333.15 |
13.82 |
0.8000 |
343.15 |
22.09 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mass fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2000 |
303.15 |
4.11 |
0.2000 |
313.15 |
7.12 |
0.2000 |
323.15 |
11.93 |
0.2000 |
333.15 |
19.34 |
0.2000 |
343.15 |
30.36 |
0.4000 |
303.15 |
3.97 |
0.4000 |
313.15 |
6.90 |
0.4000 |
323.15 |
11.50 |
0.4000 |
333.15 |
18.56 |
0.4000 |
343.15 |
29.11 |
0.6000 |
303.15 |
3.69 |
0.6000 |
313.15 |
6.45 |
0.6000 |
323.15 |
10.66 |
0.6000 |
333.15 |
17.12 |
0.6000 |
343.15 |
26.86 |
0.8000 |
303.15 |
2.87 |
0.8000 |
313.15 |
5.13 |
0.8000 |
323.15 |
8.51 |
0.8000 |
333.15 |
13.82 |
0.8000 |
343.15 |
22.09 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.2500 |
295.05 |
1040.0 |
0.2500 |
313.05 |
1026.0 |
0.2500 |
333.10 |
1010.0 |
0.2500 |
353.10 |
992.8 |
0.2500 |
368.25 |
979.2 |
0.2500 |
395.95 |
953.1 |
0.2500 |
408.35 |
941.3 |
0.2500 |
426.75 |
922.7 |
0.2500 |
444.65 |
904.1 |
0.5000 |
293.40 |
1034.0 |
0.5000 |
313.05 |
1019.0 |
0.5000 |
333.10 |
1003.0 |
0.5000 |
353.10 |
986.0 |
0.5000 |
372.20 |
969.5 |
0.5000 |
382.50 |
960.1 |
0.5000 |
392.40 |
951.0 |
0.5000 |
394.25 |
949.4 |
0.5000 |
407.85 |
936.8 |
0.5000 |
426.35 |
918.8 |
0.5000 |
445.25 |
899.1 |
0.7500 |
293.90 |
1028.0 |
0.7500 |
313.05 |
1013.0 |
0.7500 |
333.10 |
997.0 |
0.7500 |
353.10 |
980.5 |
0.7500 |
372.20 |
964.3 |
0.7500 |
382.50 |
955.2 |
0.7500 |
392.30 |
946.2 |
0.7500 |
402.30 |
936.9 |
0.7500 |
405.35 |
934.5 |
0.7500 |
418.35 |
923.0 |
0.7500 |
437.25 |
904.2 |
0.7500 |
455.15 |
887.2 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.2500 |
295.05 |
1040.0 |
0.2500 |
313.05 |
1026.0 |
0.2500 |
333.10 |
1010.0 |
0.2500 |
353.10 |
992.8 |
0.2500 |
368.25 |
979.2 |
0.2500 |
395.95 |
953.1 |
0.2500 |
408.35 |
941.3 |
0.2500 |
426.75 |
922.7 |
0.2500 |
444.65 |
904.1 |
0.5000 |
293.40 |
1034.0 |
0.5000 |
313.05 |
1019.0 |
0.5000 |
333.10 |
1003.0 |
0.5000 |
353.10 |
986.0 |
0.5000 |
372.20 |
969.5 |
0.5000 |
382.50 |
960.1 |
0.5000 |
392.40 |
951.0 |
0.5000 |
394.25 |
949.4 |
0.5000 |
407.85 |
936.8 |
0.5000 |
426.35 |
918.8 |
0.5000 |
445.25 |
899.1 |
0.7500 |
293.90 |
1028.0 |
0.7500 |
313.05 |
1013.0 |
0.7500 |
333.10 |
997.0 |
0.7500 |
353.10 |
980.5 |
0.7500 |
372.20 |
964.3 |
0.7500 |
382.50 |
955.2 |
0.7500 |
392.30 |
946.2 |
0.7500 |
402.30 |
936.9 |
0.7500 |
405.35 |
934.5 |
0.7500 |
418.35 |
923.0 |
0.7500 |
437.25 |
904.2 |
0.7500 |
455.15 |
887.2 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.2500 |
297.80 |
0.2480 |
0.2500 |
323.90 |
0.2560 |
0.2500 |
349.90 |
0.2600 |
0.2500 |
374.00 |
0.2640 |
0.2500 |
398.60 |
0.2630 |
0.2500 |
423.80 |
0.2640 |
0.5000 |
297.90 |
0.1900 |
0.5000 |
324.90 |
0.1930 |
0.5000 |
349.30 |
0.1950 |
0.5000 |
374.90 |
0.1960 |
0.5000 |
398.90 |
0.1950 |
0.5000 |
424.40 |
0.1930 |
0.5000 |
448.80 |
0.1870 |
0.7500 |
298.40 |
0.1670 |
0.7500 |
324.80 |
0.1690 |
0.7500 |
350.10 |
0.1670 |
0.7500 |
375.10 |
0.1690 |
0.7500 |
399.00 |
0.1690 |
0.7500 |
424.30 |
0.1670 |
0.7500 |
448.90 |
0.1630 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Propanol, 1,1'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.2500 |
297.80 |
0.2480 |
0.2500 |
323.90 |
0.2560 |
0.2500 |
349.90 |
0.2600 |
0.2500 |
374.00 |
0.2640 |
0.2500 |
398.60 |
0.2630 |
0.2500 |
423.80 |
0.2640 |
0.5000 |
297.90 |
0.1900 |
0.5000 |
324.90 |
0.1930 |
0.5000 |
349.30 |
0.1950 |
0.5000 |
374.90 |
0.1960 |
0.5000 |
398.90 |
0.1950 |
0.5000 |
424.40 |
0.1930 |
0.5000 |
448.80 |
0.1870 |
0.7500 |
298.40 |
0.1670 |
0.7500 |
324.80 |
0.1690 |
0.7500 |
350.10 |
0.1670 |
0.7500 |
375.10 |
0.1690 |
0.7500 |
399.00 |
0.1690 |
0.7500 |
424.30 |
0.1670 |
0.7500 |
448.90 |
0.1630 |
Sources