- Name
- Aniline, N-methyl-
- InChI
- InChI=1S/C7H9N/c1-8-7-5-3-2-4-6-7/h2-6,8H,1H3
- InChI Key
- AFBPFSWMIHJQDM-UHFFFAOYSA-N
- Formula
- C7H9N
- SMILES
- CNc1ccccc1
- Mol. Weight (g/mol)
- 107.15
- CAS
- 100-61-8
- Name
- Heptane
- InChI
- InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
- InChI Key
- IMNFDUFMRHMDMM-UHFFFAOYSA-N
- Formula
- C7H16
- SMILES
- CCCCCCC
- Mol. Weight (g/mol)
- 100.20
- CAS
- 142-82-5
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Datasets
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (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 Aniline, N-methyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1020 | 0.8180 |
| 0.1982 | 1.292 |
| 0.2968 | 1.539 |
| 0.3935 | 1.654 |
| 0.4983 | 1.676 |
| 0.5982 | 1.6 |
| 0.6934 | 1.439 |
| 0.7941 | 1.126 |
| 0.8939 | 0.6790 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Aniline, N-methyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1020 | 0.8180 |
| 0.1982 | 1.292 |
| 0.2968 | 1.539 |
| 0.3935 | 1.654 |
| 0.4983 | 1.676 |
| 0.5982 | 1.6 |
| 0.6934 | 1.439 |
| 0.7941 | 1.126 |
| 0.8939 | 0.6790 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Aniline, N-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0540 | 695.999 |
| 293.15 | 0.1084 | 708.778 |
| 293.15 | 0.1536 | 719.814 |
| 293.15 | 0.2000 | 731.341 |
| 293.15 | 0.2556 | 745.704 |
| 293.15 | 0.2976 | 756.81 |
| 293.15 | 0.3473 | 770.261 |
| 293.15 | 0.3944 | 783.41 |
| 293.15 | 0.4485 | 798.879 |
| 293.15 | 0.4953 | 812.615 |
| 293.15 | 0.5355 | 824.725 |
| 293.15 | 0.5990 | 844.458 |
| 293.15 | 0.6436 | 858.711 |
| 293.15 | 0.7024 | 878.07 |
| 293.15 | 0.7457 | 892.769 |
| 293.15 | 0.7858 | 906.675 |
| 293.15 | 0.8459 | 928.153 |
| 293.15 | 0.8952 | 946.22 |
| 293.15 | 0.9491 | 966.608 |
| 298.15 | 0.0577 | 692.58 |
| 298.15 | 0.1072 | 704.27 |
| 298.15 | 0.1473 | 713.999 |
| 298.15 | 0.2055 | 728.558 |
| 298.15 | 0.2595 | 742.491 |
| 298.15 | 0.3033 | 754.107 |
| 298.15 | 0.3401 | 764.024 |
| 298.15 | 0.3955 | 779.471 |
| 298.15 | 0.4559 | 796.765 |
| 298.15 | 0.5030 | 810.692 |
| 298.15 | 0.5431 | 822.843 |
| 298.15 | 0.5956 | 839.178 |
| 298.15 | 0.6441 | 854.671 |
| 298.15 | 0.6995 | 872.931 |
| 298.15 | 0.7491 | 889.715 |
| 298.15 | 0.7964 | 906.279 |
| 298.15 | 0.8446 | 923.55 |
| 298.15 | 0.8949 | 942.036 |
| 298.15 | 0.9465 | 961.528 |
| 303.15 | 0.0615 | 689.386 |
| 303.15 | 0.1111 | 701.082 |
| 303.15 | 0.1548 | 711.723 |
| 303.15 | 0.2069 | 724.76 |
| 303.15 | 0.2501 | 735.88 |
| 303.15 | 0.2964 | 748.035 |
| 303.15 | 0.3480 | 762.057 |
| 303.15 | 0.3979 | 775.964 |
| 303.15 | 0.4513 | 791.356 |
| 303.15 | 0.5003 | 805.793 |
| 303.15 | 0.5583 | 823.48 |
| 303.15 | 0.5988 | 836.196 |
| 303.15 | 0.6470 | 851.618 |
| 303.15 | 0.7026 | 869.963 |
| 303.15 | 0.7475 | 885.221 |
| 303.15 | 0.7954 | 901.919 |
| 303.15 | 0.8446 | 919.525 |
| 303.15 | 0.8917 | 936.846 |
| 303.15 | 0.9404 | 955.244 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Aniline, N-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0540 | 695.999 |
| 293.15 | 0.1084 | 708.778 |
| 293.15 | 0.1536 | 719.814 |
| 293.15 | 0.2000 | 731.341 |
| 293.15 | 0.2556 | 745.704 |
| 293.15 | 0.2976 | 756.81 |
| 293.15 | 0.3473 | 770.261 |
| 293.15 | 0.3944 | 783.41 |
| 293.15 | 0.4485 | 798.879 |
| 293.15 | 0.4953 | 812.615 |
| 293.15 | 0.5355 | 824.725 |
| 293.15 | 0.5990 | 844.458 |
| 293.15 | 0.6436 | 858.711 |
| 293.15 | 0.7024 | 878.07 |
| 293.15 | 0.7457 | 892.769 |
| 293.15 | 0.7858 | 906.675 |
| 293.15 | 0.8459 | 928.153 |
| 293.15 | 0.8952 | 946.22 |
| 293.15 | 0.9491 | 966.608 |
| 298.15 | 0.0577 | 692.58 |
| 298.15 | 0.1072 | 704.27 |
| 298.15 | 0.1473 | 713.999 |
| 298.15 | 0.2055 | 728.558 |
| 298.15 | 0.2595 | 742.491 |
| 298.15 | 0.3033 | 754.107 |
| 298.15 | 0.3401 | 764.024 |
| 298.15 | 0.3955 | 779.471 |
| 298.15 | 0.4559 | 796.765 |
| 298.15 | 0.5030 | 810.692 |
| 298.15 | 0.5431 | 822.843 |
| 298.15 | 0.5956 | 839.178 |
| 298.15 | 0.6441 | 854.671 |
| 298.15 | 0.6995 | 872.931 |
| 298.15 | 0.7491 | 889.715 |
| 298.15 | 0.7964 | 906.279 |
| 298.15 | 0.8446 | 923.55 |
| 298.15 | 0.8949 | 942.036 |
| 298.15 | 0.9465 | 961.528 |
| 303.15 | 0.0615 | 689.386 |
| 303.15 | 0.1111 | 701.082 |
| 303.15 | 0.1548 | 711.723 |
| 303.15 | 0.2069 | 724.76 |
| 303.15 | 0.2501 | 735.88 |
| 303.15 | 0.2964 | 748.035 |
| 303.15 | 0.3480 | 762.057 |
| 303.15 | 0.3979 | 775.964 |
| 303.15 | 0.4513 | 791.356 |
| 303.15 | 0.5003 | 805.793 |
| 303.15 | 0.5583 | 823.48 |
| 303.15 | 0.5988 | 836.196 |
| 303.15 | 0.6470 | 851.618 |
| 303.15 | 0.7026 | 869.963 |
| 303.15 | 0.7475 | 885.221 |
| 303.15 | 0.7954 | 901.919 |
| 303.15 | 0.8446 | 919.525 |
| 303.15 | 0.8917 | 936.846 |
| 303.15 | 0.9404 | 955.244 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Aniline, N-methyl- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0540 | 1164.13 |
| 293.15 | 0.1084 | 1177.21 |
| 293.15 | 0.1536 | 1188.4 |
| 293.15 | 0.2000 | 1199.96 |
| 293.15 | 0.2556 | 1214.55 |
| 293.15 | 0.2976 | 1226.12 |
| 293.15 | 0.3473 | 1240.59 |
| 293.15 | 0.3944 | 1255.22 |
| 293.15 | 0.4485 | 1273.49 |
| 293.15 | 0.4953 | 1290.98 |
| 293.15 | 0.5355 | 1306.87 |
| 293.15 | 0.5990 | 1334.98 |
| 293.15 | 0.6436 | 1356.59 |
| 293.15 | 0.7024 | 1387.65 |
| 293.15 | 0.7457 | 1412.52 |
| 293.15 | 0.7858 | 1436.65 |
| 293.15 | 0.8459 | 1474.73 |
| 293.15 | 0.8952 | 1507.91 |
| 293.15 | 0.9491 | 1545.53 |
| 298.15 | 0.0577 | 1143.9 |
| 298.15 | 0.1072 | 1156.24 |
| 298.15 | 0.1473 | 1166.33 |
| 298.15 | 0.2055 | 1181.37 |
| 298.15 | 0.2595 | 1193.92 |
| 298.15 | 0.3033 | 1208.28 |
| 298.15 | 0.3401 | 1219.16 |
| 298.15 | 0.3955 | 1236.72 |
| 298.15 | 0.4559 | 1257.57 |
| 298.15 | 0.5030 | 1275.48 |
| 298.15 | 0.5431 | 1291.9 |
| 298.15 | 0.5956 | 1315.3 |
| 298.15 | 0.6441 | 1338.79 |
| 298.15 | 0.6995 | 1368.11 |
| 298.15 | 0.7491 | 1396.25 |
| 298.15 | 0.7964 | 1425.14 |
| 298.15 | 0.8446 | 1455.89 |
| 298.15 | 0.8949 | 1489.57 |
| 298.15 | 0.9465 | 1525.56 |
| 303.15 | 0.0615 | 1124.94 |
| 303.15 | 0.1111 | 1137.53 |
| 303.15 | 0.1548 | 1148.81 |
| 303.15 | 0.2069 | 1162.57 |
| 303.15 | 0.2501 | 1174.36 |
| 303.15 | 0.2964 | 1187.49 |
| 303.15 | 0.3480 | 1203.16 |
| 303.15 | 0.3979 | 1219.16 |
| 303.15 | 0.4513 | 1238.04 |
| 303.15 | 0.5003 | 1256.55 |
| 303.15 | 0.5583 | 1280.79 |
| 303.15 | 0.5988 | 1299.21 |
| 303.15 | 0.6470 | 1322.6 |
| 303.15 | 0.7026 | 1351.94 |
| 303.15 | 0.7475 | 1377.44 |
| 303.15 | 0.7954 | 1406.27 |
| 303.15 | 0.8446 | 1437.49 |
| 303.15 | 0.8917 | 1468.76 |
| 303.15 | 0.9404 | 1502.43 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Aniline, N-methyl- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0540 | 1164.13 |
| 293.15 | 0.1084 | 1177.21 |
| 293.15 | 0.1536 | 1188.4 |
| 293.15 | 0.2000 | 1199.96 |
| 293.15 | 0.2556 | 1214.55 |
| 293.15 | 0.2976 | 1226.12 |
| 293.15 | 0.3473 | 1240.59 |
| 293.15 | 0.3944 | 1255.22 |
| 293.15 | 0.4485 | 1273.49 |
| 293.15 | 0.4953 | 1290.98 |
| 293.15 | 0.5355 | 1306.87 |
| 293.15 | 0.5990 | 1334.98 |
| 293.15 | 0.6436 | 1356.59 |
| 293.15 | 0.7024 | 1387.65 |
| 293.15 | 0.7457 | 1412.52 |
| 293.15 | 0.7858 | 1436.65 |
| 293.15 | 0.8459 | 1474.73 |
| 293.15 | 0.8952 | 1507.91 |
| 293.15 | 0.9491 | 1545.53 |
| 298.15 | 0.0577 | 1143.9 |
| 298.15 | 0.1072 | 1156.24 |
| 298.15 | 0.1473 | 1166.33 |
| 298.15 | 0.2055 | 1181.37 |
| 298.15 | 0.2595 | 1193.92 |
| 298.15 | 0.3033 | 1208.28 |
| 298.15 | 0.3401 | 1219.16 |
| 298.15 | 0.3955 | 1236.72 |
| 298.15 | 0.4559 | 1257.57 |
| 298.15 | 0.5030 | 1275.48 |
| 298.15 | 0.5431 | 1291.9 |
| 298.15 | 0.5956 | 1315.3 |
| 298.15 | 0.6441 | 1338.79 |
| 298.15 | 0.6995 | 1368.11 |
| 298.15 | 0.7491 | 1396.25 |
| 298.15 | 0.7964 | 1425.14 |
| 298.15 | 0.8446 | 1455.89 |
| 298.15 | 0.8949 | 1489.57 |
| 298.15 | 0.9465 | 1525.56 |
| 303.15 | 0.0615 | 1124.94 |
| 303.15 | 0.1111 | 1137.53 |
| 303.15 | 0.1548 | 1148.81 |
| 303.15 | 0.2069 | 1162.57 |
| 303.15 | 0.2501 | 1174.36 |
| 303.15 | 0.2964 | 1187.49 |
| 303.15 | 0.3480 | 1203.16 |
| 303.15 | 0.3979 | 1219.16 |
| 303.15 | 0.4513 | 1238.04 |
| 303.15 | 0.5003 | 1256.55 |
| 303.15 | 0.5583 | 1280.79 |
| 303.15 | 0.5988 | 1299.21 |
| 303.15 | 0.6470 | 1322.6 |
| 303.15 | 0.7026 | 1351.94 |
| 303.15 | 0.7475 | 1377.44 |
| 303.15 | 0.7954 | 1406.27 |
| 303.15 | 0.8446 | 1437.49 |
| 303.15 | 0.8917 | 1468.76 |
| 303.15 | 0.9404 | 1502.43 |
Sources
- Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
- Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems