Mixture of Aniline + 2-Butanone

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Aniline

Name
Aniline
InChI
InChI=1S/C6H7N/c7-6-4-2-1-3-5-6/h1-5H,7H2
InChI Key
PAYRUJLWNCNPSJ-UHFFFAOYSA-N
Formula
C6H7N
SMILES
Nc1ccccc1
Mol. Weight (g/mol)
93.13
CAS
62-53-3

2-Butanone

Name
2-Butanone
InChI
InChI=1S/C4H8O/c1-3-4(2)5/h3H2,1-2H3
InChI Key
ZWEHNKRNPOVVGH-UHFFFAOYSA-N
Formula
C4H8O
SMILES
CCC(C)=O
Mol. Weight (g/mol)
72.11
CAS
78-93-3
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ρl - Mass density, kg/m3 (2)
  3. csound,fluid - Speed of Sound, m/s (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of 2-Butanone (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1156 -0.3780
0.1565 -0.4990
0.2099 -0.6480
0.3121 -0.8790
0.4116 -1.075
0.5106 -1.173
0.6086 -1.171
0.7009 -1.071
0.8064 -0.8140
0.9018 -0.4690

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of 2-Butanone (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1156 -0.3780
0.1565 -0.4990
0.2099 -0.6480
0.3121 -0.8790
0.4116 -1.075
0.5106 -1.173
0.6086 -1.171
0.7009 -1.071
0.8064 -0.8140
0.9018 -0.4690

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0580 1011.292
293.15 0.1122 1001.344
293.15 0.1576 993.678
293.15 0.2052 985.068
293.15 0.2543 976.056
293.15 0.3043 966.42
293.15 0.3562 956.208
293.15 0.4059 946.279
293.15 0.4530 936.5
293.15 0.5048 925.617
293.15 0.5443 917.103
293.15 0.6120 902.143
293.15 0.6480 894.022
293.15 0.7044 880.787
293.15 0.7754 863.737
293.15 0.8081 855.598
293.15 0.8493 845.213
293.15 0.9027 831.249
293.15 0.9476 819.373
298.15 0.0560 1007.337
298.15 0.1188 997.647
298.15 0.1547 990.216
298.15 0.2038 981.189
298.15 0.2563 971.23
298.15 0.3064 961.559
298.15 0.3474 953.414
298.15 0.4089 940.989
298.15 0.4523 932.032
298.15 0.5026 921.385
298.15 0.5467 911.916
298.15 0.6019 899.666
298.15 0.6481 889.131
298.15 0.7048 875.989
298.15 0.7451 866.153
298.15 0.8030 851.853
298.15 0.8487 840.349
298.15 0.9019 826.554
298.15 0.9489 813.934
303.15 0.0582 1002.61
303.15 0.1097 993.104
303.15 0.1485 986.049
303.15 0.2050 975.667
303.15 0.2507 967.388
303.15 0.3064 956.964
303.15 0.3426 949.873
303.15 0.4140 935.434
303.15 0.4470 928.634
303.15 0.4910 919.218
303.15 0.5537 905.656
303.15 0.6044 894.417
303.15 0.6434 885.415
303.15 0.7038 871.181
303.15 0.7716 854.721
303.15 0.8079 845.614
303.15 0.8481 835.388
303.15 0.8988 822.096
303.15 0.9466 809.221

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0580 1011.292
293.15 0.1122 1001.344
293.15 0.1576 993.678
293.15 0.2052 985.068
293.15 0.2543 976.056
293.15 0.3043 966.42
293.15 0.3562 956.208
293.15 0.4059 946.279
293.15 0.4530 936.5
293.15 0.5048 925.617
293.15 0.5443 917.103
293.15 0.6120 902.143
293.15 0.6480 894.022
293.15 0.7044 880.787
293.15 0.7754 863.737
293.15 0.8081 855.598
293.15 0.8493 845.213
293.15 0.9027 831.249
293.15 0.9476 819.373
298.15 0.0560 1007.337
298.15 0.1188 997.647
298.15 0.1547 990.216
298.15 0.2038 981.189
298.15 0.2563 971.23
298.15 0.3064 961.559
298.15 0.3474 953.414
298.15 0.4089 940.989
298.15 0.4523 932.032
298.15 0.5026 921.385
298.15 0.5467 911.916
298.15 0.6019 899.666
298.15 0.6481 889.131
298.15 0.7048 875.989
298.15 0.7451 866.153
298.15 0.8030 851.853
298.15 0.8487 840.349
298.15 0.9019 826.554
298.15 0.9489 813.934
303.15 0.0582 1002.61
303.15 0.1097 993.104
303.15 0.1485 986.049
303.15 0.2050 975.667
303.15 0.2507 967.388
303.15 0.3064 956.964
303.15 0.3426 949.873
303.15 0.4140 935.434
303.15 0.4470 928.634
303.15 0.4910 919.218
303.15 0.5537 905.656
303.15 0.6044 894.417
303.15 0.6434 885.415
303.15 0.7038 871.181
303.15 0.7716 854.721
303.15 0.8079 845.614
303.15 0.8481 835.388
303.15 0.8988 822.096
303.15 0.9466 809.221

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Speed of sound, m/s - Liquid
293.15 0.0580 1633.73
293.15 0.1122 1612.22
293.15 0.1576 1594.71
293.15 0.2052 1576.01
293.15 0.2543 1556.68
293.15 0.3043 1536.62
293.15 0.3562 1515.48
293.15 0.4059 1495.18
293.15 0.4530 1475.25
293.15 0.5048 1453.16
293.15 0.5443 1435.84
293.15 0.6120 1405.44
293.15 0.6480 1388.95
293.15 0.7044 1362.11
293.15 0.7754 1328.59
293.15 0.8081 1311.28
293.15 0.8493 1290.46
293.15 0.9027 1262.94
293.15 0.9476 1239.59
298.15 0.0560 1615.43
298.15 0.1188 1593.59
298.15 0.1547 1576.89
298.15 0.2038 1557.51
298.15 0.2563 1536.46
298.15 0.3064 1516.35
298.15 0.3474 1499.63
298.15 0.4089 1474.12
298.15 0.4523 1455.79
298.15 0.5026 1434.14
298.15 0.5467 1414.88
298.15 0.6019 1390.03
298.15 0.6481 1368.49
298.15 0.7048 1341.93
298.15 0.7451 1322.03
298.15 0.8030 1293.23
298.15 0.8487 1270.14
298.15 0.9019 1242.8
298.15 0.9489 1218.03
303.15 0.0582 1596.11
303.15 0.1097 1575.62
303.15 0.1485 1560.26
303.15 0.2050 1537.97
303.15 0.2507 1520.34
303.15 0.3064 1497.88
303.15 0.3426 1482.95
303.15 0.4140 1453.33
303.15 0.4470 1439.45
303.15 0.4910 1420.26
303.15 0.5537 1392.66
303.15 0.6044 1369.77
303.15 0.6434 1351.53
303.15 0.7038 1322.64
303.15 0.7716 1289.42
303.15 0.8079 1271.08
303.15 0.8481 1250.64
303.15 0.8988 1224.22
303.15 0.9466 1199.01

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Speed of sound, m/s - Liquid
293.15 0.0580 1633.73
293.15 0.1122 1612.22
293.15 0.1576 1594.71
293.15 0.2052 1576.01
293.15 0.2543 1556.68
293.15 0.3043 1536.62
293.15 0.3562 1515.48
293.15 0.4059 1495.18
293.15 0.4530 1475.25
293.15 0.5048 1453.16
293.15 0.5443 1435.84
293.15 0.6120 1405.44
293.15 0.6480 1388.95
293.15 0.7044 1362.11
293.15 0.7754 1328.59
293.15 0.8081 1311.28
293.15 0.8493 1290.46
293.15 0.9027 1262.94
293.15 0.9476 1239.59
298.15 0.0560 1615.43
298.15 0.1188 1593.59
298.15 0.1547 1576.89
298.15 0.2038 1557.51
298.15 0.2563 1536.46
298.15 0.3064 1516.35
298.15 0.3474 1499.63
298.15 0.4089 1474.12
298.15 0.4523 1455.79
298.15 0.5026 1434.14
298.15 0.5467 1414.88
298.15 0.6019 1390.03
298.15 0.6481 1368.49
298.15 0.7048 1341.93
298.15 0.7451 1322.03
298.15 0.8030 1293.23
298.15 0.8487 1270.14
298.15 0.9019 1242.8
298.15 0.9489 1218.03
303.15 0.0582 1596.11
303.15 0.1097 1575.62
303.15 0.1485 1560.26
303.15 0.2050 1537.97
303.15 0.2507 1520.34
303.15 0.3064 1497.88
303.15 0.3426 1482.95
303.15 0.4140 1453.33
303.15 0.4470 1439.45
303.15 0.4910 1420.26
303.15 0.5537 1392.66
303.15 0.6044 1369.77
303.15 0.6434 1351.53
303.15 0.7038 1322.64
303.15 0.7716 1289.42
303.15 0.8079 1271.08
303.15 0.8481 1250.64
303.15 0.8988 1224.22
303.15 0.9466 1199.01

Sources