- 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
- 2-Pyrrolidinone, 1-methyl-
- InChI
- InChI=1S/C5H9NO/c1-6-4-2-3-5(6)7/h2-4H2,1H3
- InChI Key
- SECXISVLQFMRJM-UHFFFAOYSA-N
- Formula
- C5H9NO
- SMILES
- CN1CCCC1=O
- Mol. Weight (g/mol)
- 99.13
- CAS
- 872-50-4
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Datasets
- Activity coefficient (2)
- η - Viscosity, Pa*s (2)
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (2)
- Vapor Liquid Equilibrium at Constant Temperature (2)
Activity coefficient of Ethanol (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Ethanol (1) - Liquid |
|---|---|
| 333.20 | 0.6060 |
| 348.20 | 0.6050 |
| 363.20 | 0.6180 |
Activity coefficient of Ethanol (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Ethanol (1) - Liquid |
|---|---|
| 333.20 | 0.6060 |
| 348.20 | 0.6050 |
| 363.20 | 0.6180 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0011 |
| 293.15 | 0.0992 | 0.0011 |
| 293.15 | 0.1985 | 0.0012 |
| 293.15 | 0.2973 | 0.0012 |
| 293.15 | 0.3963 | 0.0013 |
| 293.15 | 0.4948 | 0.0014 |
| 293.15 | 0.5932 | 0.0014 |
| 293.15 | 0.6912 | 0.0015 |
| 293.15 | 0.7897 | 0.0016 |
| 293.15 | 0.8875 | 0.0017 |
| 293.15 | 1.0000 | 0.0019 |
| 303.15 | 0.0000 | 0.0010 |
| 303.15 | 0.0992 | 0.0010 |
| 303.15 | 0.1985 | 0.0010 |
| 303.15 | 0.2973 | 0.0010 |
| 303.15 | 0.3963 | 0.0011 |
| 303.15 | 0.4948 | 0.0011 |
| 303.15 | 0.5932 | 0.0012 |
| 303.15 | 0.6912 | 0.0013 |
| 303.15 | 0.7897 | 0.0014 |
| 303.15 | 0.8875 | 0.0014 |
| 303.15 | 1.0000 | 0.0016 |
| 313.15 | 0.0000 | 0.0008 |
| 313.15 | 0.0992 | 0.0008 |
| 313.15 | 0.1985 | 0.0008 |
| 313.15 | 0.2973 | 0.0009 |
| 313.15 | 0.3963 | 0.0009 |
| 313.15 | 0.4948 | 0.0010 |
| 313.15 | 0.5932 | 0.0010 |
| 313.15 | 0.6912 | 0.0011 |
| 313.15 | 0.7897 | 0.0012 |
| 313.15 | 0.8875 | 0.0012 |
| 313.15 | 1.0000 | 0.0013 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.0992 | 0.0007 |
| 323.15 | 0.1985 | 0.0007 |
| 323.15 | 0.2973 | 0.0007 |
| 323.15 | 0.3963 | 0.0008 |
| 323.15 | 0.4948 | 0.0008 |
| 323.15 | 0.5932 | 0.0009 |
| 323.15 | 0.6912 | 0.0010 |
| 323.15 | 0.7897 | 0.0010 |
| 323.15 | 0.8875 | 0.0011 |
| 323.15 | 1.0000 | 0.0011 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0011 |
| 293.15 | 0.0992 | 0.0011 |
| 293.15 | 0.1985 | 0.0012 |
| 293.15 | 0.2973 | 0.0012 |
| 293.15 | 0.3963 | 0.0013 |
| 293.15 | 0.4948 | 0.0014 |
| 293.15 | 0.5932 | 0.0014 |
| 293.15 | 0.6912 | 0.0015 |
| 293.15 | 0.7897 | 0.0016 |
| 293.15 | 0.8875 | 0.0017 |
| 293.15 | 1.0000 | 0.0019 |
| 303.15 | 0.0000 | 0.0010 |
| 303.15 | 0.0992 | 0.0010 |
| 303.15 | 0.1985 | 0.0010 |
| 303.15 | 0.2973 | 0.0010 |
| 303.15 | 0.3963 | 0.0011 |
| 303.15 | 0.4948 | 0.0011 |
| 303.15 | 0.5932 | 0.0012 |
| 303.15 | 0.6912 | 0.0013 |
| 303.15 | 0.7897 | 0.0014 |
| 303.15 | 0.8875 | 0.0014 |
| 303.15 | 1.0000 | 0.0016 |
| 313.15 | 0.0000 | 0.0008 |
| 313.15 | 0.0992 | 0.0008 |
| 313.15 | 0.1985 | 0.0008 |
| 313.15 | 0.2973 | 0.0009 |
| 313.15 | 0.3963 | 0.0009 |
| 313.15 | 0.4948 | 0.0010 |
| 313.15 | 0.5932 | 0.0010 |
| 313.15 | 0.6912 | 0.0011 |
| 313.15 | 0.7897 | 0.0012 |
| 313.15 | 0.8875 | 0.0012 |
| 313.15 | 1.0000 | 0.0013 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.0992 | 0.0007 |
| 323.15 | 0.1985 | 0.0007 |
| 323.15 | 0.2973 | 0.0007 |
| 323.15 | 0.3963 | 0.0008 |
| 323.15 | 0.4948 | 0.0008 |
| 323.15 | 0.5932 | 0.0009 |
| 323.15 | 0.6912 | 0.0010 |
| 323.15 | 0.7897 | 0.0010 |
| 323.15 | 0.8875 | 0.0011 |
| 323.15 | 1.0000 | 0.0011 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0000 | 1.3616 |
| 293.15 | 0.0992 | 1.3797 |
| 293.15 | 0.1985 | 1.3953 |
| 293.15 | 0.2973 | 1.4089 |
| 293.15 | 0.3963 | 1.4209 |
| 293.15 | 0.4948 | 1.4313 |
| 293.15 | 0.5932 | 1.4406 |
| 293.15 | 0.6912 | 1.449 |
| 293.15 | 0.7897 | 1.4563 |
| 293.15 | 0.8875 | 1.4633 |
| 293.15 | 1.0000 | 1.4706 |
| 303.15 | 0.0000 | 1.3574 |
| 303.15 | 0.0992 | 1.376 |
| 303.15 | 0.1985 | 1.3916 |
| 303.15 | 0.2973 | 1.4051 |
| 303.15 | 0.3963 | 1.4168 |
| 303.15 | 0.4948 | 1.4273 |
| 303.15 | 0.5932 | 1.4366 |
| 303.15 | 0.6912 | 1.4449 |
| 303.15 | 0.7897 | 1.4523 |
| 303.15 | 0.8875 | 1.4593 |
| 303.15 | 1.0000 | 1.4664 |
| 313.15 | 0.0000 | 1.3532 |
| 313.15 | 0.0992 | 1.3717 |
| 313.15 | 0.1985 | 1.3872 |
| 313.15 | 0.2973 | 1.4011 |
| 313.15 | 0.3963 | 1.4127 |
| 313.15 | 0.4948 | 1.4234 |
| 313.15 | 0.5932 | 1.4329 |
| 313.15 | 0.6912 | 1.4411 |
| 313.15 | 0.7897 | 1.4484 |
| 313.15 | 0.8875 | 1.4552 |
| 313.15 | 1.0000 | 1.4621 |
| 323.15 | 0.0000 | 1.3493 |
| 323.15 | 0.0992 | 1.3677 |
| 323.15 | 0.1985 | 1.3837 |
| 323.15 | 0.2973 | 1.3974 |
| 323.15 | 0.3963 | 1.4089 |
| 323.15 | 0.4948 | 1.4195 |
| 323.15 | 0.5932 | 1.4289 |
| 323.15 | 0.6912 | 1.4372 |
| 323.15 | 0.7897 | 1.4443 |
| 323.15 | 0.8875 | 1.4512 |
| 323.15 | 1.0000 | 1.4576 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0000 | 1.3616 |
| 293.15 | 0.0992 | 1.3797 |
| 293.15 | 0.1985 | 1.3953 |
| 293.15 | 0.2973 | 1.4089 |
| 293.15 | 0.3963 | 1.4209 |
| 293.15 | 0.4948 | 1.4313 |
| 293.15 | 0.5932 | 1.4406 |
| 293.15 | 0.6912 | 1.449 |
| 293.15 | 0.7897 | 1.4563 |
