- Name
- 1-Butanol
- InChI
- InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
- InChI Key
- LRHPLDYGYMQRHN-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CCCCO
- Mol. Weight (g/mol)
- 74.12
- CAS
- 71-36-3
- 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
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Datasets
- η - Viscosity, Pa*s (2)
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (2)
- Tboil - Boiling temperature at pressure P, K (2)
- Vapor Liquid Equilibrium at Constant Pressure (3)
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 |
| 288.15 | 0.0000 | 0.0034 |
| 288.15 | 0.1001 | 0.0024 |
| 288.15 | 0.2003 | 0.0018 |
| 288.15 | 0.3000 | 0.0014 |
| 288.15 | 0.4003 | 0.0011 |
| 288.15 | 0.5000 | 0.0010 |
| 288.15 | 0.6001 | 0.0008 |
| 288.15 | 0.7003 | 0.0007 |
| 288.15 | 0.8006 | 0.0006 |
| 288.15 | 0.9002 | 0.0006 |
| 288.15 | 1.0000 | 0.0005 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.1001 | 0.0021 |
| 293.15 | 0.2003 | 0.0016 |
| 293.15 | 0.3000 | 0.0013 |
| 293.15 | 0.4003 | 0.0011 |
| 293.15 | 0.5000 | 0.0009 |
| 293.15 | 0.6001 | 0.0008 |
| 293.15 | 0.7003 | 0.0007 |
| 293.15 | 0.8006 | 0.0006 |
| 293.15 | 0.9002 | 0.0006 |
| 293.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.1001 | 0.0019 |
| 298.15 | 0.2003 | 0.0015 |
| 298.15 | 0.3000 | 0.0012 |
| 298.15 | 0.4003 | 0.0010 |
| 298.15 | 0.5000 | 0.0008 |
| 298.15 | 0.6001 | 0.0007 |
| 298.15 | 0.7003 | 0.0006 |
| 298.15 | 0.8006 | 0.0006 |
| 298.15 | 0.9002 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.1001 | 0.0017 |
| 303.15 | 0.2003 | 0.0013 |
| 303.15 | 0.3000 | 0.0011 |
| 303.15 | 0.4003 | 0.0009 |
| 303.15 | 0.5000 | 0.0008 |
| 303.15 | 0.6001 | 0.0007 |
| 303.15 | 0.7003 | 0.0006 |
| 303.15 | 0.8006 | 0.0006 |
| 303.15 | 0.9002 | 0.0005 |
| 303.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.1001 | 0.0015 |
| 308.15 | 0.2003 | 0.0012 |
| 308.15 | 0.3000 | 0.0010 |
| 308.15 | 0.4003 | 0.0008 |
| 308.15 | 0.5000 | 0.0007 |
| 308.15 | 0.6001 | 0.0007 |
| 308.15 | 0.7003 | 0.0006 |
| 308.15 | 0.8006 | 0.0005 |
| 308.15 | 0.9002 | 0.0005 |
| 308.15 | 1.0000 | 0.0004 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.1001 | 0.0014 |
| 313.15 | 0.2003 | 0.0011 |
| 313.15 | 0.3000 | 0.0009 |
| 313.15 | 0.4003 | 0.0008 |
| 313.15 | 0.5000 | 0.0007 |
| 313.15 | 0.6001 | 0.0006 |
| 313.15 | 0.7003 | 0.0005 |
| 313.15 | 0.8006 | 0.0005 |
| 313.15 | 0.9002 | 0.0005 |
| 313.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.1001 | 0.0012 |
| 318.15 | 0.2003 | 0.0010 |
| 318.15 | 0.3000 | 0.0009 |
| 318.15 | 0.4003 | 0.0007 |
| 318.15 | 0.5000 | 0.0006 |
