- Name
- 1-Propanol
- InChI
- InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
- InChI Key
- BDERNNFJNOPAEC-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CCCO
- Mol. Weight (g/mol)
- 60.09
- CAS
- 71-23-8
- Name
- Cyclohexane
- InChI
- InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
- InChI Key
- XDTMQSROBMDMFD-UHFFFAOYSA-N
- Formula
- C6H12
- SMILES
- C1CCCCC1
- Mol. Weight (g/mol)
- 84.16
- CAS
- 110-82-7
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 (4)
- Excess molar enthalpy (molar enthalpy (2)
- Pvap - Vapor or sublimation pressure, kPa (2)
- ρl - Mass density, kg/m3 (4)
- csound,fluid - Speed of Sound, m/s (2)
- Binary diffusion coefficient, m2/s (2)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0022 |
| 293.15 | 0.0487 | 0.0021 |
| 293.15 | 0.0993 | 0.0020 |
| 293.15 | 0.1967 | 0.0017 |
| 293.15 | 0.2993 | 0.0015 |
| 293.15 | 0.4017 | 0.0014 |
| 293.15 | 0.5071 | 0.0013 |
| 293.15 | 0.6048 | 0.0011 |
| 293.15 | 0.7036 | 0.0010 |
| 293.15 | 0.8062 | 0.0010 |
| 293.15 | 0.9053 | 0.0010 |
| 293.15 | 0.9522 | 0.0010 |
| 293.15 | 1.0000 | 0.0010 |
| 298.15 | 0.0000 | 0.0019 |
| 298.15 | 0.0487 | 0.0018 |
| 298.15 | 0.0993 | 0.0017 |
| 298.15 | 0.1967 | 0.0015 |
| 298.15 | 0.2993 | 0.0014 |
| 298.15 | 0.4017 | 0.0012 |
| 298.15 | 0.5071 | 0.0011 |
| 298.15 | 0.6048 | 0.0010 |
| 298.15 | 0.7036 | 0.0009 |
| 298.15 | 0.8062 | 0.0009 |
| 298.15 | 0.9053 | 0.0009 |
| 298.15 | 0.9522 | 0.0009 |
| 298.15 | 1.0000 | 0.0009 |
| 303.15 | 0.0000 | 0.0017 |
| 303.15 | 0.0487 | 0.0016 |
| 303.15 | 0.0993 | 0.0016 |
| 303.15 | 0.1967 | 0.0014 |
| 303.15 | 0.2993 | 0.0012 |
| 303.15 | 0.4017 | 0.0011 |
| 303.15 | 0.5071 | 0.0010 |
| 303.15 | 0.6048 | 0.0009 |
| 303.15 | 0.7036 | 0.0009 |
| 303.15 | 0.8062 | 0.0008 |
| 303.15 | 0.9053 | 0.0008 |
| 303.15 | 0.9522 | 0.0008 |
| 303.15 | 1.0000 | 0.0008 |
Viscosity, Pa*s [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0008 |
| 0.1021 | 0.0008 |
| 0.2112 | 0.0009 |
| 0.3122 | 0.0009 |
| 0.4211 | 0.0010 |
| 0.5151 | 0.0011 |
| 0.6203 | 0.0011 |
| 0.7208 | 0.0013 |
| 0.8143 | 0.0014 |
| 0.9079 | 0.0016 |
| 1.0000 | 0.0017 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0022 |
| 293.15 | 0.0487 | 0.0021 |
| 293.15 | 0.0993 | 0.0020 |
| 293.15 | 0.1967 | 0.0017 |
| 293.15 | 0.2993 | 0.0015 |
| 293.15 | 0.4017 | 0.0014 |
| 293.15 | 0.5071 | 0.0013 |
| 293.15 | 0.6048 | 0.0011 |
| 293.15 | 0.7036 | 0.0010 |
| 293.15 | 0.8062 | 0.0010 |
| 293.15 | 0.9053 | 0.0010 |
| 293.15 | 0.9522 | 0.0010 |
| 293.15 | 1.0000 | 0.0010 |
| 298.15 | 0.0000 | 0.0019 |
| 298.15 | 0.0487 | 0.0018 |