| 293.15 | 0.8875 | 1.4633 |
| 293.15 | 1.0000 | 1.4706 |
| 303.15 | 0.0000 | 1.3574 |
| 303.15 | 0.0992 | 1.376 |
| 303.15 | 0.1985 | 1.3916 |
| 303.15 | 0.2973 | 1.4051 |
| 303.15 | 0.3963 | 1.4168 |
| 303.15 | 0.4948 | 1.4273 |
| 303.15 | 0.5932 | 1.4366 |
| 303.15 | 0.6912 | 1.4449 |
| 303.15 | 0.7897 | 1.4523 |
| 303.15 | 0.8875 | 1.4593 |
| 303.15 | 1.0000 | 1.4664 |
| 313.15 | 0.0000 | 1.3532 |
| 313.15 | 0.0992 | 1.3717 |
| 313.15 | 0.1985 | 1.3872 |
| 313.15 | 0.2973 | 1.4011 |
| 313.15 | 0.3963 | 1.4127 |
| 313.15 | 0.4948 | 1.4234 |
| 313.15 | 0.5932 | 1.4329 |
| 313.15 | 0.6912 | 1.4411 |
| 313.15 | 0.7897 | 1.4484 |
| 313.15 | 0.8875 | 1.4552 |
| 313.15 | 1.0000 | 1.4621 |
| 323.15 | 0.0000 | 1.3493 |
| 323.15 | 0.0992 | 1.3677 |
| 323.15 | 0.1985 | 1.3837 |
| 323.15 | 0.2973 | 1.3974 |
| 323.15 | 0.3963 | 1.4089 |
| 323.15 | 0.4948 | 1.4195 |
| 323.15 | 0.5932 | 1.4289 |
| 323.15 | 0.6912 | 1.4372 |
| 323.15 | 0.7897 | 1.4443 |
| 323.15 | 0.8875 | 1.4512 |
| 323.15 | 1.0000 | 1.4576 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 789.54 |
| 293.15 | 0.0992 | 829.76 |
| 293.15 | 0.1985 | 864.84 |
| 293.15 | 0.2973 | 894.36 |
| 293.15 | 0.3963 | 920.89 |
| 293.15 | 0.4948 | 944.41 |
| 293.15 | 0.5932 | 965.0 |
| 293.15 | 0.6912 | 983.96 |
| 293.15 | 0.7897 | 1000.86 |
| 293.15 | 0.8875 | 1016.79 |
| 293.15 | 1.0000 | 1032.87 |
| 303.15 | 0.0000 | 780.94 |
| 303.15 | 0.0992 | 820.98 |
| 303.15 | 0.1985 | 855.96 |
| 303.15 | 0.2973 | 885.42 |
| 303.15 | 0.3963 | 911.91 |
| 303.15 | 0.4948 | 935.43 |
| 303.15 | 0.5932 | 955.97 |
| 303.15 | 0.6912 | 974.94 |
| 303.15 | 0.7897 | 991.85 |
| 303.15 | 0.8875 | 1007.8 |
| 303.15 | 1.0000 | 1023.95 |
| 313.15 | 0.0000 | 772.2 |
| 313.15 | 0.0992 | 812.09 |
| 313.15 | 0.1985 | 846.98 |
| 313.15 | 0.2973 | 876.39 |
| 313.15 | 0.3963 | 902.87 |
| 313.15 | 0.4948 | 926.39 |
| 313.15 | 0.5932 | 946.9 |
| 313.15 | 0.6912 | 965.89 |
| 313.15 | 0.7897 | 982.82 |
| 313.15 | 0.8875 | 998.8 |
| 313.15 | 1.0000 | 1015.03 |
| 323.15 | 0.0000 | 763.29 |
| 323.15 | 0.0992 | 803.05 |
| 323.15 | 0.1985 | 837.87 |
| 323.15 | 0.2973 | 867.27 |
| 323.15 | 0.3963 | 893.76 |
| 323.15 | 0.4948 | 917.3 |
| 323.15 | 0.5932 | 937.79 |
| 323.15 | 0.6912 | 956.8 |
| 323.15 | 0.7897 | 973.77 |
| 323.15 | 0.8875 | 989.78 |
| 323.15 | 1.0000 | 1006.1 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 789.54 |
| 293.15 | 0.0992 | 829.76 |
| 293.15 | 0.1985 | 864.84 |
| 293.15 | 0.2973 | 894.36 |
| 293.15 | 0.3963 | 920.89 |
| 293.15 | 0.4948 | 944.41 |
| 293.15 | 0.5932 | 965.0 |
| 293.15 | 0.6912 | 983.96 |
| 293.15 | 0.7897 | 1000.86 |
| 293.15 | 0.8875 | 1016.79 |
| 293.15 | 1.0000 | 1032.87 |
| 303.15 | 0.0000 | 780.94 |
| 303.15 | 0.0992 | 820.98 |
| 303.15 | 0.1985 | 855.96 |
| 303.15 | 0.2973 | 885.42 |
| 303.15 | 0.3963 | 911.91 |
| 303.15 | 0.4948 | 935.43 |
| 303.15 | 0.5932 | 955.97 |
| 303.15 | 0.6912 | 974.94 |
| 303.15 | 0.7897 | 991.85 |
| 303.15 | 0.8875 | 1007.8 |
| 303.15 | 1.0000 | 1023.95 |
| 313.15 | 0.0000 | 772.2 |
| 313.15 | 0.0992 | 812.09 |
| 313.15 | 0.1985 | 846.98 |
| 313.15 | 0.2973 | 876.39 |
| 313.15 | 0.3963 | 902.87 |
| 313.15 | 0.4948 | 926.39 |
| 313.15 | 0.5932 | 946.9 |
| 313.15 | 0.6912 | 965.89 |
| 313.15 | 0.7897 | 982.82 |
| 313.15 | 0.8875 | 998.8 |
| 313.15 | 1.0000 | 1015.03 |
| 323.15 | 0.0000 | 763.29 |
| 323.15 | 0.0992 | 803.05 |
| 323.15 | 0.1985 | 837.87 |
| 323.15 | 0.2973 | 867.27 |
| 323.15 | 0.3963 | 893.76 |
| 323.15 | 0.4948 | 917.3 |
| 323.15 | 0.5932 | 937.79 |
| 323.15 | 0.6912 | 956.8 |
| 323.15 | 0.7897 | 973.77 |
| 323.15 | 0.8875 | 989.78 |
| 323.15 | 1.0000 | 1006.1 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0000 | 1162.3 |
| 293.15 | 0.0992 | 1226.1 |
| 293.15 | 0.1985 | 1284.2 |
| 293.15 | 0.2973 | 1331.7 |
| 293.15 | 0.3963 | 1375.7 |
| 293.15 | 0.4948 | 1414.8 |
| 293.15 | 0.5932 | 1448.9 |
| 293.15 | 0.6912 | 1480.7 |
| 293.15 | 0.7897 | 1509.4 |
| 293.15 | 0.8875 | 1537.0 |
| 293.15 | 1.0000 | 1565.3 |
| 303.15 | 0.0000 | 1128.9 |
| 303.15 | 0.0992 | 1191.3 |
| 303.15 | 0.1985 | 1248.9 |
| 303.15 | 0.2973 | 1295.9 |
| 303.15 | 0.3963 | 1338.9 |
| 303.15 | 0.4948 | 1377.6 |
| 303.15 | 0.5932 | 1411.4 |
| 303.15 | 0.6912 | 1442.9 |
| 303.15 | 0.7897 | 1471.4 |
| 303.15 | 0.8875 | 1498.5 |
| 303.15 | 1.0000 | 1526.5 |
| 313.15 | 0.0000 | 1095.4 |
| 313.15 | 0.0992 | 1157.0 |
| 313.15 | 0.1985 | 1214.7 |
| 313.15 | 0.2973 | 1260.3 |
| 313.15 | 0.3963 | 1302.5 |
| 313.15 | 0.4948 | 1341.0 |
| 313.15 | 0.5932 | 1374.2 |
| 313.15 | 0.6912 | 1405.3 |
| 313.15 | 0.7897 | 1433.5 |
| 313.15 | 0.8875 | 1460.3 |
| 313.15 | 1.0000 | 1487.8 |
| 323.15 | 0.0000 | 1071.9 |
| 323.15 | 0.0992 | 1122.7 |
| 323.15 | 0.1985 | 1179.6 |
| 323.15 | 0.2973 | 1224.9 |
| 323.15 | 0.3963 | 1266.6 |
| 323.15 | 0.4948 | 1304.6 |
| 323.15 | 0.5932 | 1337.3 |
| 323.15 | 0.6912 | 1368.3 |
| 323.15 | 0.7897 | 1396.1 |
| 323.15 | 0.8875 | 1422.8 |
| 323.15 | 1.0000 | 1450.2 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Pyrrolidinone, 1-methyl- (2) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0000 | 1162.3 |
| 293.15 | 0.0992 | 1226.1 |
| 293.15 | 0.1985 | 1284.2 |
| 293.15 | 0.2973 | 1331.7 |
| 293.15 | 0.3963 | 1375.7 |
| 293.15 | 0.4948 | 1414.8 |
| 293.15 | 0.5932 | 1448.9 |
| 293.15 | 0.6912 | 1480.7 |
| 293.15 | 0.7897 | 1509.4 |
| 293.15 | 0.8875 | 1537.0 |
| 293.15 | 1.0000 | 1565.3 |
| 303.15 | 0.0000 | 1128.9 |
| 303.15 | 0.0992 | 1191.3 |
| 303.15 | 0.1985 | 1248.9 |
| 303.15 | 0.2973 | 1295.9 |
| 303.15 | 0.3963 | 1338.9 |
| 303.15 | 0.4948 | 1377.6 |
| 303.15 | 0.5932 | 1411.4 |
| 303.15 | 0.6912 | 1442.9 |
| 303.15 | 0.7897 | 1471.4 |
| 303.15 | 0.8875 | 1498.5 |
| 303.15 | 1.0000 | 1526.5 |
| 313.15 | 0.0000 | 1095.4 |
| 313.15 | 0.0992 | 1157.0 |
| 313.15 | 0.1985 | 1214.7 |
| 313.15 | 0.2973 | 1260.3 |
| 313.15 | 0.3963 | 1302.5 |
| 313.15 | 0.4948 | 1341.0 |
| 313.15 | 0.5932 | 1374.2 |
| 313.15 | 0.6912 | 1405.3 |
| 313.15 | 0.7897 | 1433.5 |
| 313.15 | 0.8875 | 1460.3 |
| 313.15 | 1.0000 | 1487.8 |
| 323.15 | 0.0000 | 1071.9 |
| 323.15 | 0.0992 | 1122.7 |
| 323.15 | 0.1985 | 1179.6 |
| 323.15 | 0.2973 | 1224.9 |
| 323.15 | 0.3963 | 1266.6 |
| 323.15 | 0.4948 | 1304.6 |
| 323.15 | 0.5932 | 1337.3 |
| 323.15 | 0.6912 | 1368.3 |
| 323.15 | 0.7897 | 1396.1 |
| 323.15 | 0.8875 | 1422.8 |
| 323.15 | 1.0000 | 1450.2 |
Vapor Liquid Equilibrium at Constant Temperature [ref]
Operational condition: Temperature, K = 333.15 (VLE)
| P [kPa] - VLE | x1[mol/mol] of Ethanol (1) - Liquid |
|---|---|
| 0.4706 | 0.0000 |
| 2.16 | 0.0660 |
| 2.66 | 0.0930 |
| 3.94 | 0.1400 |
| 6.09 | 0.2150 |
| 8.45 | 0.2750 |
| 11.08 | 0.3340 |
| 13.35 | 0.3850 |
| 15.549 | 0.4350 |
| 18.131 | 0.4890 |
| 21.7 | 0.5550 |
| 24.17 | 0.5970 |
| 26.81 | 0.6430 |
| 29.24 | 0.6860 |
| 31.76 | 0.7280 |
| 34.291 | 0.7700 |
| 36.61 | 0.8120 |
| 38.61 | 0.8460 |
| 40.641 | 0.8830 |
| 43.9 | 0.9410 |
| 45.3 | 0.9680 |
| 46.92 | 1.0000 |
Vapor Liquid Equilibrium at Constant Temperature [ref]
Operational condition: Temperature, K = 313.15 (VLE)
| P [kPa] - VLE | x1[mol/mol] of Ethanol (1) - Liquid |
|---|---|
| 0.1387 | 0.0000 |
| 0.7706 | 0.0617 |
| 1.332 | 0.1130 |
| 2.0465 | 0.1722 |
| 2.7464 | 0.2254 |
| 3.702 | 0.2923 |
| 4.08 | 0.3146 |
| 5.264 | 0.3888 |
| 5.641 | 0.4102 |
| 6.02 | 0.4309 |
| 7.206 | 0.4943 |
| 8.577 | 0.5622 |
| 9.018 | 0.5831 |
| 10.828 | 0.6661 |
| 12.386 | 0.7368 |
| 13.423 | 0.7838 |
| 14.669 | 0.8408 |
| 15.975 | 0.9020 |
| 16.763 | 0.9418 |
| 17.887 | 1.0000 |
Sources
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
- Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K