- Name
- Ethanol, 2,2,2-trifluoro-
- InChI
- InChI=1S/C2H3F3O/c3-2(4,5)1-6/h6H,1H2
- InChI Key
- RHQDFWAXVIIEBN-UHFFFAOYSA-N
- Formula
- C2H3F3O
- SMILES
- OCC(F)(F)F
- Mol. Weight (g/mol)
- 100.04
- CAS
- 75-89-8
- Name
- Tetrahydrofuran
- InChI
- InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
- InChI Key
- WYURNTSHIVDZCO-UHFFFAOYSA-N
- Formula
- C4H8O
- SMILES
- C1CCOC1
- Mol. Weight (g/mol)
- 72.11
- CAS
- 109-99-9
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Datasets
- η - Viscosity, Pa*s (2)
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (2)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.1022 | 0.0021 |
| 283.15 | 0.2018 | 0.0016 |
| 283.15 | 0.3033 | 0.0012 |
| 283.15 | 0.4037 | 0.0010 |
| 283.15 | 0.5014 | 0.0009 |
| 283.15 | 0.6036 | 0.0008 |
| 283.15 | 0.7004 | 0.0007 |
| 283.15 | 0.8532 | 0.0006 |
| 283.15 | 0.9033 | 0.0006 |
| 298.15 | 0.1022 | 0.0015 |
| 298.15 | 0.2018 | 0.0012 |
| 298.15 | 0.3033 | 0.0010 |
| 298.15 | 0.4037 | 0.0008 |
| 298.15 | 0.5014 | 0.0007 |
| 298.15 | 0.6036 | 0.0006 |
| 298.15 | 0.7004 | 0.0006 |
| 298.15 | 0.8532 | 0.0005 |
| 298.15 | 0.9033 | 0.0005 |
| 313.15 | 0.1022 | 0.0011 |
| 313.15 | 0.2018 | 0.0009 |
| 313.15 | 0.3033 | 0.0008 |
| 313.15 | 0.4037 | 0.0007 |
| 313.15 | 0.5014 | 0.0006 |
| 313.15 | 0.6036 | 0.0005 |
| 313.15 | 0.7004 | 0.0005 |
| 313.15 | 0.8532 | 0.0004 |
| 313.15 | 0.9033 | 0.0004 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.1022 | 0.0021 |
| 283.15 | 0.2018 | 0.0016 |
| 283.15 | 0.3033 | 0.0012 |
| 283.15 | 0.4037 | 0.0010 |
| 283.15 | 0.5014 | 0.0009 |
| 283.15 | 0.6036 | 0.0008 |
| 283.15 | 0.7004 | 0.0007 |
| 283.15 | 0.8532 | 0.0006 |
| 283.15 | 0.9033 | 0.0006 |
| 298.15 | 0.1022 | 0.0015 |
| 298.15 | 0.2018 | 0.0012 |
| 298.15 | 0.3033 | 0.0010 |
| 298.15 | 0.4037 | 0.0008 |
| 298.15 | 0.5014 | 0.0007 |
| 298.15 | 0.6036 | 0.0006 |
| 298.15 | 0.7004 | 0.0006 |
| 298.15 | 0.8532 | 0.0005 |
| 298.15 | 0.9033 | 0.0005 |
| 313.15 | 0.1022 | 0.0011 |
| 313.15 | 0.2018 | 0.0009 |
| 313.15 | 0.3033 | 0.0008 |
| 313.15 | 0.4037 | 0.0007 |
| 313.15 | 0.5014 | 0.0006 |
| 313.15 | 0.6036 | 0.0005 |
| 313.15 | 0.7004 | 0.0005 |
| 313.15 | 0.8532 | 0.0004 |
| 313.15 | 0.9033 | 0.0004 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 283.15 | 0.0530 | -0.3830 |
| 283.15 | 0.1070 | -0.7230 |
| 283.15 | 0.2120 | -1.235 |
| 283.15 | 0.3160 | -1.594 |
| 283.15 | 0.4170 | -1.735 |
| 283.15 | 0.5170 | -1.729 |
| 283.15 | 0.6180 | -1.569 |
| 283.15 | 0.7170 | -1.27 |
| 283.15 | 0.8100 | -0.9040 |
| 283.15 | 0.9080 | -0.4480 |
| 283.15 | 0.9540 | -0.2130 |
| 298.15 | 0.0530 | -0.4720 |
| 298.15 | 0.1070 | -0.9390 |
| 298.15 | 0.2120 | -1.543 |
| 298.15 | 0.3160 | -1.883 |
| 298.15 | 0.4170 | -2.003 |
| 298.15 | 0.5170 | -1.956 |
| 298.15 | 0.6180 | -1.751 |
| 298.15 | 0.7170 | -1.427 |
| 298.15 | 0.8100 | -0.9930 |
| 298.15 | 0.9080 | -0.4890 |
| 298.15 | 0.9540 | -0.2340 |
| 313.15 | 0.0530 | -0.4740 |
| 313.15 | 0.1070 | -0.9280 |
| 313.15 | 0.2120 | -1.57 |
| 313.15 | 0.3160 | -1.984 |
| 313.15 | 0.4170 | -2.144 |
| 313.15 | 0.5170 | -2.094 |
| 313.15 | 0.6180 | -1.869 |
| 313.15 | 0.7170 | -1.51 |
| 313.15 | 0.8100 | -1.063 |
| 313.15 | 0.9080 | -0.5250 |
| 313.15 | 0.9540 | -0.2570 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 283.15 | 0.0530 | -0.3830 |
| 283.15 | 0.1070 | -0.7230 |
| 283.15 | 0.2120 | -1.235 |
| 283.15 | 0.3160 | -1.594 |
| 283.15 | 0.4170 | -1.735 |
| 283.15 | 0.5170 | -1.729 |
| 283.15 | 0.6180 | -1.569 |
| 283.15 | 0.7170 | -1.27 |
| 283.15 | 0.8100 | -0.9040 |
| 283.15 | 0.9080 | -0.4480 |
| 283.15 | 0.9540 | -0.2130 |
| 298.15 | 0.0530 | -0.4720 |
| 298.15 | 0.1070 | -0.9390 |
| 298.15 | 0.2120 | -1.543 |
| 298.15 | 0.3160 | -1.883 |
| 298.15 | 0.4170 | -2.003 |
| 298.15 | 0.5170 | -1.956 |
| 298.15 | 0.6180 | -1.751 |
| 298.15 | 0.7170 | -1.427 |
| 298.15 | 0.8100 | -0.9930 |
| 298.15 | 0.9080 | -0.4890 |
| 298.15 | 0.9540 | -0.2340 |
| 313.15 | 0.0530 | -0.4740 |
| 313.15 | 0.1070 | -0.9280 |
| 313.15 | 0.2120 | -1.57 |
| 313.15 | 0.3160 | -1.984 |
| 313.15 | 0.4170 | -2.144 |
| 313.15 | 0.5170 | -2.094 |
| 313.15 | 0.6180 | -1.869 |
| 313.15 | 0.7170 | -1.51 |
| 313.15 | 0.8100 | -1.063 |
| 313.15 | 0.9080 | -0.5250 |
| 313.15 | 0.9540 | -0.2570 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.1087 | 1336.89 |
| 283.15 | 0.2084 | 1277.4 |
| 283.15 | 0.2990 | 1226.31 |
| 283.15 | 0.4038 | 1171.02 |
| 283.15 | 0.4953 | 1125.37 |
| 283.15 | 0.5967 | 1076.79 |
| 283.15 | 0.7048 | 1027.26 |
| 283.15 | 0.8048 | 982.37 |
| 283.15 | 0.8868 | 946.79 |
| 283.15 | 0.9657 | 913.1 |
| 298.15 | 0.0362 | 1358.26 |
| 298.15 | 0.1041 | 1315.13 |
| 298.15 | 0.2053 | 1255.19 |
| 298.15 | 0.3031 | 1201.4 |
| 298.15 | 0.4018 | 1150.15 |
| 298.15 | 0.4986 | 1103.07 |
| 298.15 | 0.5989 | 1055.77 |
| 298.15 | 0.7019 | 1009.19 |
| 298.15 | 0.7978 | 967.32 |
| 298.15 | 0.8990 | 924.33 |
| 313.15 | 0.1024 | 1291.64 |
| 313.15 | 0.1991 | 1234.96 |
| 313.15 | 0.3032 | 1178.51 |
| 313.15 | 0.3554 | 1151.61 |
| 313.15 | 0.4972 | 1082.56 |
| 313.15 | 0.5960 | 1037.96 |
| 313.15 | 0.7191 | 983.05 |
| 313.15 | 0.7922 | 952.13 |
| 313.15 | 0.8937 | 909.37 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.1087 | 1336.89 |