| 298.15 | 0.0993 | 0.0017 |
| 298.15 | 0.1967 | 0.0015 |
| 298.15 | 0.2993 | 0.0014 |
| 298.15 | 0.4017 | 0.0012 |
| 298.15 | 0.5071 | 0.0011 |
| 298.15 | 0.6048 | 0.0010 |
| 298.15 | 0.7036 | 0.0009 |
| 298.15 | 0.8062 | 0.0009 |
| 298.15 | 0.9053 | 0.0009 |
| 298.15 | 0.9522 | 0.0009 |
| 298.15 | 1.0000 | 0.0009 |
| 303.15 | 0.0000 | 0.0017 |
| 303.15 | 0.0487 | 0.0016 |
| 303.15 | 0.0993 | 0.0016 |
| 303.15 | 0.1967 | 0.0014 |
| 303.15 | 0.2993 | 0.0012 |
| 303.15 | 0.4017 | 0.0011 |
| 303.15 | 0.5071 | 0.0010 |
| 303.15 | 0.6048 | 0.0009 |
| 303.15 | 0.7036 | 0.0009 |
| 303.15 | 0.8062 | 0.0008 |
| 303.15 | 0.9053 | 0.0008 |
| 303.15 | 0.9522 | 0.0008 |
| 303.15 | 1.0000 | 0.0008 |
Viscosity, Pa*s [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0008 |
| 0.1021 | 0.0008 |
| 0.2112 | 0.0009 |
| 0.3122 | 0.0009 |
| 0.4211 | 0.0010 |
| 0.5151 | 0.0011 |
| 0.6203 | 0.0011 |
| 0.7208 | 0.0013 |
| 0.8143 | 0.0014 |
| 0.9079 | 0.0016 |
| 1.0000 | 0.0017 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 0.0503 | 0.0910 |
| 298.15 | 0.1005 | 0.1730 |
| 298.15 | 0.1499 | 0.2470 |
| 298.15 | 0.2005 | 0.3160 |
| 298.15 | 0.2499 | 0.3780 |
| 298.15 | 0.3005 | 0.4350 |
| 298.15 | 0.3503 | 0.4860 |
| 298.15 | 0.4003 | 0.5310 |
| 298.15 | 0.4501 | 0.5690 |
| 298.15 | 0.4998 | 0.5990 |
| 298.15 | 0.5504 | 0.6230 |
| 298.15 | 0.6006 | 0.6370 |
| 298.15 | 0.6503 | 0.6420 |
| 298.15 | 0.6995 | 0.6360 |
| 298.15 | 0.8005 | 0.5820 |
| 298.15 | 0.8497 | 0.5300 |
| 298.15 | 0.9005 | 0.4560 |
| 298.15 | 0.9502 | 0.3460 |
| 313.15 | 0.0503 | 0.1070 |
| 313.15 | 0.1005 | 0.2080 |
| 313.15 | 0.1499 | 0.3000 |
| 313.15 | 0.2005 | 0.3880 |
| 313.15 | 0.2498 | 0.4670 |
| 313.15 | 0.3004 | 0.5410 |
| 313.15 | 0.3502 | 0.6070 |
| 313.15 | 0.4001 | 0.6660 |
| 313.15 | 0.4500 | 0.7170 |
| 313.15 | 0.4997 | 0.7580 |
| 313.15 | 0.5502 | 0.7900 |
| 313.15 | 0.6006 | 0.8100 |
| 313.15 | 0.6503 | 0.8190 |
| 313.15 | 0.6994 | 0.8130 |
| 313.15 | 0.7503 | 0.7910 |
| 313.15 | 0.8005 | 0.7500 |
| 313.15 | 0.8497 | 0.6890 |
| 313.15 | 0.9005 | 0.5980 |
| 313.15 | 0.9502 | 0.4590 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 0.0503 | 0.0910 |
| 298.15 | 0.1005 | 0.1730 |
| 298.15 | 0.1499 | 0.2470 |
| 298.15 | 0.2005 | 0.3160 |
| 298.15 | 0.2499 | 0.3780 |
| 298.15 | 0.3005 | 0.4350 |
| 298.15 | 0.3503 | 0.4860 |
| 298.15 | 0.4003 | 0.5310 |
| 298.15 | 0.4501 | 0.5690 |
| 298.15 | 0.4998 | 0.5990 |
| 298.15 | 0.5504 | 0.6230 |
| 298.15 | 0.6006 | 0.6370 |
| 298.15 | 0.6503 | 0.6420 |
| 298.15 | 0.6995 | 0.6360 |
| 298.15 | 0.8005 | 0.5820 |
| 298.15 | 0.8497 | 0.5300 |
