Datasets
-
Henry's Law constant (mole fraction scale), kPa (2)
-
η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
Henry's Law constant (mole fraction scale), kPa of Tetrahydrofuran (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Tetrahydrofuran (2) - Liquid |
293.20 |
0.0000 |
27.0 |
Henry's Law constant (mole fraction scale), kPa of Tetrahydrofuran (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Tetrahydrofuran (2) - Liquid |
293.20 |
0.0000 |
27.0 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0541 |
0.0063 |
298.15 |
0.1044 |
0.0054 |
298.15 |
0.1535 |
0.0047 |
298.15 |
0.2050 |
0.0040 |
298.15 |
0.2574 |
0.0035 |
298.15 |
0.3054 |
0.0030 |
298.15 |
0.4003 |
0.0023 |
298.15 |
0.5004 |
0.0017 |
298.15 |
0.6111 |
0.0013 |
298.15 |
0.7032 |
0.0010 |
298.15 |
0.8116 |
0.0007 |
298.15 |
0.9048 |
0.0006 |
303.15 |
0.0541 |
0.0052 |
303.15 |
0.1044 |
0.0046 |
303.15 |
0.1535 |
0.0040 |
303.15 |
0.2050 |
0.0034 |
303.15 |
0.2574 |
0.0030 |
303.15 |
0.3054 |
0.0026 |
303.15 |
0.4003 |
0.0021 |
303.15 |
0.5004 |
0.0016 |
303.15 |
0.6111 |
0.0012 |
303.15 |
0.7032 |
0.0009 |
303.15 |
0.8116 |
0.0007 |
303.15 |
0.9048 |
0.0006 |
308.15 |
0.0541 |
0.0042 |
308.15 |
0.1044 |
0.0037 |
308.15 |
0.1535 |
0.0032 |
308.15 |
0.2050 |
0.0028 |
308.15 |
0.2574 |
0.0025 |
308.15 |
0.3054 |
0.0022 |
308.15 |
0.4003 |
0.0017 |
308.15 |
0.5004 |
0.0013 |
308.15 |
0.6111 |
0.0010 |
308.15 |
0.7032 |
0.0008 |
308.15 |
0.8116 |
0.0006 |
308.15 |
0.9048 |
0.0005 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0541 |
0.0063 |
298.15 |
0.1044 |
0.0054 |
298.15 |
0.1535 |
0.0047 |
298.15 |
0.2050 |
0.0040 |
298.15 |
0.2574 |
0.0035 |
298.15 |
0.3054 |
0.0030 |
298.15 |
0.4003 |
0.0023 |
298.15 |
0.5004 |
0.0017 |
298.15 |
0.6111 |
0.0013 |
298.15 |
0.7032 |
0.0010 |
298.15 |
0.8116 |
0.0007 |
298.15 |
0.9048 |
0.0006 |
303.15 |
0.0541 |
0.0052 |
303.15 |
0.1044 |
0.0046 |
303.15 |
0.1535 |
0.0040 |
303.15 |
0.2050 |
0.0034 |
303.15 |
0.2574 |
0.0030 |
303.15 |
0.3054 |
0.0026 |
303.15 |
0.4003 |
0.0021 |
303.15 |
0.5004 |
0.0016 |
303.15 |
0.6111 |
0.0012 |
303.15 |
0.7032 |
0.0009 |
303.15 |
0.8116 |
0.0007 |
303.15 |
0.9048 |
0.0006 |
308.15 |
0.0541 |
0.0042 |
308.15 |
0.1044 |
0.0037 |
308.15 |
0.1535 |
0.0032 |
308.15 |
0.2050 |
0.0028 |
308.15 |
0.2574 |
0.0025 |
308.15 |
0.3054 |
0.0022 |
308.15 |
0.4003 |
0.0017 |
308.15 |
0.5004 |
0.0013 |
308.15 |
0.6111 |
0.0010 |
308.15 |
0.7032 |
0.0008 |
308.15 |
0.8116 |
0.0006 |
308.15 |
0.9048 |
0.0005 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0541 |
823.522 |
298.15 |
0.1044 |
825.135 |
298.15 |
0.1535 |
826.78 |
298.15 |
0.2050 |
828.609 |
298.15 |
0.2574 |
830.564 |
298.15 |
0.3054 |
832.449 |
298.15 |
0.4003 |
836.541 |
298.15 |
0.5004 |
841.464 |
298.15 |
0.6111 |
847.802 |
298.15 |
0.7032 |
853.984 |
298.15 |
0.8116 |
862.541 |
298.15 |
0.9048 |
871.362 |
303.15 |
0.0541 |
819.992 |
303.15 |
0.1044 |
821.552 |
303.15 |
0.1535 |
823.145 |
303.15 |
0.2050 |
824.915 |
303.15 |
0.2574 |
826.809 |
303.15 |
0.3054 |
828.634 |
303.15 |
0.4003 |
832.585 |
303.15 |
0.5004 |
837.343 |
303.15 |
0.6111 |
843.471 |
303.15 |
0.7032 |
849.444 |
303.15 |
0.8116 |
857.718 |
303.15 |
0.9048 |
866.235 |
308.15 |
0.0541 |
816.44 |
308.15 |
0.1044 |
817.948 |
308.15 |
0.1535 |
819.488 |
308.15 |
0.2050 |
821.202 |
308.15 |
0.2574 |
823.029 |
308.15 |
0.3054 |
824.796 |
308.15 |
0.4003 |
828.614 |
308.15 |
0.5004 |
833.216 |
308.15 |
0.6111 |
839.116 |
308.15 |
0.7032 |
844.874 |
308.15 |
0.8116 |
852.874 |
308.15 |
0.9048 |
861.083 |
313.15 |
0.0541 |
812.862 |
313.15 |
0.1044 |
814.315 |
313.15 |
0.1535 |
815.803 |
313.15 |
0.2050 |
817.465 |
313.15 |
0.2574 |
819.222 |
313.15 |
0.3054 |
820.932 |
313.15 |
0.4003 |
824.625 |
313.15 |
0.5004 |
829.064 |
313.15 |
0.6111 |
834.743 |
313.15 |
0.7032 |
840.294 |
313.15 |
0.8116 |
848.0 |
313.15 |
0.9048 |
855.903 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0541 |
823.522 |
298.15 |
0.1044 |
825.135 |
298.15 |
0.1535 |
826.78 |
298.15 |
0.2050 |
828.609 |
298.15 |
0.2574 |
830.564 |
298.15 |
0.3054 |
832.449 |
298.15 |
0.4003 |
836.541 |
298.15 |
0.5004 |
841.464 |
298.15 |
0.6111 |
847.802 |
298.15 |
0.7032 |
853.984 |
298.15 |
0.8116 |
862.541 |
298.15 |
0.9048 |
871.362 |
303.15 |
0.0541 |
819.992 |
303.15 |
0.1044 |
821.552 |
303.15 |
0.1535 |
823.145 |
303.15 |
0.2050 |
824.915 |
303.15 |
0.2574 |
826.809 |
303.15 |
0.3054 |
828.634 |
303.15 |
0.4003 |
832.585 |
303.15 |
0.5004 |
837.343 |
303.15 |
0.6111 |
843.471 |
303.15 |
0.7032 |
849.444 |
303.15 |
0.8116 |
857.718 |
303.15 |
0.9048 |
866.235 |
308.15 |
0.0541 |
816.44 |
308.15 |
0.1044 |
817.948 |
308.15 |
0.1535 |
819.488 |
308.15 |
0.2050 |
821.202 |
308.15 |
0.2574 |
823.029 |
308.15 |
0.3054 |
824.796 |
308.15 |
0.4003 |
828.614 |
308.15 |
0.5004 |
833.216 |
308.15 |
0.6111 |
839.116 |
308.15 |
0.7032 |
844.874 |
308.15 |
0.8116 |
852.874 |
308.15 |
0.9048 |
861.083 |
313.15 |
0.0541 |
812.862 |
313.15 |
0.1044 |
814.315 |
313.15 |
0.1535 |
815.803 |
313.15 |
0.2050 |
817.465 |
313.15 |
0.2574 |
819.222 |
313.15 |
0.3054 |
820.932 |
313.15 |
0.4003 |
824.625 |
313.15 |
0.5004 |
829.064 |
313.15 |
0.6111 |
834.743 |
313.15 |
0.7032 |
840.294 |
313.15 |
0.8116 |
848.0 |
313.15 |
0.9048 |
855.903 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0541 |