| 318.15 | 0.6001 | 0.0006 |
| 318.15 | 0.7003 | 0.0005 |
| 318.15 | 0.8006 | 0.0005 |
| 318.15 | 0.9002 | 0.0004 |
| 318.15 | 1.0000 | 0.0004 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.1001 | 0.0011 |
| 323.15 | 0.2003 | 0.0009 |
| 323.15 | 0.3000 | 0.0008 |
| 323.15 | 0.4003 | 0.0007 |
| 323.15 | 0.5000 | 0.0006 |
| 323.15 | 0.6001 | 0.0005 |
| 323.15 | 0.7003 | 0.0005 |
| 323.15 | 0.8006 | 0.0004 |
| 323.15 | 0.9002 | 0.0004 |
| 323.15 | 1.0000 | 0.0004 |
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 |
| 288.15 | 0.0000 | 0.0034 |
| 288.15 | 0.1001 | 0.0024 |
| 288.15 | 0.2003 | 0.0018 |
| 288.15 | 0.3000 | 0.0014 |
| 288.15 | 0.4003 | 0.0011 |
| 288.15 | 0.5000 | 0.0010 |
| 288.15 | 0.6001 | 0.0008 |
| 288.15 | 0.7003 | 0.0007 |
| 288.15 | 0.8006 | 0.0006 |
| 288.15 | 0.9002 | 0.0006 |
| 288.15 | 1.0000 | 0.0005 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.1001 | 0.0021 |
| 293.15 | 0.2003 | 0.0016 |
| 293.15 | 0.3000 | 0.0013 |
| 293.15 | 0.4003 | 0.0011 |
| 293.15 | 0.5000 | 0.0009 |
| 293.15 | 0.6001 | 0.0008 |
| 293.15 | 0.7003 | 0.0007 |
| 293.15 | 0.8006 | 0.0006 |
| 293.15 | 0.9002 | 0.0006 |
| 293.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.1001 | 0.0019 |
| 298.15 | 0.2003 | 0.0015 |
| 298.15 | 0.3000 | 0.0012 |
| 298.15 | 0.4003 | 0.0010 |
| 298.15 | 0.5000 | 0.0008 |
| 298.15 | 0.6001 | 0.0007 |
| 298.15 | 0.7003 | 0.0006 |
| 298.15 | 0.8006 | 0.0006 |
| 298.15 | 0.9002 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.1001 | 0.0017 |
| 303.15 | 0.2003 | 0.0013 |
| 303.15 | 0.3000 | 0.0011 |
| 303.15 | 0.4003 | 0.0009 |
| 303.15 | 0.5000 | 0.0008 |
| 303.15 | 0.6001 | 0.0007 |
| 303.15 | 0.7003 | 0.0006 |
| 303.15 | 0.8006 | 0.0006 |
| 303.15 | 0.9002 | 0.0005 |
| 303.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.1001 | 0.0015 |
| 308.15 | 0.2003 | 0.0012 |
| 308.15 | 0.3000 | 0.0010 |
| 308.15 | 0.4003 | 0.0008 |
| 308.15 | 0.5000 | 0.0007 |
| 308.15 | 0.6001 | 0.0007 |
| 308.15 | 0.7003 | 0.0006 |
| 308.15 | 0.8006 | 0.0005 |
| 308.15 | 0.9002 | 0.0005 |
| 308.15 | 1.0000 | 0.0004 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.1001 | 0.0014 |
| 313.15 | 0.2003 | 0.0011 |
| 313.15 | 0.3000 | 0.0009 |
| 313.15 | 0.4003 | 0.0008 |
| 313.15 | 0.5000 | 0.0007 |
| 313.15 | 0.6001 | 0.0006 |
| 313.15 | 0.7003 | 0.0005 |
| 313.15 | 0.8006 | 0.0005 |
| 313.15 | 0.9002 | 0.0005 |
| 313.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.1001 | 0.0012 |
| 318.15 | 0.2003 | 0.0010 |
| 318.15 | 0.3000 | 0.0009 |
| 318.15 | 0.4003 | 0.0007 |
| 318.15 | 0.5000 | 0.0006 |
| 318.15 | 0.6001 | 0.0006 |
| 318.15 | 0.7003 | 0.0005 |
| 318.15 | 0.8006 | 0.0005 |
| 318.15 | 0.9002 | 0.0004 |
| 318.15 | 1.0000 | 0.0004 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.1001 | 0.0011 |
| 323.15 | 0.2003 | 0.0009 |
| 323.15 | 0.3000 | 0.0008 |
| 323.15 | 0.4003 | 0.0007 |
| 323.15 | 0.5000 | 0.0006 |
| 323.15 | 0.6001 | 0.0005 |
| 323.15 | 0.7003 | 0.0005 |
| 323.15 | 0.8006 | 0.0004 |
| 323.15 | 0.9002 | 0.0004 |
| 323.15 | 1.0000 | 0.0004 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4014 |
| 288.15 | 0.1001 | 1.402 |
| 288.15 | 0.2003 | 1.4028 |
| 288.15 | 0.3000 | 1.4036 |
| 288.15 | 0.4003 | 1.4043 |
| 288.15 | 0.5000 | 1.4051 |
| 288.15 | 0.6001 | 1.4059 |
| 288.15 | 0.7003 | 1.4068 |
| 288.15 | 0.8006 | 1.4077 |
| 288.15 | 0.9002 | 1.4087 |
| 288.15 | 1.0000 | 1.4096 |
| 293.15 | 0.0000 | 1.3993 |
| 293.15 | 0.1001 | 1.3999 |
| 293.15 | 0.2003 | 1.4006 |
| 293.15 | 0.3000 | 1.4013 |
| 293.15 | 0.4003 | 1.4021 |
| 293.15 | 0.5000 | 1.4028 |
| 293.15 | 0.6001 | 1.4035 |
| 293.15 | 0.7003 | 1.4044 |
| 293.15 | 0.8006 | 1.4052 |
| 293.15 | 0.9002 | 1.4061 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.3973 |
| 298.15 | 0.1001 | 1.3978 |
| 298.15 | 0.2003 | 1.3985 |
| 298.15 | 0.3000 | 1.3991 |
| 298.15 | 0.4003 | 1.3998 |
| 298.15 | 0.5000 | 1.4004 |
| 298.15 | 0.6001 | 1.4011 |
| 298.15 | 0.7003 | 1.4019 |
| 298.15 | 0.8006 | 1.4027 |
| 298.15 | 0.9002 | 1.4035 |
| 298.15 | 1.0000 | 1.4043 |
| 303.15 | 0.0000 | 1.3952 |
| 303.15 | 0.1001 | 1.3957 |
| 303.15 | 0.2003 | 1.3963 |
| 303.15 | 0.3000 | 1.3969 |
| 303.15 | 0.4003 | 1.3974 |
| 303.15 | 0.5000 | 1.398 |
| 303.15 | 0.6001 | 1.3987 |
| 303.15 | 0.7003 | 1.3994 |
| 303.15 | 0.8006 | 1.4001 |
| 303.15 | 0.9002 | 1.4009 |
| 303.15 | 1.0000 | 1.4016 |
| 308.15 | 0.0000 | 1.3932 |
| 308.15 | 0.1001 | 1.3936 |
| 308.15 | 0.2003 | 1.3941 |
| 308.15 | 0.3000 | 1.3946 |
| 308.15 | 0.4003 | 1.3951 |
| 308.15 | 0.5000 | 1.3957 |
| 308.15 | 0.6001 | 1.3962 |
| 308.15 | 0.7003 | 1.3969 |
| 308.15 | 0.8006 | 1.3975 |
| 308.15 | 0.9002 | 1.3983 |
| 308.15 | 1.0000 | 1.399 |
| 313.15 | 0.0000 | 1.3911 |
| 313.15 | 0.1001 | 1.3914 |
| 313.15 | 0.2003 | 1.3919 |
| 313.15 | 0.3000 | 1.3923 |
| 313.15 | 0.4003 | 1.3928 |
| 313.15 | 0.5000 | 1.3933 |
| 313.15 | 0.6001 | 1.3938 |
| 313.15 | 0.7003 | 1.3943 |
| 313.15 | 0.8006 | 1.3949 |
| 313.15 | 0.9002 | 1.3956 |
| 313.15 | 1.0000 | 1.3963 |
| 318.15 | 0.0000 | 1.389 |
| 318.15 | 0.1001 | 1.3893 |
| 318.15 | 0.2003 | 1.3897 |
| 318.15 | 0.3000 | 1.3901 |
| 318.15 | 0.4003 | 1.3905 |
| 318.15 | 0.5000 | 1.3909 |
| 318.15 | 0.6001 | 1.3913 |
| 318.15 | 0.7003 | 1.3918 |
| 318.15 | 0.8006 | 1.3923 |
| 318.15 | 0.9002 | 1.3929 |
| 318.15 | 1.0000 | 1.3936 |
| 323.15 | 0.0000 | 1.3869 |
| 323.15 | 0.1001 | 1.3871 |
| 323.15 | 0.2003 | 1.3874 |
| 323.15 | 0.3000 | 1.3878 |
| 323.15 | 0.4003 | 1.3881 |
| 323.15 | 0.5000 | 1.3885 |
| 323.15 | 0.6001 | 1.3888 |
| 323.15 | 0.7003 | 1.3893 |
| 323.15 | 0.8006 | 1.3897 |
| 323.15 | 0.9002 | 1.3903 |
| 323.15 | 1.0000 | 1.3909 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4014 |
| 288.15 | 0.1001 | 1.402 |
| 288.15 | 0.2003 | 1.4028 |
| 288.15 | 0.3000 | 1.4036 |
| 288.15 | 0.4003 | 1.4043 |
| 288.15 | 0.5000 | 1.4051 |
| 288.15 | 0.6001 | 1.4059 |
| 288.15 | 0.7003 | 1.4068 |
| 288.15 | 0.8006 | 1.4077 |
| 288.15 | 0.9002 | 1.4087 |
| 288.15 | 1.0000 | 1.4096 |
| 293.15 | 0.0000 | 1.3993 |
| 293.15 | 0.1001 | 1.3999 |
| 293.15 | 0.2003 | 1.4006 |
| 293.15 | 0.3000 | 1.4013 |
| 293.15 | 0.4003 | 1.4021 |
| 293.15 | 0.5000 | 1.4028 |
| 293.15 | 0.6001 | 1.4035 |
| 293.15 | 0.7003 | 1.4044 |
| 293.15 | 0.8006 | 1.4052 |
| 293.15 | 0.9002 | 1.4061 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.3973 |
| 298.15 | 0.1001 | 1.3978 |
| 298.15 | 0.2003 | 1.3985 |
| 298.15 | 0.3000 | 1.3991 |
| 298.15 | 0.4003 | 1.3998 |
| 298.15 | 0.5000 | 1.4004 |
| 298.15 | 0.6001 | 1.4011 |
| 298.15 | 0.7003 | 1.4019 |
| 298.15 | 0.8006 | 1.4027 |
| 298.15 | 0.9002 | 1.4035 |
| 298.15 | 1.0000 | 1.4043 |
| 303.15 | 0.0000 | 1.3952 |
| 303.15 | 0.1001 | 1.3957 |
| 303.15 | 0.2003 | 1.3963 |
| 303.15 | 0.3000 | 1.3969 |
| 303.15 | 0.4003 | 1.3974 |
| 303.15 | 0.5000 | 1.398 |
| 303.15 | 0.6001 | 1.3987 |
| 303.15 | 0.7003 | 1.3994 |
| 303.15 | 0.8006 | 1.4001 |
| 303.15 | 0.9002 | 1.4009 |
| 303.15 | 1.0000 | 1.4016 |
| 308.15 | 0.0000 | 1.3932 |
| 308.15 | 0.1001 | 1.3936 |
| 308.15 | 0.2003 | 1.3941 |
| 308.15 | 0.3000 | 1.3946 |
| 308.15 | 0.4003 | 1.3951 |
| 308.15 | 0.5000 | 1.3957 |
| 308.15 | 0.6001 | 1.3962 |
| 308.15 | 0.7003 | 1.3969 |
| 308.15 | 0.8006 | 1.3975 |
| 308.15 | 0.9002 | 1.3983 |
| 308.15 | 1.0000 | 1.399 |
| 313.15 | 0.0000 | 1.3911 |
| 313.15 | 0.1001 | 1.3914 |
| 313.15 | 0.2003 | 1.3919 |
| 313.15 | 0.3000 | 1.3923 |
| 313.15 | 0.4003 | 1.3928 |
| 313.15 | 0.5000 | 1.3933 |
| 313.15 | 0.6001 | 1.3938 |
| 313.15 | 0.7003 | 1.3943 |
| 313.15 | 0.8006 | 1.3949 |
| 313.15 | 0.9002 | 1.3956 |
| 313.15 | 1.0000 | 1.3963 |
| 318.15 | 0.0000 | 1.389 |
| 318.15 | 0.1001 | 1.3893 |
| 318.15 | 0.2003 | 1.3897 |
| 318.15 | 0.3000 | 1.3901 |
| 318.15 | 0.4003 | 1.3905 |
| 318.15 | 0.5000 | 1.3909 |
| 318.15 | 0.6001 | 1.3913 |
| 318.15 | 0.7003 | 1.3918 |
| 318.15 | 0.8006 | 1.3923 |
| 318.15 | 0.9002 | 1.3929 |
| 318.15 | 1.0000 | 1.3936 |
| 323.15 | 0.0000 | 1.3869 |
| 323.15 | 0.1001 | 1.3871 |
| 323.15 | 0.2003 | 1.3874 |
| 323.15 | 0.3000 | 1.3878 |
| 323.15 | 0.4003 | 1.3881 |
| 323.15 | 0.5000 | 1.3885 |
| 323.15 | 0.6001 | 1.3888 |
| 323.15 | 0.7003 | 1.3893 |
| 323.15 | 0.8006 | 1.3897 |
| 323.15 | 0.9002 | 1.3903 |
| 323.15 | 1.0000 | 1.3909 |
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 |
| 288.15 | 0.0000 | 813.37 |
| 288.15 | 0.1001 | 820.7 |
| 288.15 | 0.2003 | 828.11 |
| 288.15 | 0.3000 | 835.61 |
| 288.15 | 0.4003 | 843.28 |
| 288.15 | 0.5000 | 851.03 |
| 288.15 | 0.6001 | 858.98 |
| 288.15 | 0.7003 | 867.19 |
| 288.15 | 0.8006 | 875.64 |
| 288.15 | 0.9002 | 884.34 |
| 288.15 | 1.0000 | 893.29 |
| 293.15 | 0.0000 | 809.57 |
| 293.15 | 0.1001 | 816.75 |
| 293.15 | 0.2003 | 823.99 |
| 293.15 | 0.3000 | 831.34 |
| 293.15 | 0.4003 | 838.84 |
| 293.15 | 0.5000 | 846.43 |
| 293.15 | 0.6001 | 854.21 |
| 293.15 | 0.7003 | 862.27 |
| 293.15 | 0.8006 | 870.54 |
| 293.15 | 0.9002 | 879.08 |
| 293.15 | 1.0000 | 887.86 |
| 298.15 | 0.0000 | 805.76 |
| 298.15 | 0.1001 | 812.77 |
| 298.15 | 0.2003 | 819.86 |
| 298.15 | 0.3000 | 827.04 |
| 298.15 | 0.4003 | 834.38 |
| 298.15 | 0.5000 | 841.8 |
| 298.15 | 0.6001 | 849.43 |
| 298.15 | 0.7003 | 857.31 |
| 298.15 | 0.8006 | 865.41 |
| 298.15 | 0.9002 | 873.78 |
| 298.15 | 1.0000 | 882.4 |
| 303.15 | 0.0000 | 801.92 |
| 303.15 | 0.1001 | 808.76 |
| 303.15 | 0.2003 | 815.69 |
| 303.15 | 0.3000 | 822.71 |
| 303.15 | 0.4003 | 829.89 |
| 303.15 | 0.5000 | 837.15 |
| 303.15 | 0.6001 | 844.61 |
| 303.15 | 0.7003 | 852.32 |
| 303.15 | 0.8006 | 860.26 |
| 303.15 | 0.9002 | 868.46 |
| 303.15 | 1.0000 | 876.91 |
| 308.15 | 0.0000 | 798.05 |
| 308.15 | 0.1001 | 804.73 |
| 308.15 | 0.2003 | 811.49 |
| 308.15 | 0.3000 | 818.36 |
| 308.15 | 0.4003 | 825.36 |
| 308.15 | 0.5000 | 832.46 |
| 308.15 | 0.6001 | 839.75 |
| 308.15 | 0.7003 | 847.3 |
| 308.15 | 0.8006 | 855.06 |
| 308.15 | 0.9002 | 863.09 |
| 308.15 | 1.0000 | 871.38 |
| 313.15 | 0.0000 | 794.15 |
| 313.15 | 0.1001 | 800.66 |
| 313.15 | 0.2003 | 807.26 |
| 313.15 | 0.3000 | 813.96 |
| 313.15 | 0.4003 | 820.81 |
| 313.15 | 0.5000 | 827.74 |
| 313.15 | 0.6001 | 834.86 |
| 313.15 | 0.7003 | 842.24 |
| 313.15 | 0.8006 | 849.83 |
| 313.15 | 0.9002 | 857.7 |
| 313.15 | 1.0000 | 865.81 |
| 318.15 | 0.0000 | 790.23 |
| 318.15 | 0.1001 | 796.55 |
| 318.15 | 0.2003 | 802.99 |
| 318.15 | 0.3000 | 809.53 |
| 318.15 | 0.4003 | 816.21 |
| 318.15 | 0.5000 | 822.98 |
| 318.15 | 0.6001 | 829.93 |
| 318.15 | 0.7003 | 837.14 |
| 318.15 | 0.8006 | 844.56 |
| 318.15 | 0.9002 | 852.25 |
