- Name
- 1-Propanamine, N-propyl-
- InChI
- InChI=1S/C6H15N/c1-3-5-7-6-4-2/h7H,3-6H2,1-2H3
- InChI Key
- WEHWNAOGRSTTBQ-UHFFFAOYSA-N
- Formula
- C6H15N
- SMILES
- CCCNCCC
- Mol. Weight (g/mol)
- 101.19
- CAS
- 142-84-7
- Name
- 2-Heptanone
- InChI
- InChI=1S/C7H14O/c1-3-4-5-6-7(2)8/h3-6H2,1-2H3
- InChI Key
- CATSNJVOTSVZJV-UHFFFAOYSA-N
- Formula
- C7H14O
- SMILES
- CCCCCC(C)=O
- Mol. Weight (g/mol)
- 114.19
- CAS
- 110-43-0
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
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (2)
- Excess molar volume, m3/mol (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Propanamine, N-propyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1145 | 0.0470 |
| 0.2120 | 0.0880 |
| 0.3072 | 0.1180 |
| 0.4034 | 0.1430 |
| 0.4993 | 0.1620 |
| 0.6017 | 0.1700 |
| 0.6872 | 0.1590 |
| 0.7868 | 0.1370 |
| 0.8796 | 0.0960 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Propanamine, N-propyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1145 | 0.0470 |
| 0.2120 | 0.0880 |
| 0.3072 | 0.1180 |
| 0.4034 | 0.1430 |
| 0.4993 | 0.1620 |
| 0.6017 | 0.1700 |
| 0.6872 | 0.1590 |
| 0.7868 | 0.1370 |
| 0.8796 | 0.0960 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Heptanone (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0603 | 743.175 |
| 293.15 | 0.1045 | 746.717 |
| 293.15 | 0.1559 | 750.817 |
| 293.15 | 0.2013 | 754.413 |
| 293.15 | 0.2526 | 758.468 |
| 293.15 | 0.2936 | 761.7 |
| 293.15 | 0.3492 | 766.042 |
| 293.15 | 0.4579 | 774.494 |
| 293.15 | 0.4930 | 777.204 |
| 293.15 | 0.5494 | 781.554 |
| 293.15 | 0.5894 | 784.624 |
| 293.15 | 0.6478 | 789.087 |
| 293.15 | 0.6896 | 792.266 |
| 293.15 | 0.7615 | 797.717 |
| 293.15 | 0.8025 | 800.833 |
| 293.15 | 0.8139 | 801.69 |
| 293.15 | 0.8993 | 808.079 |
| 293.15 | 0.9480 | 811.684 |
| 298.15 | 0.0521 | 738.054 |
| 298.15 | 0.1048 | 742.273 |
| 298.15 | 0.1557 | 746.324 |
| 298.15 | 0.2000 | 749.853 |
| 298.15 | 0.2526 | 754.005 |
| 298.15 | 0.2962 | 757.449 |
| 298.15 | 0.3436 | 761.173 |
| 298.15 | 0.3850 | 764.422 |
| 298.15 | 0.4478 | 769.307 |
| 298.15 | 0.5427 | 776.662 |
| 298.15 | 0.6003 | 781.222 |
| 298.15 | 0.6436 | 784.41 |
| 298.15 | 0.6900 | 787.95 |
| 298.15 | 0.7418 | 791.892 |
| 298.15 | 0.8061 | 796.768 |
| 298.15 | 0.8548 | 800.432 |
| 298.15 | 0.8993 | 803.773 |
| 298.15 | 0.9528 | 807.724 |
| 303.15 | 0.0578 | 733.883 |
| 303.15 | 0.1054 | 737.733 |
| 303.15 | 0.1579 | 741.943 |