| 298.15 | 0.9005 | 0.4560 |
| 298.15 | 0.9502 | 0.3460 |
| 313.15 | 0.0503 | 0.1070 |
| 313.15 | 0.1005 | 0.2080 |
| 313.15 | 0.1499 | 0.3000 |
| 313.15 | 0.2005 | 0.3880 |
| 313.15 | 0.2498 | 0.4670 |
| 313.15 | 0.3004 | 0.5410 |
| 313.15 | 0.3502 | 0.6070 |
| 313.15 | 0.4001 | 0.6660 |
| 313.15 | 0.4500 | 0.7170 |
| 313.15 | 0.4997 | 0.7580 |
| 313.15 | 0.5502 | 0.7900 |
| 313.15 | 0.6006 | 0.8100 |
| 313.15 | 0.6503 | 0.8190 |
| 313.15 | 0.6994 | 0.8130 |
| 313.15 | 0.7503 | 0.7910 |
| 313.15 | 0.8005 | 0.7500 |
| 313.15 | 0.8497 | 0.6890 |
| 313.15 | 0.9005 | 0.5980 |
| 313.15 | 0.9502 | 0.4590 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Cyclohexane (2) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 0.3999 | 303.39 | 15.10 |
| 0.3999 | 308.56 | 18.50 |
| 0.3999 | 313.42 | 22.30 |
| 0.3999 | 318.12 | 26.70 |
| 0.3999 | 323.18 | 31.60 |
| 0.3999 | 328.27 | 38.40 |
| 0.3999 | 333.26 | 45.60 |
| 0.3999 | 338.24 | 54.00 |
| 0.3999 | 343.17 | 64.10 |
| 0.9000 | 303.56 | 17.90 |
| 0.9000 | 308.37 | 21.80 |
| 0.9000 | 313.29 | 26.20 |
| 0.9000 | 318.28 | 31.60 |
| 0.9000 | 323.07 | 37.60 |
| 0.9000 | 328.25 | 45.40 |
| 0.9000 | 333.17 | 54.00 |
| 0.9000 | 338.26 | 63.70 |
| 0.9000 | 343.19 | 75.60 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Cyclohexane (2) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 0.3999 | 303.39 | 15.10 |
| 0.3999 | 308.56 | 18.50 |
| 0.3999 | 313.42 | 22.30 |
| 0.3999 | 318.12 | 26.70 |
| 0.3999 | 323.18 | 31.60 |
| 0.3999 | 328.27 | 38.40 |
| 0.3999 | 333.26 | 45.60 |
| 0.3999 | 338.24 | 54.00 |
| 0.3999 | 343.17 | 64.10 |
| 0.9000 | 303.56 | 17.90 |
| 0.9000 | 308.37 | 21.80 |
| 0.9000 | 313.29 | 26.20 |
| 0.9000 | 318.28 | 31.60 |
| 0.9000 | 323.07 | 37.60 |
| 0.9000 | 328.25 | 45.40 |
| 0.9000 | 333.17 | 54.00 |
| 0.9000 | 338.26 | 63.70 |
| 0.9000 | 343.19 | 75.60 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 803.59 |
| 293.15 | 0.0487 | 801.17 |
| 293.15 | 0.0993 | 798.82 |
| 293.15 | 0.1967 | 794.76 |
| 293.15 | 0.2993 | 791.11 |
| 293.15 | 0.4017 | 787.98 |
| 293.15 | 0.5071 | 785.25 |
| 293.15 | 0.6048 | 783.08 |
| 293.15 | 0.7036 | 781.23 |
| 293.15 | 0.8062 | 779.66 |
| 293.15 | 0.9053 | 778.68 |
| 293.15 | 0.9522 | 778.41 |
| 293.15 | 1.0000 | 778.62 |
| 298.15 | 0.0000 | 799.58 |
| 298.15 | 0.0487 | 797.11 |
| 298.15 | 0.0993 | 794.71 |
| 298.15 | 0.1967 | 790.54 |
| 298.15 | 0.2993 | 786.78 |
| 298.15 | 0.4017 | 783.54 |
| 298.15 | 0.5071 | 780.71 |
| 298.15 | 0.6048 | 778.47 |
| 298.15 | 0.7036 | 776.55 |
| 298.15 | 0.8062 | 774.94 |
| 298.15 | 0.9053 | 773.93 |
| 298.15 | 0.9522 | 773.66 |
| 298.15 | 1.0000 | 773.92 |
| 303.15 | 0.0000 | 795.55 |
| 303.15 | 0.0487 | 793.02 |
| 303.15 | 0.0993 | 790.56 |
| 303.15 | 0.1967 | 786.28 |
| 303.15 | 0.2993 | 782.41 |
| 303.15 | 0.4017 | 779.05 |
| 303.15 | 0.5071 | 776.12 |
| 303.15 | 0.6048 | 773.8 |
| 303.15 | 0.7036 | 771.82 |
| 303.15 | 0.8062 | 770.17 |
| 303.15 | 0.9053 | 769.14 |
| 303.15 | 0.9522 | 768.87 |
| 303.15 | 1.0000 | 769.19 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 769.16 |
| 0.1021 | 769.52 |
| 0.2112 | 770.68 |
| 0.3122 | 772.37 |
| 0.4211 | 774.63 |
| 0.5151 | 776.9 |
| 0.6203 | 779.94 |
| 0.7208 | 783.15 |
| 0.8143 | 786.73 |
| 0.9079 | 790.83 |
| 1.0000 | 795.66 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 803.59 |
| 293.15 | 0.0487 | 801.17 |
| 293.15 | 0.0993 | 798.82 |
| 293.15 | 0.1967 | 794.76 |
| 293.15 | 0.2993 | 791.11 |
| 293.15 | 0.4017 | 787.98 |
| 293.15 | 0.5071 | 785.25 |
| 293.15 | 0.6048 | 783.08 |
| 293.15 | 0.7036 | 781.23 |
| 293.15 | 0.8062 | 779.66 |
| 293.15 | 0.9053 | 778.68 |
| 293.15 | 0.9522 | 778.41 |
| 293.15 | 1.0000 | 778.62 |
| 298.15 | 0.0000 | 799.58 |
| 298.15 | 0.0487 | 797.11 |
| 298.15 | 0.0993 | 794.71 |
| 298.15 | 0.1967 | 790.54 |
| 298.15 | 0.2993 | 786.78 |
| 298.15 | 0.4017 | 783.54 |
| 298.15 | 0.5071 | 780.71 |
| 298.15 | 0.6048 | 778.47 |
| 298.15 | 0.7036 | 776.55 |
| 298.15 | 0.8062 | 774.94 |
| 298.15 | 0.9053 | 773.93 |
| 298.15 | 0.9522 | 773.66 |
| 298.15 | 1.0000 | 773.92 |
| 303.15 | 0.0000 | 795.55 |
| 303.15 | 0.0487 | 793.02 |
| 303.15 | 0.0993 | 790.56 |
| 303.15 | 0.1967 | 786.28 |
| 303.15 | 0.2993 | 782.41 |
| 303.15 | 0.4017 | 779.05 |
| 303.15 | 0.5071 | 776.12 |
| 303.15 | 0.6048 | 773.8 |
| 303.15 | 0.7036 | 771.82 |
| 303.15 | 0.8062 | 770.17 |
| 303.15 | 0.9053 | 769.14 |
| 303.15 | 0.9522 | 768.87 |
| 303.15 | 1.0000 | 769.19 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 769.16 |
| 0.1021 | 769.52 |
| 0.2112 | 770.68 |
| 0.3122 | 772.37 |
| 0.4211 | 774.63 |
| 0.5151 | 776.9 |
| 0.6203 | 779.94 |
| 0.7208 | 783.15 |
| 0.8143 | 786.73 |
| 0.9079 | 790.83 |
| 1.0000 | 795.66 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0000 | 1223.0 |
| 293.15 | 0.0487 | 1222.0 |
| 293.15 | 0.0993 | 1222.0 |
| 293.15 | 0.1967 | 1223.0 |
| 293.15 | 0.2993 | 1225.0 |
| 293.15 | 0.4017 | 1228.0 |
| 293.15 | 0.5071 | 1233.0 |
| 293.15 | 0.6048 | 1238.0 |
| 293.15 | 0.7036 | 1244.0 |
| 293.15 | 0.8062 | 1252.0 |
| 293.15 | 0.9053 | 1262.0 |
| 293.15 | 0.9522 | 1268.0 |
| 293.15 | 1.0000 | 1279.0 |
| 298.15 | 0.0000 | 1206.0 |
| 298.15 | 0.0487 | 1205.0 |
