- Name
- Ethanol
- InChI
- InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
- InChI Key
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N
- Formula
- C2H6O
- SMILES
- CCO
- Mol. Weight (g/mol)
- 46.07
- CAS
- 64-17-5
- Name
- 1-Butanol, 3-methyl-, acetate
- InChI
- InChI=1S/C7H14O2/c1-6(2)4-5-9-7(3)8/h6H,4-5H2,1-3H3
- InChI Key
- MLFHJEHSLIIPHL-UHFFFAOYSA-N
- Formula
- C7H14O2
- SMILES
- CC(=O)OCCC(C)C
- Mol. Weight (g/mol)
- 130.18
- CAS
- 123-92-2
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
- n0 - Refractive index (Na D-line)
- ρl - Mass density, kg/m3 (2)
- γ - Surface tension liquid-gas, N/m
- Excess molar volume, m3/mol
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 100.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0013 |
| 288.15 | 0.0500 | 0.0012 |
| 288.15 | 0.1000 | 0.0011 |
| 288.15 | 0.1500 | 0.0011 |
| 288.15 | 0.2000 | 0.0010 |
| 288.15 | 0.2500 | 0.0010 |
| 288.15 | 0.3000 | 0.0010 |
| 288.15 | 0.3500 | 0.0009 |
| 288.15 | 0.4000 | 0.0009 |
| 288.15 | 0.4500 | 0.0009 |
| 288.15 | 0.5000 | 0.0009 |
| 288.15 | 0.5500 | 0.0009 |
| 288.15 | 0.6000 | 0.0009 |
| 288.15 | 0.6500 | 0.0009 |
| 288.15 | 0.7000 | 0.0009 |
| 288.15 | 0.7500 | 0.0009 |
| 288.15 | 0.8000 | 0.0009 |
| 288.15 | 0.8500 | 0.0009 |
| 288.15 | 0.9000 | 0.0009 |
| 288.15 | 0.9500 | 0.0009 |
| 288.15 | 1.0000 | 0.0009 |
| 298.15 | 0.0000 | 0.0011 |
| 298.15 | 0.0500 | 0.0010 |
| 298.15 | 0.1000 | 0.0009 |
| 298.15 | 0.1500 | 0.0009 |
| 298.15 | 0.2000 | 0.0009 |
| 298.15 | 0.2500 | 0.0008 |
| 298.15 | 0.3000 | 0.0008 |
| 298.15 | 0.3500 | 0.0008 |
| 298.15 | 0.4000 | 0.0008 |
| 298.15 | 0.4500 | 0.0008 |
| 298.15 | 0.5000 | 0.0008 |
| 298.15 | 0.5500 | 0.0008 |
| 298.15 | 0.6000 | 0.0008 |
| 298.15 | 0.6500 | 0.0008 |
| 298.15 | 0.7000 | 0.0008 |
| 298.15 | 0.7500 | 0.0008 |
| 298.15 | 0.8000 | 0.0008 |
| 298.15 | 0.8500 | 0.0008 |
| 298.15 | 0.9000 | 0.0008 |
| 298.15 | 0.9500 | 0.0008 |
| 298.15 | 1.0000 | 0.0008 |
| 308.15 | 0.0000 | 0.0009 |
| 308.15 | 0.0500 | 0.0008 |
| 308.15 | 0.1000 | 0.0008 |
| 308.15 | 0.1500 | 0.0008 |
| 308.15 | 0.2000 | 0.0007 |
| 308.15 | 0.2500 | 0.0007 |
| 308.15 | 0.3000 | 0.0007 |
| 308.15 | 0.3500 | 0.0007 |
| 308.15 | 0.4000 | 0.0007 |
| 308.15 | 0.4500 | 0.0007 |
| 308.15 | 0.5000 | 0.0007 |
| 308.15 | 0.5500 | 0.0007 |
| 308.15 | 0.6000 | 0.0007 |
| 308.15 | 0.6500 | 0.0007 |
| 308.15 | 0.7000 | 0.0007 |
| 308.15 | 0.7500 | 0.0007 |
| 308.15 | 0.8000 | 0.0007 |
