Datasets
-
η - Viscosity, Pa*s (4)
-
ρl - Mass density, kg/m3 (6)
Viscosity, Pa*s
[ref]
Operational condition: Mass fraction =
0.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
298.13 |
98.00 |
0.0262 |
298.15 |
49030.00 |
0.0359 |
298.15 |
98060.00 |
0.0481 |
298.15 |
196130.00 |
0.0823 |
322.00 |
196130.00 |
0.0271 |
322.25 |
98060.00 |
0.0172 |
322.32 |
49030.00 |
0.0133 |
322.36 |
98.00 |
0.0101 |
355.34 |
98.00 |
0.0040 |
355.56 |
49030.00 |
0.0051 |
355.67 |
98060.00 |
0.0063 |
355.76 |
196130.00 |
0.0093 |
392.20 |
98.00 |
0.0019 |
392.33 |
49030.00 |
0.0024 |
392.39 |
98060.00 |
0.0029 |
392.77 |
196130.00 |
0.0040 |
434.54 |
98060.00 |
0.0016 |
434.56 |
49030.00 |
0.0013 |
434.59 |
98.00 |
0.0011 |
434.70 |
196130.00 |
0.0022 |
462.27 |
196130.00 |
0.0016 |
462.40 |
49030.00 |
0.0010 |
462.47 |
98060.00 |
0.0012 |
462.61 |
98.00 |
0.0007 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
298.13 |
0.0262 |
322.36 |
0.0101 |
355.34 |
0.0040 |
392.20 |
0.0019 |
434.59 |
0.0011 |
462.61 |
0.0007 |
Viscosity, Pa*s
[ref]
Operational condition: Mass fraction =
0.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
298.13 |
98.00 |
0.0262 |
298.15 |
49030.00 |
0.0359 |
298.15 |
98060.00 |
0.0481 |
298.15 |
196130.00 |
0.0823 |
322.00 |
196130.00 |
0.0271 |
322.25 |
98060.00 |
0.0172 |
322.32 |
49030.00 |
0.0133 |
322.36 |
98.00 |
0.0101 |
355.34 |
98.00 |
0.0040 |
355.56 |
49030.00 |
0.0051 |
355.67 |
98060.00 |
0.0063 |
355.76 |
196130.00 |
0.0093 |
392.20 |
98.00 |
0.0019 |
392.33 |
49030.00 |
0.0024 |
392.39 |
98060.00 |
0.0029 |
392.77 |
196130.00 |
0.0040 |
434.54 |
98060.00 |
0.0016 |
434.56 |
49030.00 |
0.0013 |
434.59 |
98.00 |
0.0011 |
434.70 |
196130.00 |
0.0022 |
462.27 |
196130.00 |
0.0016 |
462.40 |
49030.00 |
0.0010 |
462.47 |
98060.00 |
0.0012 |
462.61 |
98.00 |
0.0007 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
298.13 |
0.0262 |
322.36 |
0.0101 |
355.34 |
0.0040 |
392.20 |
0.0019 |
434.59 |
0.0011 |
462.61 |
0.0007 |
Mass density, kg/m3
[ref]
Operational condition: Mass fraction =
0.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
298.13 |
98.00 |
1115.1 |
298.15 |
49030.00 |
1136.47 |
298.15 |
98060.00 |
1152.73 |
298.15 |
196130.00 |
1180.8 |
322.00 |
196130.00 |
1169.4 |
322.25 |
98060.00 |
1139.05 |
322.32 |
49030.00 |
1121.83 |
322.36 |
98.00 |
1101.75 |
355.34 |
98.00 |
1079.0 |
355.56 |
49030.00 |
1099.04 |
355.67 |
98060.00 |
1118.11 |
355.76 |
196130.00 |
1151.43 |
392.20 |
98.00 |
1047.37 |
392.33 |
49030.00 |
1070.25 |
392.39 |
98060.00 |
1092.45 |
392.77 |
196130.00 |
1129.25 |
434.54 |
98060.00 |
1059.58 |
434.56 |
49030.00 |
1032.55 |
434.59 |
98.00 |
1002.88 |
434.70 |
196130.00 |
1101.01 |
462.27 |
196130.00 |
1080.63 |
462.40 |
49030.00 |
1004.97 |
462.47 |
98060.00 |
1035.79 |
462.61 |
98.00 |
968.72 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
298.13 |
1115.1 |
322.36 |
1101.75 |
355.34 |
1079.0 |
392.20 |
1047.37 |
434.59 |
1002.88 |
462.61 |
968.72 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Triethylene glycol (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
101.00 |
0.5000 |
1115.45 |
Mass density, kg/m3
[ref]
Operational condition: Mass fraction =
0.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
298.13 |
98.00 |
1115.1 |
298.15 |
49030.00 |
1136.47 |
298.15 |
98060.00 |
1152.73 |
298.15 |
196130.00 |
1180.8 |
322.00 |
196130.00 |
1169.4 |
322.25 |
98060.00 |
1139.05 |
322.32 |
49030.00 |
1121.83 |
322.36 |
98.00 |
1101.75 |
355.34 |
98.00 |
1079.0 |
355.56 |
49030.00 |
1099.04 |
355.67 |
98060.00 |
1118.11 |
355.76 |
196130.00 |
1151.43 |
392.20 |
98.00 |
1047.37 |
392.33 |
49030.00 |
1070.25 |
392.39 |
98060.00 |
1092.45 |
392.77 |
196130.00 |
1129.25 |
434.54 |
98060.00 |
1059.58 |
434.56 |
49030.00 |
1032.55 |
434.59 |
98.00 |
1002.88 |
434.70 |
196130.00 |
1101.01 |
462.27 |
196130.00 |
1080.63 |
462.40 |
49030.00 |
1004.97 |
462.47 |
98060.00 |
1035.79 |
462.61 |
98.00 |
968.72 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
298.13 |
1115.1 |
322.36 |
1101.75 |
355.34 |
1079.0 |
392.20 |
1047.37 |
434.59 |
1002.88 |
462.61 |
968.72 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Triethylene glycol (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
101.00 |
0.5000 |
1115.45 |
Sources