1344.5 |
298.15 |
0.1044 |
1341.3 |
298.15 |
0.1535 |
1337.5 |
298.15 |
0.2050 |
1333.5 |
298.15 |
0.2574 |
1329.8 |
298.15 |
0.3054 |
1326.5 |
298.15 |
0.4003 |
1319.6 |
298.15 |
0.5004 |
1312.2 |
298.15 |
0.6111 |
1302.9 |
298.15 |
0.7032 |
1295.5 |
298.15 |
0.8116 |
1287.9 |
298.15 |
0.9048 |
1281.7 |
303.15 |
0.0541 |
1327.7 |
303.15 |
0.1044 |
1324.3 |
303.15 |
0.1535 |
1320.4 |
303.15 |
0.2050 |
1316.0 |
303.15 |
0.2574 |
1312.4 |
303.15 |
0.3054 |
1308.7 |
303.15 |
0.4003 |
1301.4 |
303.15 |
0.5004 |
1293.4 |
303.15 |
0.6111 |
1283.4 |
303.15 |
0.7032 |
1275.5 |
303.15 |
0.8116 |
1266.9 |
303.15 |
0.9048 |
1259.7 |
308.15 |
0.0541 |
1310.7 |
308.15 |
0.1044 |
1307.3 |
308.15 |
0.1535 |
1303.0 |
308.15 |
0.2050 |
1298.8 |
308.15 |
0.2574 |
1294.7 |
308.15 |
0.3054 |
1290.9 |
308.15 |
0.4003 |
1283.1 |
308.15 |
0.5004 |
1274.6 |
308.15 |
0.6111 |
1264.1 |
308.15 |
0.7032 |
1255.2 |
308.15 |
0.8116 |
1244.9 |
308.15 |
0.9048 |
1237.0 |
313.15 |
0.0541 |
1294.2 |
313.15 |
0.1044 |
1290.6 |
313.15 |
0.1535 |
1286.2 |
313.15 |
0.2050 |
1282.0 |
313.15 |
0.2574 |
1277.6 |
313.15 |
0.3054 |
1273.8 |
313.15 |
0.4003 |
1265.5 |
313.15 |
0.5004 |
1256.5 |
313.15 |
0.6111 |
1245.4 |
313.15 |
0.7032 |
1236.1 |
313.15 |
0.8116 |
1225.0 |
313.15 |
0.9048 |
1216.3 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0541 |
1344.5 |
298.15 |
0.1044 |
1341.3 |
298.15 |
0.1535 |
1337.5 |
298.15 |
0.2050 |
1333.5 |
298.15 |
0.2574 |
1329.8 |
298.15 |
0.3054 |
1326.5 |
298.15 |
0.4003 |
1319.6 |
298.15 |
0.5004 |
1312.2 |
298.15 |
0.6111 |
1302.9 |
298.15 |
0.7032 |
1295.5 |
298.15 |
0.8116 |
1287.9 |
298.15 |
0.9048 |
1281.7 |
303.15 |
0.0541 |
1327.7 |
303.15 |
0.1044 |
1324.3 |
303.15 |
0.1535 |
1320.4 |
303.15 |
0.2050 |
1316.0 |
303.15 |
0.2574 |
1312.4 |
303.15 |
0.3054 |
1308.7 |
303.15 |
0.4003 |
1301.4 |
303.15 |
0.5004 |
1293.4 |
303.15 |
0.6111 |
1283.4 |
303.15 |
0.7032 |
1275.5 |
303.15 |
0.8116 |
1266.9 |
303.15 |
0.9048 |
1259.7 |
308.15 |
0.0541 |
1310.7 |
308.15 |
0.1044 |
1307.3 |
308.15 |
0.1535 |
1303.0 |
308.15 |
0.2050 |
1298.8 |
308.15 |
0.2574 |
1294.7 |
308.15 |
0.3054 |
1290.9 |
308.15 |
0.4003 |
1283.1 |
308.15 |
0.5004 |
1274.6 |
308.15 |
0.6111 |
1264.1 |
308.15 |
0.7032 |
1255.2 |
308.15 |
0.8116 |
1244.9 |
308.15 |
0.9048 |
1237.0 |
313.15 |
0.0541 |
1294.2 |
313.15 |
0.1044 |
1290.6 |
313.15 |
0.1535 |
1286.2 |
313.15 |
0.2050 |
1282.0 |
313.15 |
0.2574 |
1277.6 |
313.15 |
0.3054 |
1273.8 |
313.15 |
0.4003 |
1265.5 |
313.15 |
0.5004 |
1256.5 |
313.15 |
0.6111 |
1245.4 |
313.15 |
0.7032 |
1236.1 |
313.15 |
0.8116 |
1225.0 |
313.15 |
0.9048 |
1216.3 |
Sources