| 283.15 | 0.2084 | 1277.4 |
| 283.15 | 0.2990 | 1226.31 |
| 283.15 | 0.4038 | 1171.02 |
| 283.15 | 0.4953 | 1125.37 |
| 283.15 | 0.5967 | 1076.79 |
| 283.15 | 0.7048 | 1027.26 |
| 283.15 | 0.8048 | 982.37 |
| 283.15 | 0.8868 | 946.79 |
| 283.15 | 0.9657 | 913.1 |
| 298.15 | 0.0362 | 1358.26 |
| 298.15 | 0.1041 | 1315.13 |
| 298.15 | 0.2053 | 1255.19 |
| 298.15 | 0.3031 | 1201.4 |
| 298.15 | 0.4018 | 1150.15 |
| 298.15 | 0.4986 | 1103.07 |
| 298.15 | 0.5989 | 1055.77 |
| 298.15 | 0.7019 | 1009.19 |
| 298.15 | 0.7978 | 967.32 |
| 298.15 | 0.8990 | 924.33 |
| 313.15 | 0.1024 | 1291.64 |
| 313.15 | 0.1991 | 1234.96 |
| 313.15 | 0.3032 | 1178.51 |
| 313.15 | 0.3554 | 1151.61 |
| 313.15 | 0.4972 | 1082.56 |
| 313.15 | 0.5960 | 1037.96 |
| 313.15 | 0.7191 | 983.05 |
| 313.15 | 0.7922 | 952.13 |
| 313.15 | 0.8937 | 909.37 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Speed of sound, m/s - Liquid |
| 283.15 | 0.1087 | 897.7 |
| 283.15 | 0.2084 | 932.6 |
| 283.15 | 0.2990 | 966.8 |
| 283.15 | 0.4038 | 1010.1 |
| 283.15 | 0.4953 | 1052.1 |
| 283.15 | 0.6013 | 1104.4 |
| 283.15 | 0.7048 | 1161.1 |
| 283.15 | 0.7958 | 1213.8 |
| 283.15 | 0.9058 | 1283.2 |
| 283.15 | 0.9657 | 1324.1 |
| 298.15 | 0.1106 | 854.6 |
| 298.15 | 0.2095 | 885.0 |
| 298.15 | 0.3019 | 917.9 |
| 298.15 | 0.4065 | 959.4 |
| 298.15 | 0.5076 | 1003.3 |
| 298.15 | 0.6172 | 1055.8 |
| 298.15 | 0.7123 | 1104.9 |
| 298.15 | 0.8205 | 1164.5 |
| 298.15 | 0.9042 | 1216.3 |
| 313.15 | 0.1024 | 808.3 |
| 313.15 | 0.1991 | 834.3 |
| 313.15 | 0.3032 | 868.4 |
| 313.15 | 0.3554 | 886.4 |
| 313.15 | 0.4972 | 942.6 |
| 313.15 | 0.5960 | 985.9 |
| 313.15 | 0.7191 | 1045.5 |
| 313.15 | 0.7922 | 1082.8 |
| 313.15 | 0.8937 | 1138.7 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Speed of sound, m/s - Liquid |
| 283.15 | 0.1087 | 897.7 |
| 283.15 | 0.2084 | 932.6 |
| 283.15 | 0.2990 | 966.8 |
| 283.15 | 0.4038 | 1010.1 |
| 283.15 | 0.4953 | 1052.1 |
| 283.15 | 0.6013 | 1104.4 |
| 283.15 | 0.7048 | 1161.1 |
| 283.15 | 0.7958 | 1213.8 |
| 283.15 | 0.9058 | 1283.2 |
| 283.15 | 0.9657 | 1324.1 |
| 298.15 | 0.1106 | 854.6 |
| 298.15 | 0.2095 | 885.0 |
| 298.15 | 0.3019 | 917.9 |
| 298.15 | 0.4065 | 959.4 |
| 298.15 | 0.5076 | 1003.3 |
| 298.15 | 0.6172 | 1055.8 |
| 298.15 | 0.7123 | 1104.9 |
| 298.15 | 0.8205 | 1164.5 |
| 298.15 | 0.9042 | 1216.3 |
| 313.15 | 0.1024 | 808.3 |
| 313.15 | 0.1991 | 834.3 |
| 313.15 | 0.3032 | 868.4 |
| 313.15 | 0.3554 | 886.4 |
| 313.15 | 0.4972 | 942.6 |
| 313.15 | 0.5960 | 985.9 |
| 313.15 | 0.7191 | 1045.5 |
| 313.15 | 0.7922 | 1082.8 |
| 313.15 | 0.8937 | 1138.7 |