| 308.15 | 0.8500 | 0.0007 |
| 308.15 | 0.9000 | 0.0007 |
| 308.15 | 0.9500 | 0.0007 |
| 308.15 | 1.0000 | 0.0007 |
| 318.15 | 0.0000 | 0.0008 |
| 318.15 | 0.0500 | 0.0007 |
| 318.15 | 0.1000 | 0.0007 |
| 318.15 | 0.1500 | 0.0007 |
| 318.15 | 0.2000 | 0.0006 |
| 318.15 | 0.2500 | 0.0006 |
| 318.15 | 0.3000 | 0.0006 |
| 318.15 | 0.3500 | 0.0006 |
| 318.15 | 0.4000 | 0.0006 |
| 318.15 | 0.4500 | 0.0006 |
| 318.15 | 0.5000 | 0.0006 |
| 318.15 | 0.5500 | 0.0006 |
| 318.15 | 0.6000 | 0.0006 |
| 318.15 | 0.6500 | 0.0006 |
| 318.15 | 0.7000 | 0.0006 |
| 318.15 | 0.7500 | 0.0006 |
| 318.15 | 0.8000 | 0.0006 |
| 318.15 | 0.8500 | 0.0006 |
| 318.15 | 0.9000 | 0.0006 |
| 318.15 | 0.9500 | 0.0006 |
| 318.15 | 1.0000 | 0.0006 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 100.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.3633 |
| 288.15 | 0.0500 | 1.368 |
| 288.15 | 0.1000 | 1.3721 |
| 288.15 | 0.1500 | 1.3756 |
| 288.15 | 0.2000 | 1.3787 |
| 288.15 | 0.2500 | 1.3815 |
| 288.15 | 0.3000 | 1.3839 |
| 288.15 | 0.3500 | 1.3861 |
| 288.15 | 0.4000 | 1.3881 |
| 288.15 | 0.4500 | 1.39 |
| 288.15 | 0.5000 | 1.3916 |
| 288.15 | 0.5500 | 1.3932 |
| 288.15 | 0.6000 | 1.3946 |
| 288.15 | 0.6500 | 1.396 |
| 288.15 | 0.7000 | 1.3972 |
| 288.15 | 0.7500 | 1.3983 |
| 288.15 | 0.8000 | 1.3993 |
| 288.15 | 0.8500 | 1.4003 |
| 288.15 | 0.9000 | 1.4012 |
| 288.15 | 0.9500 | 1.4021 |
| 288.15 | 1.0000 | 1.4029 |
| 298.15 | 0.0000 | 1.3594 |
| 298.15 | 0.0500 | 1.3639 |
| 298.15 | 0.1000 | 1.3679 |
| 298.15 | 0.1500 | 1.3713 |
| 298.15 | 0.2000 | 1.3744 |
| 298.15 | 0.2500 | 1.3771 |
| 298.15 | 0.3000 | 1.3795 |
| 298.15 | 0.3500 | 1.3817 |
| 298.15 | 0.4000 | 1.3837 |
| 298.15 | 0.4500 | 1.3855 |
| 298.15 | 0.5000 | 1.3872 |
| 298.15 | 0.5500 | 1.3887 |
| 298.15 | 0.6000 | 1.3901 |
| 298.15 | 0.6500 | 1.3914 |
| 298.15 | 0.7000 | 1.3926 |
| 298.15 | 0.7500 | 1.3938 |
| 298.15 | 0.8000 | 1.3948 |
| 298.15 | 0.8500 | 1.3958 |
| 298.15 | 0.9000 | 1.3967 |
| 298.15 | 0.9500 | 1.3976 |
| 298.15 | 1.0000 | 1.3984 |
| 308.15 | 0.0000 | 1.3553 |
| 308.15 | 0.0500 | 1.3596 |
| 308.15 | 0.1000 | 1.3635 |
| 308.15 | 0.1500 | 1.3669 |
| 308.15 | 0.2000 | 1.3699 |
| 308.15 | 0.2500 | 1.3726 |
| 308.15 | 0.3000 | 1.375 |
| 308.15 | 0.3500 | 1.3771 |
| 308.15 | 0.4000 | 1.3791 |
| 308.15 | 0.4500 | 1.3809 |
| 308.15 | 0.5000 | 1.3825 |
| 308.15 | 0.5500 | 1.384 |
| 308.15 | 0.6000 | 1.3855 |
| 308.15 | 0.6500 | 1.3867 |
| 308.15 | 0.7000 | 1.388 |
| 308.15 | 0.7500 | 1.3891 |
| 308.15 | 0.8000 | 1.3901 |
| 308.15 | 0.8500 | 1.3911 |
| 308.15 | 0.9000 | 1.392 |
| 308.15 | 0.9500 | 1.3928 |
| 308.15 | 1.0000 | 1.3937 |
| 318.15 | 0.0000 | 1.3515 |
| 318.15 | 0.0500 | 1.3556 |
| 318.15 | 0.1000 | 1.3593 |
| 318.15 | 0.1500 | 1.3626 |
| 318.15 | 0.2000 | 1.3656 |
| 318.15 | 0.2500 | 1.3682 |
| 318.15 | 0.3000 | 1.3706 |
| 318.15 | 0.3500 | 1.3727 |
| 318.15 | 0.4000 | 1.3746 |
| 318.15 | 0.4500 | 1.3763 |
| 318.15 | 0.5000 | 1.378 |
| 318.15 | 0.5500 | 1.3794 |
| 318.15 | 0.6000 | 1.3808 |
| 318.15 | 0.6500 | 1.3821 |
| 318.15 | 0.7000 | 1.3833 |
| 318.15 | 0.7500 | 1.3844 |
| 318.15 | 0.8000 | 1.3854 |
| 318.15 | 0.8500 | 1.3864 |
| 318.15 | 0.9000 | 1.3873 |
| 318.15 | 0.9500 | 1.3881 |
| 318.15 | 1.0000 | 1.3889 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0741 | 803.2 |
| 293.15 | 0.1483 | 814.43 |
| 293.15 | 0.2224 | 823.82 |
| 293.15 | 0.2976 | 831.78 |
| 293.15 | 0.3766 | 839.04 |
| 293.15 | 0.4562 | 845.29 |
| 293.15 | 0.5240 | 849.98 |
| 293.15 | 0.6178 | 855.66 |
| 293.15 | 0.7017 | 860.12 |
| 293.15 | 0.7774 | 863.76 |
| 293.15 | 0.8732 | 867.92 |
| 293.15 | 0.9568 | 871.25 |
| 303.15 | 0.0741 | 794.28 |
| 303.15 | 0.1483 | 805.27 |
| 303.15 | 0.2224 | 814.48 |
| 303.15 | 0.2976 | 822.3 |
| 303.15 | 0.3766 | 829.45 |
| 303.15 | 0.4562 | 835.6 |
| 303.15 | 0.5240 | 840.23 |
| 303.15 | 0.6178 | 845.86 |
| 303.15 | 0.7017 | 850.27 |
| 303.15 | 0.7774 | 853.91 |
| 303.15 | 0.8732 | 858.09 |
| 303.15 | 0.9568 | 861.45 |
| 313.15 | 0.0741 | 785.22 |
| 313.15 | 0.1483 | 795.97 |
| 313.15 | 0.2224 | 804.99 |
| 313.15 | 0.2976 | 812.67 |
| 313.15 | 0.3766 | 819.71 |
| 313.15 | 0.4562 | 825.78 |
| 313.15 | 0.5240 | 830.36 |
| 313.15 | 0.6178 | 835.94 |
| 313.15 | 0.7017 | 840.36 |
| 313.15 | 0.7774 | 843.98 |
| 313.15 | 0.8732 | 848.19 |
| 313.15 | 0.9568 | 851.58 |
| 323.15 | 0.0741 | 775.98 |
| 323.15 | 0.1483 | 786.48 |
| 323.15 | 0.2224 | 795.33 |
| 323.15 | 0.2976 | 802.86 |
| 323.15 | 0.3766 | 809.8 |
| 323.15 | 0.4562 | 815.79 |
| 323.15 | 0.5240 | 820.34 |
| 323.15 | 0.6178 | 825.88 |
| 323.15 | 0.7017 | 830.3 |
| 323.15 | 0.7774 | 833.94 |
| 323.15 | 0.8732 | 838.18 |
| 323.15 | 0.9568 | 841.64 |
| 333.15 | 0.0741 | 766.5 |
| 333.15 | 0.1483 | 776.77 |
| 333.15 | 0.2224 | 785.43 |
| 333.15 | 0.2976 | 792.85 |
| 333.15 | 0.3766 | 799.69 |
| 333.15 | 0.4562 | 805.62 |
| 333.15 | 0.5240 | 810.13 |
| 333.15 | 0.6178 | 815.71 |
| 333.15 | 0.7017 | 820.1 |
| 333.15 | 0.7774 | 823.77 |
| 333.15 | 0.8732 | 828.07 |
| 333.15 | 0.9568 | 831.6 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 793.6 |
| 288.15 | 0.0500 | 803.41 |
| 288.15 | 0.1000 | 811.89 |
| 288.15 | 0.1500 | 819.25 |
| 288.15 | 0.2000 | 825.81 |
| 288.15 | 0.2500 | 831.66 |
| 288.15 | 0.3000 | 836.85 |
| 288.15 | 0.3500 | 841.58 |
| 288.15 | 0.4000 | 845.81 |
| 288.15 | 0.4500 | 849.7 |
| 288.15 | 0.5000 | 853.26 |
| 288.15 | 0.5500 | 856.53 |
| 288.15 | 0.6000 | 859.57 |
| 288.15 | 0.6500 | 862.36 |
| 288.15 | 0.7000 | 865.0 |
| 288.15 | 0.7500 | 867.44 |
| 288.15 | 0.8000 | 869.73 |
| 288.15 | 0.8500 | 871.89 |
| 288.15 | 0.9000 | 873.95 |
| 288.15 | 0.9500 | 875.87 |
| 288.15 | 1.0000 | 877.72 |
| 298.15 | 0.0000 | 785.0 |
| 298.15 | 0.0500 | 794.64 |
| 298.15 | 0.1000 | 802.92 |
| 298.15 | 0.1500 | 810.13 |
| 298.15 | 0.2000 | 816.58 |
| 298.15 | 0.2500 | 822.31 |
| 298.15 | 0.3000 | 827.42 |
| 298.15 | 0.3500 | 832.08 |
| 298.15 | 0.4000 | 836.24 |
| 298.15 | 0.4500 | 840.07 |
| 298.15 | 0.5000 | 843.59 |
| 298.15 | 0.5500 | 846.82 |
| 298.15 | 0.6000 | 849.83 |
| 298.15 | 0.6500 | 852.58 |
| 298.15 | 0.7000 | 855.21 |
| 298.15 | 0.7500 | 857.64 |
| 298.15 | 0.8000 | 859.93 |
| 298.15 | 0.8500 | 862.08 |
| 298.15 | 0.9000 | 864.14 |
| 298.15 | 0.9500 | 866.09 |
| 298.15 | 1.0000 | 867.91 |
| 308.15 | 0.0000 | 776.31 |
| 308.15 | 0.0500 | 785.74 |
| 308.15 | 0.1000 | 793.84 |
| 308.15 | 0.1500 | 800.9 |
| 308.15 | 0.2000 | 807.21 |
| 308.15 | 0.2500 | 812.85 |
| 308.15 | 0.3000 | 817.86 |
| 308.15 | 0.3500 | 822.44 |
| 308.15 | 0.4000 | 826.53 |
| 308.15 | 0.4500 | 830.32 |
| 308.15 | 0.5000 | 833.79 |
| 308.15 | 0.5500 | 836.99 |
| 308.15 | 0.6000 | 839.97 |
| 308.15 | 0.6500 | 842.71 |
| 308.15 | 0.7000 | 845.33 |
| 308.15 | 0.7500 | 847.75 |
| 308.15 | 0.8000 | 850.04 |
| 308.15 | 0.8500 | 852.2 |
| 308.15 | 0.9000 | 854.28 |
| 308.15 | 0.9500 | 856.25 |
| 308.15 | 1.0000 | 858.07 |
| 318.15 | 0.0000 | 767.44 |
| 318.15 | 0.0500 | 776.69 |
| 318.15 | 0.1000 | 784.6 |
| 318.15 | 0.1500 | 791.5 |
| 318.15 | 0.2000 | 797.69 |
| 318.15 | 0.2500 | 803.22 |
| 318.15 | 0.3000 | 808.15 |
| 318.15 | 0.3500 | 812.65 |
| 318.15 | 0.4000 | 816.69 |
| 318.15 | 0.4500 | 820.42 |
| 318.15 | 0.5000 | 823.86 |
| 318.15 | 0.5500 | 827.03 |
| 318.15 | 0.6000 | 829.99 |
| 318.15 | 0.6500 | 832.72 |
| 318.15 | 0.7000 | 835.33 |
| 318.15 | 0.7500 | 837.75 |
| 318.15 | 0.8000 | 840.05 |
| 318.15 | 0.8500 | 842.22 |
| 318.15 | 0.9000 | 844.34 |
| 318.15 | 0.9500 | 846.32 |
| 318.15 | 1.0000 | 848.17 |
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 288.15 | 0.0000 | 0.0230 |
| 288.15 | 0.0500 | 0.0232 |
| 288.15 | 0.1000 | 0.0234 |
| 288.15 | 0.1500 | 0.0236 |
| 288.15 | 0.2000 | 0.0237 |
| 288.15 | 0.2500 | 0.0238 |
| 288.15 | 0.3000 | 0.0240 |
| 288.15 | 0.3500 | 0.0241 |
| 288.15 | 0.4000 | 0.0242 |
| 288.15 | 0.4500 | 0.0243 |
| 288.15 | 0.5000 | 0.0244 |
| 288.15 | 0.5500 | 0.0245 |
| 288.15 | 0.6000 | 0.0246 |
| 288.15 | 0.6500 | 0.0247 |
| 288.15 | 0.7000 | 0.0248 |
| 288.15 | 0.7500 | 0.0249 |
| 288.15 | 0.8000 | 0.0250 |
| 288.15 | 0.8500 | 0.0251 |
| 288.15 | 0.9000 | 0.0252 |
| 288.15 | 0.9500 | 0.0253 |
| 288.15 | 1.0000 | 0.0254 |
| 298.15 | 0.0000 | 0.0223 |
| 298.15 | 0.0500 | 0.0224 |
| 298.15 | 0.1000 | 0.0225 |
| 298.15 | 0.1500 | 0.0227 |
| 298.15 | 0.2000 | 0.0228 |
| 298.15 | 0.2500 | 0.0229 |
| 298.15 | 0.3500 | 0.0230 |
| 298.15 | 0.4000 | 0.0231 |
| 298.15 | 0.4500 | 0.0232 |
| 298.15 | 0.5000 | 0.0233 |
| 298.15 | 0.5500 | 0.0234 |
| 298.15 | 0.6000 | 0.0235 |
| 298.15 | 0.6500 | 0.0236 |
| 298.15 | 0.7000 | 0.0237 |
| 298.15 | 0.7500 | 0.0238 |
| 298.15 | 0.8000 | 0.0239 |
| 298.15 | 0.8500 | 0.0240 |
| 298.15 | 0.9000 | 0.0241 |
| 298.15 | 0.9500 | 0.0242 |
| 298.15 | 1.0000 | 0.0243 |
| 308.15 | 0.0000 | 0.0215 |
| 308.15 | 0.0500 | 0.0216 |
| 308.15 | 0.1000 | 0.0216 |
| 308.15 | 0.1500 | 0.0217 |
| 308.15 | 0.2000 | 0.0218 |
| 308.15 | 0.2500 | 0.0219 |
| 308.15 | 0.3000 | 0.0220 |
| 308.15 | 0.3500 | 0.0221 |
| 308.15 | 0.4000 | 0.0222 |
| 308.15 | 0.4500 | 0.0223 |
| 308.15 | 0.5000 | 0.0224 |
| 308.15 | 0.5500 | 0.0225 |
| 308.15 | 0.6000 | 0.0226 |
| 308.15 | 0.6500 | 0.0227 |
| 308.15 | 0.7000 | 0.0228 |
| 308.15 | 0.7500 | 0.0229 |
| 308.15 | 0.8000 | 0.0230 |
| 308.15 | 0.8500 | 0.0231 |
| 308.15 | 0.9000 | 0.0232 |
| 308.15 | 0.9500 | 0.0233 |
| 308.15 | 1.0000 | 0.0234 |
| 318.15 | 0.0000 | 0.0206 |
| 318.15 | 0.0500 | 0.0206 |
| 318.15 | 0.1000 | 0.0206 |
| 318.15 | 0.1500 | 0.0207 |
| 318.15 | 0.2000 | 0.0208 |
| 318.15 | 0.2500 | 0.0209 |
| 318.15 | 0.3000 | 0.0210 |
| 318.15 | 0.3500 | 0.0211 |
| 318.15 | 0.4000 | 0.0212 |
| 318.15 | 0.4500 | 0.0213 |
| 318.15 | 0.5000 | 0.0214 |
| 318.15 | 0.5500 | 0.0215 |
| 318.15 | 0.6000 | 0.0216 |
| 318.15 | 0.6500 | 0.0217 |
| 318.15 | 0.7000 | 0.0218 |
| 318.15 | 0.7500 | 0.0219 |
| 318.15 | 0.8000 | 0.0220 |
| 318.15 | 0.8500 | 0.0221 |
| 318.15 | 0.9000 | 0.0222 |
| 318.15 | 0.9500 | 0.0223 |
| 318.15 | 1.0000 | 0.0224 |
Excess molar volume, m3/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid | Excess molar volume, m3/mol - Liquid |
| 293.15 | 0.0741 | 3.8000e-08 |
| 293.15 | 0.1483 | 6.7000e-08 |
| 293.15 | 0.2224 | 8.6000e-08 |
| 293.15 | 0.2976 | 1.1100e-07 |
| 293.15 | 0.3766 | 1.1900e-07 |
| 293.15 | 0.4562 | 1.2900e-07 |
| 293.15 | 0.5240 | 1.3200e-07 |
| 293.15 | 0.6178 | 1.3300e-07 |
| 293.15 | 0.7017 | 1.2700e-07 |
| 293.15 | 0.7774 | 1.1100e-07 |
| 293.15 | 0.8732 | 8.0000e-08 |
| 293.15 | 0.9568 | 3.5000e-08 |
| 303.15 | 0.0741 | 4.8000e-08 |
| 303.15 | 0.1483 | 8.6000e-08 |
| 303.15 | 0.2224 | 1.1200e-07 |
| 303.15 | 0.2976 | 1.4200e-07 |
| 303.15 | 0.3766 | 1.5300e-07 |
| 303.15 | 0.4562 | 1.6600e-07 |
| 303.15 | 0.5240 | 1.7100e-07 |
| 303.15 | 0.6178 | 1.7100e-07 |
| 303.15 | 0.7017 | 1.6500e-07 |
| 303.15 | 0.7774 | 1.4300e-07 |
| 303.15 | 0.8732 | 1.0100e-07 |
| 303.15 | 0.9568 | 4.3000e-08 |
| 313.15 | 0.0741 | 6.1000e-08 |
| 313.15 | 0.1483 | 1.0900e-07 |
| 313.15 | 0.2224 | 1.4400e-07 |
| 313.15 | 0.2976 | 1.8100e-07 |
| 313.15 | 0.3766 | 1.9600e-07 |
| 313.15 | 0.4562 | 2.1200e-07 |
| 313.15 | 0.5240 | 2.1700e-07 |
| 313.15 | 0.6178 | 2.1700e-07 |
| 313.15 | 0.7017 | 2.0300e-07 |
| 313.15 | 0.7774 | 1.7800e-07 |
| 313.15 | 0.8732 | 1.2300e-07 |
| 313.15 | 0.9568 | 5.3000e-08 |
| 323.15 | 0.0741 | 7.7000e-08 |
| 323.15 | 0.1483 | 1.3700e-07 |
| 323.15 | 0.2224 | 1.8100e-07 |
| 323.15 | 0.2976 | 2.2600e-07 |
| 323.15 | 0.3766 | 2.4700e-07 |
| 323.15 | 0.4562 | 2.6700e-07 |
| 323.15 | 0.5240 | 2.7100e-07 |
| 323.15 | 0.6178 | 2.7000e-07 |
| 323.15 | 0.7017 | 2.5100e-07 |
| 323.15 | 0.7774 | 2.1800e-07 |
| 323.15 | 0.8732 | 1.5000e-07 |
| 323.15 | 0.9568 | 6.1000e-08 |
| 333.15 | 0.0741 | 9.5000e-08 |
| 333.15 | 0.1483 | 1.7000e-07 |
| 333.15 | 0.2224 | 2.2600e-07 |
| 333.15 | 0.2976 | 2.7900e-07 |
| 333.15 | 0.3766 | 3.0700e-07 |
| 333.15 | 0.4562 | 3.3000e-07 |
| 333.15 | 0.5240 | 3.3700e-07 |
| 333.15 | 0.6178 | 3.2600e-07 |
| 333.15 | 0.7017 | 3.0700e-07 |
| 333.15 | 0.7774 | 2.6500e-07 |
| 333.15 | 0.8732 | 1.8100e-07 |
| 333.15 | 0.9568 | 7.2000e-08 |
Sources
- Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
- Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
- Refractive Indices and Surface Tensions of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
Note: These property values are available through the Cheméo API. A free account gives you an access key.