| 303.15 | 0.2005 | 745.356 |
| 303.15 | 0.2497 | 749.277 |
| 303.15 | 0.2951 | 752.865 |
| 303.15 | 0.3476 | 756.998 |
| 303.15 | 0.3856 | 759.993 |
| 303.15 | 0.4504 | 765.062 |
| 303.15 | 0.5442 | 772.346 |
| 303.15 | 0.5891 | 775.815 |
| 303.15 | 0.6420 | 779.872 |
| 303.15 | 0.6870 | 783.319 |
| 303.15 | 0.7413 | 787.465 |
| 303.15 | 0.7994 | 791.897 |
| 303.15 | 0.8564 | 796.191 |
| 303.15 | 0.8993 | 799.423 |
| 303.15 | 0.9497 | 803.188 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Heptanone (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0603 | 743.175 |
| 293.15 | 0.1045 | 746.717 |
| 293.15 | 0.1559 | 750.817 |
| 293.15 | 0.2013 | 754.413 |
| 293.15 | 0.2526 | 758.468 |
| 293.15 | 0.2936 | 761.7 |
| 293.15 | 0.3492 | 766.042 |
| 293.15 | 0.4579 | 774.494 |
| 293.15 | 0.4930 | 777.204 |
| 293.15 | 0.5494 | 781.554 |
| 293.15 | 0.5894 | 784.624 |
| 293.15 | 0.6478 | 789.087 |
| 293.15 | 0.6896 | 792.266 |
| 293.15 | 0.7615 | 797.717 |
| 293.15 | 0.8025 | 800.833 |
| 293.15 | 0.8139 | 801.69 |
| 293.15 | 0.8993 | 808.079 |
| 293.15 | 0.9480 | 811.684 |
| 298.15 | 0.0521 | 738.054 |
| 298.15 | 0.1048 | 742.273 |
| 298.15 | 0.1557 | 746.324 |
| 298.15 | 0.2000 | 749.853 |
| 298.15 | 0.2526 | 754.005 |
| 298.15 | 0.2962 | 757.449 |
| 298.15 | 0.3436 | 761.173 |
| 298.15 | 0.3850 | 764.422 |
| 298.15 | 0.4478 | 769.307 |
| 298.15 | 0.5427 | 776.662 |
| 298.15 | 0.6003 | 781.222 |
| 298.15 | 0.6436 | 784.41 |
| 298.15 | 0.6900 | 787.95 |
| 298.15 | 0.7418 | 791.892 |
| 298.15 | 0.8061 | 796.768 |
| 298.15 | 0.8548 | 800.432 |
| 298.15 | 0.8993 | 803.773 |
| 298.15 | 0.9528 | 807.724 |
| 303.15 | 0.0578 | 733.883 |
| 303.15 | 0.1054 | 737.733 |
| 303.15 | 0.1579 | 741.943 |
| 303.15 | 0.2005 | 745.356 |
| 303.15 | 0.2497 | 749.277 |
| 303.15 | 0.2951 | 752.865 |
| 303.15 | 0.3476 | 756.998 |
| 303.15 | 0.3856 | 759.993 |
| 303.15 | 0.4504 | 765.062 |
| 303.15 | 0.5442 | 772.346 |
| 303.15 | 0.5891 | 775.815 |
| 303.15 | 0.6420 | 779.872 |
| 303.15 | 0.6870 | 783.319 |
| 303.15 | 0.7413 | 787.465 |
| 303.15 | 0.7994 | 791.897 |
| 303.15 | 0.8564 | 796.191 |
| 303.15 | 0.8993 | 799.423 |
| 303.15 | 0.9497 | 803.188 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Heptanone (2) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0603 | 1213.92 |
| 293.15 | 0.1045 | 1217.16 |
| 293.15 | 0.1559 | 1220.98 |
| 293.15 | 0.2013 | 1224.34 |
| 293.15 | 0.2526 | 1228.07 |
| 293.15 | 0.2936 | 1231.1 |
| 293.15 | 0.3492 | 1235.18 |
| 293.15 | 0.4579 | 1243.0 |
| 293.15 | 0.4930 | 1245.63 |
| 293.15 | 0.5494 | 1249.63 |
| 293.15 | 0.5894 | 1252.58 |
| 293.15 | 0.6478 | 1256.87 |
| 293.15 | 0.6896 | 1259.89 |
| 293.15 | 0.7615 | 1265.06 |
| 293.15 | 0.8025 | 1267.98 |
| 293.15 | 0.8139 | 1268.79 |
| 293.15 | 0.8993 | 1274.99 |
| 293.15 | 0.9480 | 1278.43 |
| 298.15 | 0.0521 | 1191.83 |
| 298.15 | 0.1048 | 1195.99 |
| 298.15 | 0.1557 | 1199.81 |
| 298.15 | 0.2000 | 1203.17 |
| 298.15 | 0.2526 | 1207.08 |
| 298.15 | 0.2962 | 1210.38 |
| 298.15 | 0.3436 | 1213.91 |
| 298.15 | 0.3850 | 1217.04 |
| 298.15 | 0.4478 | 1221.7 |
| 298.15 | 0.5427 | 1228.84 |
| 298.15 | 0.6436 | 1236.36 |
| 298.15 | 0.6900 | 1239.82 |
| 298.15 | 0.7418 | 1243.63 |
| 298.15 | 0.8061 | 1248.48 |
| 298.15 | 0.8548 | 1251.96 |
| 298.15 | 0.8993 | 1255.34 |
| 298.15 | 0.9528 | 1259.09 |
| 303.15 | 0.0578 | 1172.14 |
| 303.15 | 0.1054 | 1175.85 |
| 303.15 | 0.1579 | 1179.93 |
| 303.15 | 0.2005 | 1183.24 |
| 303.15 | 0.2497 | 1187.1 |
| 303.15 | 0.2951 | 1190.6 |
| 303.15 | 0.3476 | 1194.66 |
| 303.15 | 0.3856 | 1197.65 |
| 303.15 | 0.4504 | 1202.61 |
| 303.15 | 0.5442 | 1209.82 |
| 303.15 | 0.5891 | 1213.37 |
| 303.15 | 0.6420 | 1217.32 |
| 303.15 | 0.6870 | 1220.79 |
| 303.15 | 0.7413 | 1224.95 |
| 303.15 | 0.7994 | 1229.37 |
| 303.15 | 0.8564 | 1233.66 |
| 303.15 | 0.8993 | 1236.92 |
| 303.15 | 0.9497 | 1239.96 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Heptanone (2) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0603 | 1213.92 |
| 293.15 | 0.1045 | 1217.16 |
| 293.15 | 0.1559 | 1220.98 |
| 293.15 | 0.2013 | 1224.34 |
| 293.15 | 0.2526 | 1228.07 |
| 293.15 | 0.2936 | 1231.1 |
| 293.15 | 0.3492 | 1235.18 |
| 293.15 | 0.4579 | 1243.0 |
| 293.15 | 0.4930 | 1245.63 |
| 293.15 | 0.5494 | 1249.63 |
| 293.15 | 0.5894 | 1252.58 |
| 293.15 | 0.6478 | 1256.87 |
| 293.15 | 0.6896 | 1259.89 |
| 293.15 | 0.7615 | 1265.06 |
| 293.15 | 0.8025 | 1267.98 |
| 293.15 | 0.8139 | 1268.79 |
| 293.15 | 0.8993 | 1274.99 |
| 293.15 | 0.9480 | 1278.43 |
| 298.15 | 0.0521 | 1191.83 |
| 298.15 | 0.1048 | 1195.99 |
| 298.15 | 0.1557 | 1199.81 |
| 298.15 | 0.2000 | 1203.17 |
| 298.15 | 0.2526 | 1207.08 |
| 298.15 | 0.2962 | 1210.38 |
| 298.15 | 0.3436 | 1213.91 |
| 298.15 | 0.3850 | 1217.04 |
| 298.15 | 0.4478 | 1221.7 |
| 298.15 | 0.5427 | 1228.84 |
| 298.15 | 0.6436 | 1236.36 |
| 298.15 | 0.6900 | 1239.82 |
| 298.15 | 0.7418 | 1243.63 |
| 298.15 | 0.8061 | 1248.48 |
| 298.15 | 0.8548 | 1251.96 |
| 298.15 | 0.8993 | 1255.34 |
| 298.15 | 0.9528 | 1259.09 |
| 303.15 | 0.0578 | 1172.14 |
| 303.15 | 0.1054 | 1175.85 |
| 303.15 | 0.1579 | 1179.93 |
| 303.15 | 0.2005 | 1183.24 |
| 303.15 | 0.2497 | 1187.1 |
| 303.15 | 0.2951 | 1190.6 |
| 303.15 | 0.3476 | 1194.66 |
| 303.15 | 0.3856 | 1197.65 |
| 303.15 | 0.4504 | 1202.61 |
| 303.15 | 0.5442 | 1209.82 |
| 303.15 | 0.5891 | 1213.37 |
| 303.15 | 0.6420 | 1217.32 |
| 303.15 | 0.6870 | 1220.79 |
| 303.15 | 0.7413 | 1224.95 |
| 303.15 | 0.7994 | 1229.37 |
| 303.15 | 0.8564 | 1233.66 |
| 303.15 | 0.8993 | 1236.92 |
| 303.15 | 0.9497 | 1239.96 |
Excess molar volume, m3/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Heptanone (2) - Liquid | Excess molar volume, m3/mol - Liquid |
| 293.15 | 0.0603 | -3.0000e-08 |
| 293.15 | 0.1045 | -4.1900e-08 |
| 293.15 | 0.1559 | -5.4600e-08 |
| 293.15 | 0.2013 | -6.3000e-08 |
| 293.15 | 0.2526 | -7.1000e-08 |
| 293.15 | 0.2936 | -7.7500e-08 |
| 293.15 | 0.3492 | -8.0900e-08 |
| 293.15 | 0.4579 | -8.3800e-08 |
| 293.15 | 0.4930 | -8.3300e-08 |
| 293.15 | 0.5494 | -8.2200e-08 |
| 293.15 | 0.5894 | -7.9800e-08 |
| 293.15 | 0.6478 | -7.7200e-08 |
| 293.15 | 0.6896 | -7.2700e-08 |
| 293.15 | 0.7615 | -6.4700e-08 |
| 293.15 | 0.8025 | -5.8400e-08 |
| 293.15 | 0.8139 | -5.6100e-08 |
| 293.15 | 0.8993 | -4.2300e-08 |
| 293.15 | 0.9480 | -2.8000e-08 |
| 298.15 | 0.0521 | -2.1500e-08 |
| 298.15 | 0.1048 | -3.8900e-08 |
| 298.15 | 0.1557 | -4.9800e-08 |
| 298.15 | 0.2000 | -5.9600e-08 |
| 298.15 | 0.2526 | -6.6400e-08 |
| 298.15 | 0.2962 | -7.4100e-08 |
| 298.15 | 0.3436 | -7.9800e-08 |
| 298.15 | 0.3850 | -8.4600e-08 |
| 298.15 | 0.4478 | -8.6800e-08 |
| 298.15 | 0.5427 | -8.7700e-08 |
| 298.15 | 0.6003 | -8.5800e-08 |
| 298.15 | 0.6436 | -8.3200e-08 |
| 298.15 | 0.6900 | -7.8700e-08 |
| 298.15 | 0.7418 | -7.3200e-08 |
| 298.15 | 0.8061 | -6.5800e-08 |
| 298.15 | 0.8548 | -5.7400e-08 |
| 298.15 | 0.8993 | -4.8600e-08 |
| 298.15 | 0.9528 | -2.9100e-08 |
| 303.15 | 0.0578 | -2.7300e-08 |
| 303.15 | 0.1054 | -4.4100e-08 |
| 303.15 | 0.1579 | -5.8100e-08 |
| 303.15 | 0.2005 | -6.9300e-08 |
| 303.15 | 0.2497 | -7.9800e-08 |
| 303.15 | 0.2951 | -8.5500e-08 |
| 303.15 | 0.3476 | -9.0500e-08 |
| 303.15 | 0.3856 | -9.5500e-08 |
| 303.15 | 0.4504 | -9.7500e-08 |
| 303.15 | 0.5442 | -9.7300e-08 |
| 303.15 | 0.5891 | -9.5600e-08 |
| 303.15 | 0.6420 | -8.9700e-08 |
| 303.15 | 0.6870 | -8.4100e-08 |
| 303.15 | 0.7413 | -7.8100e-08 |
| 303.15 | 0.7994 | -7.0700e-08 |
| 303.15 | 0.8564 | -5.7200e-08 |
| 303.15 | 0.8993 | -4.8800e-08 |
| 303.15 | 0.9497 | -3.2800e-08 |
Excess molar volume, m3/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Heptanone (2) - Liquid | Excess molar volume, m3/mol - Liquid |
| 293.15 | 0.0603 | -3.0000e-08 |
| 293.15 | 0.1045 | -4.1900e-08 |
| 293.15 | 0.1559 | -5.4600e-08 |
| 293.15 | 0.2013 | -6.3000e-08 |
| 293.15 | 0.2526 | -7.1000e-08 |
| 293.15 | 0.2936 | -7.7500e-08 |
| 293.15 | 0.3492 | -8.0900e-08 |
| 293.15 | 0.4579 | -8.3800e-08 |
| 293.15 | 0.4930 | -8.3300e-08 |
| 293.15 | 0.5494 | -8.2200e-08 |
| 293.15 | 0.5894 | -7.9800e-08 |
| 293.15 | 0.6478 | -7.7200e-08 |
| 293.15 | 0.6896 | -7.2700e-08 |
| 293.15 | 0.7615 | -6.4700e-08 |
| 293.15 | 0.8025 | -5.8400e-08 |
| 293.15 | 0.8139 | -5.6100e-08 |
| 293.15 | 0.8993 | -4.2300e-08 |
| 293.15 | 0.9480 | -2.8000e-08 |
| 298.15 | 0.0521 | -2.1500e-08 |
| 298.15 | 0.1048 | -3.8900e-08 |
| 298.15 | 0.1557 | -4.9800e-08 |
| 298.15 | 0.2000 | -5.9600e-08 |
| 298.15 | 0.2526 | -6.6400e-08 |
| 298.15 | 0.2962 | -7.4100e-08 |
| 298.15 | 0.3436 | -7.9800e-08 |
| 298.15 | 0.3850 | -8.4600e-08 |
| 298.15 | 0.4478 | -8.6800e-08 |
| 298.15 | 0.5427 | -8.7700e-08 |
| 298.15 | 0.6003 | -8.5800e-08 |
| 298.15 | 0.6436 | -8.3200e-08 |
| 298.15 | 0.6900 | -7.8700e-08 |
| 298.15 | 0.7418 | -7.3200e-08 |
| 298.15 | 0.8061 | -6.5800e-08 |
| 298.15 | 0.8548 | -5.7400e-08 |
| 298.15 | 0.8993 | -4.8600e-08 |
| 298.15 | 0.9528 | -2.9100e-08 |
| 303.15 | 0.0578 | -2.7300e-08 |
| 303.15 | 0.1054 | -4.4100e-08 |
| 303.15 | 0.1579 | -5.8100e-08 |
| 303.15 | 0.2005 | -6.9300e-08 |
| 303.15 | 0.2497 | -7.9800e-08 |
| 303.15 | 0.2951 | -8.5500e-08 |
| 303.15 | 0.3476 | -9.0500e-08 |
| 303.15 | 0.3856 | -9.5500e-08 |
| 303.15 | 0.4504 | -9.7500e-08 |
| 303.15 | 0.5442 | -9.7300e-08 |
| 303.15 | 0.5891 | -9.5600e-08 |
| 303.15 | 0.6420 | -8.9700e-08 |
| 303.15 | 0.6870 | -8.4100e-08 |
| 303.15 | 0.7413 | -7.8100e-08 |
| 303.15 | 0.7994 | -7.0700e-08 |
| 303.15 | 0.8564 | -5.7200e-08 |
| 303.15 | 0.8993 | -4.8800e-08 |
| 303.15 | 0.9497 | -3.2800e-08 |
Sources
- Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
- Thermodynamics of (ketone + amine) mixtures. Part VI. Volumetric and speed of sound data at (293.15, 298.15, and 303.15) K for (2-heptanone + dipropylamine, +dibutylamine, or +triethylamine) systems