| 318.15 | 1.0000 | 860.2 |
| 323.15 | 0.0000 | 786.24 |
| 323.15 | 0.1001 | 792.4 |
| 323.15 | 0.2003 | 798.67 |
| 323.15 | 0.3000 | 805.05 |
| 323.15 | 0.4003 | 811.57 |
| 323.15 | 0.5000 | 818.17 |
| 323.15 | 0.6001 | 824.96 |
| 323.15 | 0.7003 | 832.0 |
| 323.15 | 0.8006 | 839.25 |
| 323.15 | 0.9002 | 846.77 |
| 323.15 | 1.0000 | 854.55 |
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 |
| 288.15 | 0.0000 | 813.37 |
| 288.15 | 0.1001 | 820.7 |
| 288.15 | 0.2003 | 828.11 |
| 288.15 | 0.3000 | 835.61 |
| 288.15 | 0.4003 | 843.28 |
| 288.15 | 0.5000 | 851.03 |
| 288.15 | 0.6001 | 858.98 |
| 288.15 | 0.7003 | 867.19 |
| 288.15 | 0.8006 | 875.64 |
| 288.15 | 0.9002 | 884.34 |
| 288.15 | 1.0000 | 893.29 |
| 293.15 | 0.0000 | 809.57 |
| 293.15 | 0.1001 | 816.75 |
| 293.15 | 0.2003 | 823.99 |
| 293.15 | 0.3000 | 831.34 |
| 293.15 | 0.4003 | 838.84 |
| 293.15 | 0.5000 | 846.43 |
| 293.15 | 0.6001 | 854.21 |
| 293.15 | 0.7003 | 862.27 |
| 293.15 | 0.8006 | 870.54 |
| 293.15 | 0.9002 | 879.08 |
| 293.15 | 1.0000 | 887.86 |
| 298.15 | 0.0000 | 805.76 |
| 298.15 | 0.1001 | 812.77 |
| 298.15 | 0.2003 | 819.86 |
| 298.15 | 0.3000 | 827.04 |
| 298.15 | 0.4003 | 834.38 |
| 298.15 | 0.5000 | 841.8 |
| 298.15 | 0.6001 | 849.43 |
| 298.15 | 0.7003 | 857.31 |
| 298.15 | 0.8006 | 865.41 |
| 298.15 | 0.9002 | 873.78 |
| 298.15 | 1.0000 | 882.4 |
| 303.15 | 0.0000 | 801.92 |
| 303.15 | 0.1001 | 808.76 |
| 303.15 | 0.2003 | 815.69 |
| 303.15 | 0.3000 | 822.71 |
| 303.15 | 0.4003 | 829.89 |
| 303.15 | 0.5000 | 837.15 |
| 303.15 | 0.6001 | 844.61 |
| 303.15 | 0.7003 | 852.32 |
| 303.15 | 0.8006 | 860.26 |
| 303.15 | 0.9002 | 868.46 |
| 303.15 | 1.0000 | 876.91 |
| 308.15 | 0.0000 | 798.05 |
| 308.15 | 0.1001 | 804.73 |
| 308.15 | 0.2003 | 811.49 |
| 308.15 | 0.3000 | 818.36 |
| 308.15 | 0.4003 | 825.36 |
| 308.15 | 0.5000 | 832.46 |
| 308.15 | 0.6001 | 839.75 |
| 308.15 | 0.7003 | 847.3 |
| 308.15 | 0.8006 | 855.06 |
| 308.15 | 0.9002 | 863.09 |
| 308.15 | 1.0000 | 871.38 |
| 313.15 | 0.0000 | 794.15 |
| 313.15 | 0.1001 | 800.66 |
| 313.15 | 0.2003 | 807.26 |
| 313.15 | 0.3000 | 813.96 |
| 313.15 | 0.4003 | 820.81 |
| 313.15 | 0.5000 | 827.74 |
| 313.15 | 0.6001 | 834.86 |
| 313.15 | 0.7003 | 842.24 |
| 313.15 | 0.8006 | 849.83 |
| 313.15 | 0.9002 | 857.7 |
| 313.15 | 1.0000 | 865.81 |
| 318.15 | 0.0000 | 790.23 |
| 318.15 | 0.1001 | 796.55 |
| 318.15 | 0.2003 | 802.99 |
| 318.15 | 0.3000 | 809.53 |
| 318.15 | 0.4003 | 816.21 |
| 318.15 | 0.5000 | 822.98 |
| 318.15 | 0.6001 | 829.93 |
| 318.15 | 0.7003 | 837.14 |
| 318.15 | 0.8006 | 844.56 |
| 318.15 | 0.9002 | 852.25 |
| 318.15 | 1.0000 | 860.2 |
| 323.15 | 0.0000 | 786.24 |
| 323.15 | 0.1001 | 792.4 |
| 323.15 | 0.2003 | 798.67 |
| 323.15 | 0.3000 | 805.05 |
| 323.15 | 0.4003 | 811.57 |
| 323.15 | 0.5000 | 818.17 |
| 323.15 | 0.6001 | 824.96 |
| 323.15 | 0.7003 | 832.0 |
| 323.15 | 0.8006 | 839.25 |
| 323.15 | 0.9002 | 846.77 |
| 323.15 | 1.0000 | 854.55 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 95.8 (Liquid)
| Mole fraction of Tetrahydrofuran (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 389.45 |
| 0.1338 | 370.65 |
| 0.2436 | 360.45 |
| 0.3257 | 354.75 |
| 0.3918 | 350.95 |
| 0.4460 | 348.25 |
| 0.4914 | 346.35 |
| 0.6123 | 342.15 |
| 0.6637 | 340.75 |
| 0.7247 | 339.35 |
| 0.8206 | 337.95 |
| 0.8876 | 337.25 |
| 1.0000 | 337.55 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 95.8 (Liquid)
| Mole fraction of Tetrahydrofuran (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 389.45 |
| 0.1338 | 370.65 |
| 0.2436 | 360.45 |
| 0.3257 | 354.75 |
| 0.3918 | 350.95 |
| 0.4460 | 348.25 |
| 0.4914 | 346.35 |
| 0.6123 | 342.15 |
| 0.6637 | 340.75 |
| 0.7247 | 339.35 |
| 0.8206 | 337.95 |
| 0.8876 | 337.25 |
| 1.0000 | 337.55 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 101.33 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of Tetrahydrofuran (2) - Liquid | y1[mol/mol] of Tetrahydrofuran (2) - Vapour |
| 380.3 | 0.1000 | 0.3895 |
| 372.0 | 0.2000 | 0.6011 |
| 365.3 | 0.3000 | 0.7371 |
| 359.7 | 0.4000 | 0.8215 |
| 355.15 | 0.5000 | 0.8785 |
| 351.15 | 0.6000 | 0.9187 |
| 347.5 | 0.7000 | 0.9486 |
| 344.45 | 0.8000 | 0.9698 |
| 341.45 | 0.9000 | 0.9868 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 101.33 (VLE)
| T [K] - VLE | x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
|---|---|
| 383.15 | 0.0500 |
| 378.55 | 0.1000 |
| 373.95 | 0.1500 |
| 371.15 | 0.2000 |
| 368.35 | 0.2500 |
| 366.15 | 0.3000 |
| 363.75 | 0.3500 |
| 361.75 | 0.4000 |
| 359.35 | 0.4500 |
| 357.05 | 0.5000 |
| 354.75 | 0.5500 |
| 352.35 | 0.6000 |
| 349.95 | 0.6500 |
| 348.15 | 0.7000 |
| 346.35 | 0.7500 |
| 344.75 | 0.8000 |
| 343.15 | 0.8500 |
| 341.75 | 0.9000 |
| 340.35 | 0.9500 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 95.8 (VLE)
| T [K] - VLE | x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
|---|---|
| 389.45 | 0.0000 |
| 370.65 | 0.1338 |
| 360.45 | 0.2436 |
| 354.75 | 0.3257 |
| 350.95 | 0.3918 |
| 348.25 | 0.4460 |
| 346.35 | 0.4914 |
| 342.15 | 0.6123 |
| 340.75 | 0.6637 |
| 339.35 | 0.7247 |
| 337.95 | 0.8206 |
| 337.25 | 0.8876 |
| 337.55 | 1.0000 |
Sources
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
- Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) K