| 298.15 | 0.0993 | 1204.0 |
| 298.15 | 0.1967 | 1204.0 |
| 298.15 | 0.2993 | 1205.0 |
| 298.15 | 0.4017 | 1207.0 |
| 298.15 | 0.5071 | 1211.0 |
| 298.15 | 0.6048 | 1215.0 |
| 298.15 | 0.7036 | 1221.0 |
| 298.15 | 0.8062 | 1228.0 |
| 298.15 | 0.9053 | 1237.0 |
| 298.15 | 0.9522 | 1243.0 |
| 298.15 | 1.0000 | 1254.0 |
| 303.15 | 0.0000 | 1189.0 |
| 303.15 | 0.0487 | 1187.0 |
| 303.15 | 0.0993 | 1186.0 |
| 303.15 | 0.1967 | 1185.0 |
| 303.15 | 0.2993 | 1185.0 |
| 303.15 | 0.4017 | 1186.0 |
| 303.15 | 0.5071 | 1189.0 |
| 303.15 | 0.6048 | 1193.0 |
| 303.15 | 0.7036 | 1198.0 |
| 303.15 | 0.8062 | 1204.0 |
| 303.15 | 0.9053 | 1213.0 |
| 303.15 | 0.9522 | 1219.0 |
| 303.15 | 1.0000 | 1230.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0000 | 1223.0 |
| 293.15 | 0.0487 | 1222.0 |
| 293.15 | 0.0993 | 1222.0 |
| 293.15 | 0.1967 | 1223.0 |
| 293.15 | 0.2993 | 1225.0 |
| 293.15 | 0.4017 | 1228.0 |
| 293.15 | 0.5071 | 1233.0 |
| 293.15 | 0.6048 | 1238.0 |
| 293.15 | 0.7036 | 1244.0 |
| 293.15 | 0.8062 | 1252.0 |
| 293.15 | 0.9053 | 1262.0 |
| 293.15 | 0.9522 | 1268.0 |
| 293.15 | 1.0000 | 1279.0 |
| 298.15 | 0.0000 | 1206.0 |
| 298.15 | 0.0487 | 1205.0 |
| 298.15 | 0.0993 | 1204.0 |
| 298.15 | 0.1967 | 1204.0 |
| 298.15 | 0.2993 | 1205.0 |
| 298.15 | 0.4017 | 1207.0 |
| 298.15 | 0.5071 | 1211.0 |
| 298.15 | 0.6048 | 1215.0 |
| 298.15 | 0.7036 | 1221.0 |
| 298.15 | 0.8062 | 1228.0 |
| 298.15 | 0.9053 | 1237.0 |
| 298.15 | 0.9522 | 1243.0 |
| 298.15 | 1.0000 | 1254.0 |
| 303.15 | 0.0000 | 1189.0 |
| 303.15 | 0.0487 | 1187.0 |
| 303.15 | 0.0993 | 1186.0 |
| 303.15 | 0.1967 | 1185.0 |
| 303.15 | 0.2993 | 1185.0 |
| 303.15 | 0.4017 | 1186.0 |
| 303.15 | 0.5071 | 1189.0 |
| 303.15 | 0.6048 | 1193.0 |
| 303.15 | 0.7036 | 1198.0 |
| 303.15 | 0.8062 | 1204.0 |
| 303.15 | 0.9053 | 1213.0 |
| 303.15 | 0.9522 | 1219.0 |
| 303.15 | 1.0000 | 1230.0 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0300 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9700 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0300 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9700 | 0.0000 |
Sources
- Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
- Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
- Excess enthalpies of ternary mixtures of (oxygenated additives + cycloalkane) in fuels and bio-fuels: (dibutyl ether + 1-propanol + cyclohexane), or methylcyclohexane, at T = (298.15 and 313.15) K
- Volumetric and transport properties of ternary mixtures containing 1-propanol, triethylamine or tri-n-butylamine and cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems