- Name
- Formamide, N,N-dimethyl-
- InChI
- InChI=1S/C3H7NO/c1-4(2)3-5/h3H,1-2H3
- InChI Key
- ZMXDDKWLCZADIW-UHFFFAOYSA-N
- Formula
- C3H7NO
- SMILES
- CN(C)C=O
- Mol. Weight (g/mol)
- 73.09
- CAS
- 68-12-2
- 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
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Datasets
- η - Viscosity, Pa*s (2)
- ρl - Mass density, kg/m3 (2)
- Tboil - Boiling temperature at pressure P, K (2)
- Excess molar volume, m3/mol (2)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0009 |
| 293.15 | 0.0999 | 0.0009 |
| 293.15 | 0.2000 | 0.0009 |
| 293.15 | 0.3000 | 0.0009 |
| 293.15 | 0.4000 | 0.0009 |
| 293.15 | 0.5001 | 0.0009 |
| 293.15 | 0.6000 | 0.0009 |
| 293.15 | 0.7000 | 0.0009 |
| 293.15 | 0.8000 | 0.0010 |
| 293.15 | 0.9001 | 0.0011 |
| 293.15 | 1.0000 | 0.0012 |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.0999 | 0.0008 |
| 298.15 | 0.2000 | 0.0008 |
| 298.15 | 0.3000 | 0.0008 |
| 298.15 | 0.4000 | 0.0008 |
| 298.15 | 0.5001 | 0.0008 |
| 298.15 | 0.6000 | 0.0008 |
| 298.15 | 0.7000 | 0.0009 |
| 298.15 | 0.8000 | 0.0009 |
| 298.15 | 0.9001 | 0.0010 |
| 298.15 | 1.0000 | 0.0011 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.0999 | 0.0008 |
| 303.15 | 0.2000 | 0.0008 |
| 303.15 | 0.3000 | 0.0008 |
| 303.15 | 0.4000 | 0.0008 |
| 303.15 | 0.5001 | 0.0008 |
| 303.15 | 0.6000 | 0.0008 |
| 303.15 | 0.7000 | 0.0008 |
| 303.15 | 0.8000 | 0.0008 |
| 303.15 | 0.9001 | 0.0009 |
| 303.15 | 1.0000 | 0.0010 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.0999 | 0.0007 |
| 313.15 | 0.2000 | 0.0007 |
| 313.15 | 0.3000 | 0.0007 |
| 313.15 | 0.4000 | 0.0007 |
| 313.15 | 0.5001 | 0.0007 |
| 313.15 | 0.6000 | 0.0007 |
| 313.15 | 0.7000 | 0.0007 |
| 313.15 | 0.8000 | 0.0007 |
| 313.15 | 0.9001 | 0.0008 |
| 313.15 | 1.0000 | 0.0008 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.0999 | 0.0006 |
| 323.15 | 0.2000 | 0.0006 |
| 323.15 | 0.3000 | 0.0006 |
| 323.15 | 0.4000 | 0.0006 |
| 323.15 | 0.5001 | 0.0006 |
| 323.15 | 0.6000 | 0.0006 |
| 323.15 | 0.7000 | 0.0006 |
| 323.15 | 0.8000 | 0.0006 |
| 323.15 | 0.9001 | 0.0007 |
| 323.15 | 1.0000 | 0.0007 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.0999 | 0.0005 |
| 333.15 | 0.2000 | 0.0005 |
| 333.15 | 0.3000 | 0.0005 |
| 333.15 | 0.4000 | 0.0005 |
| 333.15 | 0.5001 | 0.0005 |
| 333.15 | 0.6000 | 0.0005 |
| 333.15 | 0.7000 | 0.0005 |
| 333.15 | 0.8000 | 0.0005 |
| 333.15 | 0.9001 | 0.0006 |
| 333.15 | 1.0000 | 0.0006 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0009 |
| 293.15 | 0.0999 | 0.0009 |
| 293.15 | 0.2000 | 0.0009 |
| 293.15 | 0.3000 | 0.0009 |
| 293.15 | 0.4000 | 0.0009 |
| 293.15 | 0.5001 | 0.0009 |
| 293.15 | 0.6000 | 0.0009 |
| 293.15 | 0.7000 | 0.0009 |
| 293.15 | 0.8000 | 0.0010 |
| 293.15 | 0.9001 | 0.0011 |
| 293.15 | 1.0000 | 0.0012 |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.0999 | 0.0008 |
| 298.15 | 0.2000 | 0.0008 |
| 298.15 | 0.3000 | 0.0008 |
| 298.15 | 0.4000 | 0.0008 |
| 298.15 | 0.5001 | 0.0008 |
| 298.15 | 0.6000 | 0.0008 |
| 298.15 | 0.7000 | 0.0009 |
| 298.15 | 0.8000 | 0.0009 |
| 298.15 | 0.9001 | 0.0010 |
| 298.15 | 1.0000 | 0.0011 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.0999 | 0.0008 |
| 303.15 | 0.2000 | 0.0008 |
| 303.15 | 0.3000 | 0.0008 |
| 303.15 | 0.4000 | 0.0008 |
| 303.15 | 0.5001 | 0.0008 |
| 303.15 | 0.6000 | 0.0008 |
| 303.15 | 0.7000 | 0.0008 |
| 303.15 | 0.8000 | 0.0008 |
| 303.15 | 0.9001 | 0.0009 |
| 303.15 | 1.0000 | 0.0010 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.0999 | 0.0007 |
| 313.15 | 0.2000 | 0.0007 |
| 313.15 | 0.3000 | 0.0007 |
| 313.15 | 0.4000 | 0.0007 |
| 313.15 | 0.5001 | 0.0007 |
| 313.15 | 0.6000 | 0.0007 |
| 313.15 | 0.7000 | 0.0007 |
| 313.15 | 0.8000 | 0.0007 |
| 313.15 | 0.9001 | 0.0008 |
| 313.15 | 1.0000 | 0.0008 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.0999 | 0.0006 |
| 323.15 | 0.2000 | 0.0006 |
| 323.15 | 0.3000 | 0.0006 |
| 323.15 | 0.4000 | 0.0006 |
| 323.15 | 0.5001 | 0.0006 |
| 323.15 | 0.6000 | 0.0006 |
| 323.15 | 0.7000 | 0.0006 |
| 323.15 | 0.8000 | 0.0006 |
| 323.15 | 0.9001 | 0.0007 |
| 323.15 | 1.0000 | 0.0007 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.0999 | 0.0005 |
| 333.15 | 0.2000 | 0.0005 |
| 333.15 | 0.3000 | 0.0005 |
| 333.15 | 0.4000 | 0.0005 |
| 333.15 | 0.5001 | 0.0005 |
| 333.15 | 0.6000 | 0.0005 |
| 333.15 | 0.7000 | 0.0005 |
| 333.15 | 0.8000 | 0.0005 |
| 333.15 | 0.9001 | 0.0006 |
| 333.15 | 1.0000 | 0.0006 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 948.95 |
| 293.15 | 0.0999 | 938.12 |
| 293.15 | 0.2000 | 925.78 |
| 293.15 | 0.3000 | 912.89 |
| 293.15 | 0.4000 | 898.61 |
| 293.15 | 0.5001 | 883.09 |
| 293.15 | 0.6000 | 867.07 |
| 293.15 | 0.7000 | 850.04 |
| 293.15 | 0.8000 | 831.44 |
| 293.15 | 0.9001 | 811.42 |
| 293.15 | 1.0000 | 789.85 |
| 298.15 | 0.0000 | 944.21 |
| 298.15 | 0.0999 | 933.4 |
| 298.15 | 0.2000 | 921.06 |
| 298.15 | 0.3000 | 908.23 |
| 298.15 | 0.4000 | 893.96 |
| 298.15 | 0.5001 | 878.46 |
| 298.15 | 0.6000 | 862.49 |
| 298.15 | 0.7000 | 845.49 |
| 298.15 | 0.8000 | 826.96 |
| 298.15 | 0.9001 | 807.05 |
| 298.15 | 1.0000 | 785.62 |
| 303.15 | 0.0000 | 939.45 |
| 303.15 | 0.0999 | 928.64 |
| 303.15 | 0.2000 | 916.32 |
| 303.15 | 0.3000 | 903.51 |
| 303.15 | 0.4000 | 889.23 |
| 303.15 | 0.5001 | 873.76 |
| 303.15 | 0.6000 | 857.82 |
| 303.15 | 0.7000 | 840.91 |
| 303.15 | 0.8000 | 822.44 |
| 303.15 | 0.9001 | 802.6 |
| 303.15 | 1.0000 | 781.31 |
| 313.15 | 0.0000 | 929.86 |
| 313.15 | 0.0999 | 919.06 |
| 313.15 | 0.2000 | 906.76 |
| 313.15 | 0.3000 | 893.95 |
| 313.15 | 0.4000 | 879.71 |
| 313.15 | 0.5001 | 864.29 |
| 313.15 | 0.6000 | 848.42 |
| 313.15 | 0.7000 | 831.6 |
| 313.15 | 0.8000 | 813.28 |
| 313.15 | 0.9001 | 793.64 |
| 313.15 | 1.0000 | 772.56 |
| 323.15 | 0.0000 | 920.92 |
| 323.15 | 0.0999 | 909.48 |
| 323.15 | 0.2000 | 897.18 |
| 323.15 | 0.3000 | 884.39 |
| 323.15 | 0.4000 | 870.17 |
| 323.15 | 0.5001 | 854.81 |
| 323.15 | 0.6000 | 838.98 |
| 323.15 | 0.7000 | 822.26 |
| 323.15 | 0.8000 | 804.04 |
| 323.15 | 0.9001 | 784.5 |
| 323.15 | 1.0000 | 763.67 |
| 333.15 | 0.0000 | 910.64 |
| 333.15 | 0.0999 | 899.8 |
| 333.15 | 0.2000 | 887.49 |
| 333.15 | 0.3000 | 874.73 |
| 333.15 | 0.4000 | 860.51 |
| 333.15 | 0.5001 | 845.16 |
| 333.15 | 0.6000 | 829.38 |
| 333.15 | 0.7000 | 812.71 |
| 333.15 | 0.8000 | 794.55 |
| 333.15 | 0.9001 | 775.2 |
| 333.15 | 1.0000 | 754.53 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 948.95 |
| 293.15 | 0.0999 | 938.12 |
| 293.15 | 0.2000 | 925.78 |
| 293.15 | 0.3000 | 912.89 |
| 293.15 | 0.4000 | 898.61 |
| 293.15 | 0.5001 | 883.09 |
| 293.15 | 0.6000 | 867.07 |
| 293.15 | 0.7000 | 850.04 |
| 293.15 | 0.8000 | 831.44 |
| 293.15 | 0.9001 | 811.42 |
| 293.15 | 1.0000 | 789.85 |
| 298.15 | 0.0000 | 944.21 |
| 298.15 | 0.0999 | 933.4 |
| 298.15 | 0.2000 | 921.06 |
| 298.15 | 0.3000 | 908.23 |
| 298.15 | 0.4000 | 893.96 |
| 298.15 | 0.5001 | 878.46 |
| 298.15 | 0.6000 | 862.49 |
| 298.15 | 0.7000 | 845.49 |
| 298.15 | 0.8000 | 826.96 |
| 298.15 | 0.9001 | 807.05 |
| 298.15 | 1.0000 | 785.62 |
| 303.15 | 0.0000 | 939.45 |
| 303.15 | 0.0999 | 928.64 |
| 303.15 | 0.2000 | 916.32 |
| 303.15 | 0.3000 | 903.51 |
| 303.15 | 0.4000 | 889.23 |
| 303.15 | 0.5001 | 873.76 |
| 303.15 | 0.6000 | 857.82 |
| 303.15 | 0.7000 | 840.91 |
| 303.15 | 0.8000 | 822.44 |
| 303.15 | 0.9001 | 802.6 |
| 303.15 | 1.0000 | 781.31 |
| 313.15 | 0.0000 | 929.86 |
| 313.15 | 0.0999 | 919.06 |
| 313.15 | 0.2000 | 906.76 |
| 313.15 | 0.3000 | 893.95 |
| 313.15 | 0.4000 | 879.71 |
| 313.15 | 0.5001 | 864.29 |
| 313.15 | 0.6000 | 848.42 |
| 313.15 | 0.7000 | 831.6 |
| 313.15 | 0.8000 | 813.28 |
| 313.15 | 0.9001 | 793.64 |
| 313.15 | 1.0000 | 772.56 |
| 323.15 | 0.0000 | 920.92 |
| 323.15 | 0.0999 | 909.48 |
| 323.15 | 0.2000 | 897.18 |
| 323.15 | 0.3000 | 884.39 |
| 323.15 | 0.4000 | 870.17 |
| 323.15 | 0.5001 | 854.81 |
| 323.15 | 0.6000 | 838.98 |
| 323.15 | 0.7000 | 822.26 |
| 323.15 | 0.8000 | 804.04 |
| 323.15 | 0.9001 | 784.5 |
| 323.15 | 1.0000 | 763.67 |
| 333.15 | 0.0000 | 910.64 |
| 333.15 | 0.0999 | 899.8 |
| 333.15 | 0.2000 | 887.49 |
| 333.15 | 0.3000 | 874.73 |
| 333.15 | 0.4000 | 860.51 |
| 333.15 | 0.5001 | 845.16 |
| 333.15 | 0.6000 | 829.38 |
| 333.15 | 0.7000 | 812.71 |
| 333.15 | 0.8000 | 794.55 |
| 333.15 | 0.9001 | 775.2 |
| 333.15 | 1.0000 | 754.53 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 95.5 (Liquid)
| Mole fraction of Ethanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 421.15 |
| 0.0511 | 414.05 |
| 0.0993 | 408.45 |
| 0.1501 | 403.35 |
| 0.1801 | 400.55 |
| 0.2510 | 394.65 |
| 0.2957 | 391.25 |
| 0.3501 | 387.25 |
| 0.3987 | 383.95 |
| 0.4502 | 380.65 |
| 0.4986 | 377.55 |
| 0.5501 | 374.35 |
| 0.5913 | 371.85 |
| 0.6503 | 368.35 |
| 0.6945 | 365.75 |
| 0.7504 | 362.55 |
| 0.7991 | 359.75 |
| 0.8502 | 356.85 |
| 0.8883 | 354.65 |
| 0.9501 | 351.65 |
| 1.0000 | 349.95 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 95.5 (Liquid)
| Mole fraction of Ethanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 421.15 |
| 0.0511 | 414.05 |
| 0.0993 | 408.45 |
| 0.1501 | 403.35 |
| 0.1801 | 400.55 |
| 0.2510 | 394.65 |
| 0.2957 | 391.25 |
| 0.3501 | 387.25 |
| 0.3987 | 383.95 |
| 0.4502 | 380.65 |
| 0.4986 | 377.55 |
| 0.5501 | 374.35 |
| 0.5913 | 371.85 |
| 0.6503 | 368.35 |
| 0.6945 | 365.75 |
| 0.7504 | 362.55 |
| 0.7991 | 359.75 |
| 0.8502 | 356.85 |
| 0.8883 | 354.65 |
| 0.9501 | 351.65 |
| 1.0000 | 349.95 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Volume fraction of Ethanol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0999 | -6.2000e-08 |
| 0.1000 | -6.4000e-08 |
| 0.2000 | -1.1500e-07 |
| 0.3998 | -1.8500e-07 |
| 0.4996 | -2.0100e-07 |
| 0.5032 | -2.0400e-07 |
| 0.6000 | -2.0400e-07 |
| 0.6012 | -2.0500e-07 |
| 0.7996 | -1.5800e-07 |
| 0.9000 | -1.0100e-07 |
| 0.9695 | -3.6000e-08 |
| 0.9779 | -2.6000e-08 |
| 0.9930 | -0.0000 |
| 0.9973 | -0.0000 |
| 0.9991 | -0.0000 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Volume fraction of Ethanol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0999 | -6.2000e-08 |
| 0.1000 | -6.4000e-08 |
| 0.2000 | -1.1500e-07 |
| 0.3998 | -1.8500e-07 |
| 0.4996 | -2.0100e-07 |
| 0.5032 | -2.0400e-07 |
| 0.6000 | -2.0400e-07 |
| 0.6012 | -2.0500e-07 |
| 0.7996 | -1.5800e-07 |
| 0.9000 | -1.0100e-07 |
| 0.9695 | -3.6000e-08 |
| 0.9779 | -2.6000e-08 |
| 0.9930 | -0.0000 |
| 0.9973 | -0.0000 |
| 0.9991 | -0.0000 |
Sources
- Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
- Excess Gibbs energies and volumes of the ternary system ethanol + dimethylformamide + tetrahydrofuran at 298.15K
- Volumetric Properties and Viscosities of Binary Mixtures of N,N-Dimethylformamide with Methanol and Ethanol in the Temperature Range (293.15 to 333.15) K