- 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
- Tetrahydropyran
- InChI
- InChI=1S/C5H10O/c1-2-4-6-5-3-1/h1-5H2
- InChI Key
- DHXVGJBLRPWPCS-UHFFFAOYSA-N
- Formula
- C5H10O
- SMILES
- C1CCOCC1
- Mol. Weight (g/mol)
- 86.13
- CAS
- 142-68-7
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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 Tetrahydropyran (2) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.0508 | 0.0025 |
| 283.15 | 0.1011 | 0.0023 |
| 283.15 | 0.2025 | 0.0018 |
| 283.15 | 0.3024 | 0.0015 |
| 283.15 | 0.4040 | 0.0013 |
| 283.15 | 0.5027 | 0.0012 |
| 283.15 | 0.6069 | 0.0011 |
| 283.15 | 0.7013 | 0.0011 |
| 283.15 | 0.8016 | 0.0010 |
| 283.15 | 0.9064 | 0.0010 |
| 298.15 | 0.0508 | 0.0017 |
| 298.15 | 0.1011 | 0.0016 |
| 298.15 | 0.2025 | 0.0013 |
| 298.15 | 0.3024 | 0.0012 |
| 298.15 | 0.4040 | 0.0010 |
| 298.15 | 0.5027 | 0.0010 |
| 298.15 | 0.6069 | 0.0009 |
| 298.15 | 0.7013 | 0.0008 |
| 298.15 | 0.8016 | 0.0008 |
| 298.15 | 0.9064 | 0.0008 |
| 313.15 | 0.0508 | 0.0012 |
| 313.15 | 0.1011 | 0.0011 |
| 313.15 | 0.2025 | 0.0010 |
| 313.15 | 0.3024 | 0.0009 |
| 313.15 | 0.4040 | 0.0008 |
| 313.15 | 0.5027 | 0.0008 |
| 313.15 | 0.6069 | 0.0007 |
| 313.15 | 0.7013 | 0.0007 |
| 313.15 | 0.8016 | 0.0007 |
| 313.15 | 0.9064 | 0.0007 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydropyran (2) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.0508 | 0.0025 |
| 283.15 | 0.1011 | 0.0023 |
| 283.15 | 0.2025 | 0.0018 |
| 283.15 | 0.3024 | 0.0015 |
| 283.15 | 0.4040 | 0.0013 |
| 283.15 | 0.5027 | 0.0012 |
| 283.15 | 0.6069 | 0.0011 |
| 283.15 | 0.7013 | 0.0011 |
| 283.15 | 0.8016 | 0.0010 |
| 283.15 | 0.9064 | 0.0010 |
| 298.15 | 0.0508 | 0.0017 |
| 298.15 | 0.1011 | 0.0016 |
| 298.15 | 0.2025 | 0.0013 |
| 298.15 | 0.3024 | 0.0012 |
| 298.15 | 0.4040 | 0.0010 |
| 298.15 | 0.5027 | 0.0010 |
| 298.15 | 0.6069 | 0.0009 |
| 298.15 | 0.7013 | 0.0008 |
| 298.15 | 0.8016 | 0.0008 |
| 298.15 | 0.9064 | 0.0008 |
| 313.15 | 0.0508 | 0.0012 |
| 313.15 | 0.1011 | 0.0011 |
| 313.15 | 0.2025 | 0.0010 |
| 313.15 | 0.3024 | 0.0009 |
| 313.15 | 0.4040 | 0.0008 |
| 313.15 | 0.5027 | 0.0008 |
| 313.15 | 0.6069 | 0.0007 |
| 313.15 | 0.7013 | 0.0007 |
| 313.15 | 0.8016 | 0.0007 |
| 313.15 | 0.9064 | 0.0007 |
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 Tetrahydropyran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 283.15 | 0.0650 | -0.4280 |
| 283.15 | 0.1270 | -0.7430 |
| 283.15 | 0.2480 | -1.184 |
| 283.15 | 0.3600 | -1.43 |
| 283.15 | 0.4660 | -1.513 |
| 283.15 | 0.5700 | -1.464 |
| 283.15 | 0.6640 | -1.269 |
| 283.15 | 0.7550 | -1.015 |
| 283.15 | 0.8390 | -0.7010 |
| 283.15 | 0.9210 | -0.3470 |
| 283.15 | 0.9620 | -0.1550 |
| 298.15 | 0.0650 | -0.4730 |
| 298.15 | 0.1270 | -0.8550 |
| 298.15 | 0.2480 | -1.348 |
| 298.15 | 0.3600 | -1.608 |
| 298.15 | 0.4660 | -1.689 |
| 298.15 | 0.5700 | -1.62 |
| 298.15 | 0.6640 | -1.419 |
| 298.15 | 0.7550 | -1.12 |
| 298.15 | 0.8390 | -0.7710 |
| 298.15 | 0.9210 | -0.3800 |
| 298.15 | 0.9620 | -0.1790 |
| 313.15 | 0.0650 | -0.4780 |
| 313.15 | 0.1270 | -0.9000 |
| 313.15 | 0.2480 | -1.457 |
| 313.15 | 0.3600 | -1.761 |
| 313.15 | 0.4660 | -1.856 |
| 313.15 | 0.5700 | -1.786 |
| 313.15 | 0.6640 | -1.564 |
| 313.15 | 0.7550 | -1.242 |
| 313.15 | 0.8390 | -0.8510 |
| 313.15 | 0.9210 | -0.4170 |
| 313.15 | 0.9620 | -0.1950 |
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 Tetrahydropyran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 283.15 | 0.0650 | -0.4280 |
| 283.15 | 0.1270 | -0.7430 |
| 283.15 | 0.2480 | -1.184 |
| 283.15 | 0.3600 | -1.43 |
| 283.15 | 0.4660 | -1.513 |
| 283.15 | 0.5700 | -1.464 |
| 283.15 | 0.6640 | -1.269 |
| 283.15 | 0.7550 | -1.015 |
| 283.15 | 0.8390 | -0.7010 |
| 283.15 | 0.9210 | -0.3470 |
| 283.15 | 0.9620 | -0.1550 |
| 298.15 | 0.0650 | -0.4730 |
| 298.15 | 0.1270 | -0.8550 |
| 298.15 | 0.2480 | -1.348 |
| 298.15 | 0.3600 | -1.608 |
| 298.15 | 0.4660 | -1.689 |
| 298.15 | 0.5700 | -1.62 |
| 298.15 | 0.6640 | -1.419 |
| 298.15 | 0.7550 | -1.12 |
| 298.15 | 0.8390 | -0.7710 |
| 298.15 | 0.9210 | -0.3800 |
| 298.15 | 0.9620 | -0.1790 |
| 313.15 | 0.0650 | -0.4780 |
| 313.15 | 0.1270 | -0.9000 |
| 313.15 | 0.2480 | -1.457 |
| 313.15 | 0.3600 | -1.761 |
| 313.15 | 0.4660 | -1.856 |
| 313.15 | 0.5700 | -1.786 |
| 313.15 | 0.6640 | -1.564 |
| 313.15 | 0.7550 | -1.242 |
| 313.15 | 0.8390 | -0.8510 |
| 313.15 | 0.9210 | -0.4170 |
| 313.15 | 0.9620 | -0.1950 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydropyran (2) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.1039 | 1328.18 |
| 283.15 | 0.2071 | 1259.32 |
| 283.15 | 0.3073 | 1199.39 |
| 283.15 | 0.4127 | 1142.29 |
| 283.15 | 0.5017 | 1097.77 |
| 283.15 | 0.6011 | 1051.7 |
| 283.15 | 0.7183 | 1001.3 |
| 283.15 | 0.8206 | 960.36 |
| 283.15 | 0.8955 | 931.9 |
| 298.15 | 0.1023 | 1305.58 |
| 298.15 | 0.2029 | 1239.41 |
| 298.15 | 0.3203 | 1170.85 |
| 298.15 | 0.4120 | 1122.5 |
| 298.15 | 0.5192 | 1070.38 |
| 298.15 | 0.6171 | 1026.55 |
| 298.15 | 0.7342 | 977.81 |
| 298.15 | 0.7930 | 954.59 |
| 298.15 | 0.8967 | 915.73 |
| 313.15 | 0.1028 | 1280.8 |
| 313.15 | 0.2000 | 1217.96 |
| 313.15 | 0.3049 | 1157.77 |
| 313.15 | 0.4108 | 1102.63 |
| 313.15 | 0.5040 | 1058.19 |
| 313.15 | 0.5961 | 1017.26 |
| 313.15 | 0.6986 | 974.97 |
| 313.15 | 0.8321 | 923.77 |
| 313.15 | 0.8986 | 899.6 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydropyran (2) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.1039 | 1328.18 |
| 283.15 | 0.2071 | 1259.32 |
| 283.15 | 0.3073 | 1199.39 |
| 283.15 | 0.4127 | 1142.29 |
| 283.15 | 0.5017 | 1097.77 |
| 283.15 | 0.6011 | 1051.7 |
| 283.15 | 0.7183 | 1001.3 |
| 283.15 | 0.8206 | 960.36 |
| 283.15 | 0.8955 | 931.9 |
| 298.15 | 0.1023 | 1305.58 |
| 298.15 | 0.2029 | 1239.41 |
| 298.15 | 0.3203 | 1170.85 |
| 298.15 | 0.4120 | 1122.5 |
| 298.15 | 0.5192 | 1070.38 |
| 298.15 | 0.6171 | 1026.55 |
| 298.15 | 0.7342 | 977.81 |
| 298.15 | 0.7930 | 954.59 |
| 298.15 | 0.8967 | 915.73 |
| 313.15 | 0.1028 | 1280.8 |
| 313.15 | 0.2000 | 1217.96 |
| 313.15 | 0.3049 | 1157.77 |
| 313.15 | 0.4108 | 1102.63 |
| 313.15 | 0.5040 | 1058.19 |
| 313.15 | 0.5961 | 1017.26 |
| 313.15 | 0.6986 | 974.97 |
| 313.15 | 0.8321 | 923.77 |
| 313.15 | 0.8986 | 899.6 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydropyran (2) - Liquid | Speed of sound, m/s - Liquid |
| 283.15 | 0.1039 | 903.5 |
| 283.15 | 0.2071 | 942.2 |
| 283.15 | 0.3067 | 985.6 |
| 283.15 | 0.4123 | 1034.0 |
| 283.15 | 0.5017 | 1076.2 |
| 283.15 | 0.6011 | 1124.9 |
| 283.15 | 0.7183 | 1184.3 |
| 283.15 | 0.8206 | 1237.7 |
| 283.15 | 0.8955 | 1278.1 |
| 298.15 | 0.1023 | 850.5 |
| 298.15 | 0.2029 | 886.4 |
| 298.15 | 0.3203 | 933.6 |
| 298.15 | 0.4120 | 972.6 |
| 298.15 | 0.5208 | 1021.0 |
| 298.15 | 0.6171 | 1065.4 |
| 298.15 | 0.7342 | 1121.0 |
| 298.15 | 0.7996 | 1152.3 |
| 298.15 | 0.8967 | 1201.6 |
| 313.15 | 0.0995 | 813.9 |
| 313.15 | 0.2000 | 845.8 |
| 313.15 | 0.3049 | 885.0 |
| 313.15 | 0.4111 | 927.4 |
| 313.15 | 0.5040 | 967.4 |
| 313.15 | 0.6032 | 1010.4 |
| 313.15 | 0.7330 | 1070.3 |
| 313.15 | 0.8321 | 1116.2 |
| 313.15 | 0.8988 | 1149.4 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydropyran (2) - Liquid | Speed of sound, m/s - Liquid |
| 283.15 | 0.1039 | 903.5 |
| 283.15 | 0.2071 | 942.2 |
| 283.15 | 0.3067 | 985.6 |
| 283.15 | 0.4123 | 1034.0 |
| 283.15 | 0.5017 | 1076.2 |
| 283.15 | 0.6011 | 1124.9 |
| 283.15 | 0.7183 | 1184.3 |
| 283.15 | 0.8206 | 1237.7 |
| 283.15 | 0.8955 | 1278.1 |
| 298.15 | 0.1023 | 850.5 |
| 298.15 | 0.2029 | 886.4 |
| 298.15 | 0.3203 | 933.6 |
| 298.15 | 0.4120 | 972.6 |
| 298.15 | 0.5208 | 1021.0 |
| 298.15 | 0.6171 | 1065.4 |
| 298.15 | 0.7342 | 1121.0 |
| 298.15 | 0.7996 | 1152.3 |
| 298.15 | 0.8967 | 1201.6 |
| 313.15 | 0.0995 | 813.9 |
| 313.15 | 0.2000 | 845.8 |
| 313.15 | 0.3049 | 885.0 |
| 313.15 | 0.4111 | 927.4 |
| 313.15 | 0.5040 | 967.4 |
| 313.15 | 0.6032 | 1010.4 |
| 313.15 | 0.7330 | 1070.3 |
| 313.15 | 0.8321 | 1116.2 |
| 313.15 | 0.8988 | 1149.4 |