Mixture of 2-Butanone + 1-Butanamine, N-butyl-

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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

1-Butanamine, N-butyl-

Name
1-Butanamine, N-butyl-
InChI
InChI=1S/C8H19N/c1-3-5-7-9-8-6-4-2/h9H,3-8H2,1-2H3
InChI Key
JQVDAXLFBXTEQA-UHFFFAOYSA-N
Formula
C8H19N
SMILES
CCCCNCCCC
Mol. Weight (g/mol)
129.24
CAS
111-92-2
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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 1-Butanamine, N-butyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1142 0.2740
0.2078 0.4250
0.2985 0.5360
0.3978 0.6010
0.4956 0.6190
0.6001 0.5930
0.6930 0.5290
0.7846 0.4170
0.8802 0.2700

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

Operational conditions:

Mole fraction of 1-Butanamine, N-butyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1142 0.2740
0.2078 0.4250
0.2985 0.5360
0.3978 0.6010
0.4956 0.6190
0.6001 0.5930
0.6930 0.5290
0.7846 0.4170
0.8802 0.2700

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0568 760.739
293.15 0.1152 762.014
293.15 0.1488 762.814
293.15 0.1968 764.024
293.15 0.2539 765.57
293.15 0.3056 767.093
293.15 0.3564 768.675
293.15 0.4105 770.501
293.15 0.4545 772.103
293.15 0.5005 773.872
293.15 0.5553 776.145
293.15 0.6022 778.277
293.15 0.6554 780.87
293.15 0.7036 783.444
293.15 0.7554 786.435
293.15 0.8022 789.404
293.15 0.8598 793.411
293.15 0.9001 796.544
293.15 0.9513 800.881
298.15 0.0681 756.775
298.15 0.1038 757.539
298.15 0.1625 758.95
298.15 0.2034 759.972
298.15 0.2603 761.475
298.15 0.3112 762.929
298.15 0.3523 764.175
298.15 0.3937 765.506
298.15 0.4420 767.105
298.15 0.5018 769.396
298.15 0.5455 771.147
298.15 0.6036 773.698
298.15 0.6514 775.963
298.15 0.7003 778.472
298.15 0.7473 781.05
298.15 0.7978 784.142
298.15 0.8456 787.356
298.15 0.9022 791.581
298.15 0.9482 795.385
303.15 0.0621 752.548
303.15 0.1098 753.539
303.15 0.1666 754.759
303.15 0.2074 755.736
303.15 0.2593 757.08
303.15 0.3090 758.454
303.15 0.3551 759.79
303.15 0.4045 761.368
303.15 0.4566 763.133
303.15 0.4957 764.551
303.15 0.5402 766.282
303.15 0.6005 768.842
303.15 0.6493 771.091
303.15 0.7004 773.646
303.15 0.7486 776.288
303.15 0.8005 779.398
303.15 0.8456 782.362
303.15 0.8990 786.254
303.15 0.9530 790.578

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0568 760.739
293.15 0.1152 762.014
293.15 0.1488 762.814
293.15 0.1968 764.024
293.15 0.2539 765.57
293.15 0.3056 767.093
293.15 0.3564 768.675
293.15 0.4105 770.501
293.15 0.4545 772.103
293.15 0.5005 773.872
293.15 0.5553 776.145
293.15 0.6022 778.277
293.15 0.6554 780.87
293.15 0.7036 783.444
293.15 0.7554 786.435
293.15 0.8022 789.404
293.15 0.8598 793.411
293.15 0.9001 796.544
293.15 0.9513 800.881
298.15 0.0681 756.775
298.15 0.1038 757.539
298.15 0.1625 758.95
298.15 0.2034 759.972
298.15 0.2603 761.475
298.15 0.3112 762.929
298.15 0.3523 764.175
298.15 0.3937 765.506
298.15 0.4420 767.105
298.15 0.5018 769.396
298.15 0.5455 771.147
298.15 0.6036 773.698
298.15 0.6514 775.963
298.15 0.7003 778.472
298.15 0.7473 781.05
298.15 0.7978 784.142
298.15 0.8456 787.356
298.15 0.9022 791.581
298.15 0.9482 795.385
303.15 0.0621 752.548
303.15 0.1098 753.539
303.15 0.1666 754.759
303.15 0.2074 755.736
303.15 0.2593 757.08
303.15 0.3090 758.454
303.15 0.3551 759.79
303.15 0.4045 761.368
303.15 0.4566 763.133
303.15 0.4957 764.551
303.15 0.5402 766.282
303.15 0.6005 768.842
303.15 0.6493 771.091
303.15 0.7004 773.646
303.15 0.7486 776.288
303.15 0.8005 779.398
303.15 0.8456 782.362
303.15 0.8990 786.254
303.15 0.9530 790.578

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0568 1258.16
293.15 0.1152 1254.96
293.15 0.1488 1252.9
293.15 0.1968 1250.3
293.15 0.2539 1247.19
293.15 0.3056 1244.42
293.15 0.3564 1241.62
293.15 0.4105 1238.72
293.15 0.4545 1236.36
293.15 0.5005 1233.96
293.15 0.5553 1231.06
293.15 0.6022 1228.89
293.15 0.6554 1225.75
293.15 0.7036 1223.35
293.15 0.7554 1220.79
293.15 0.8022 1218.72
293.15 0.8598 1216.34
293.15 0.9001 1214.96
293.15 0.9513 1213.5
298.15 0.0681 1237.35
298.15 0.1038 1235.31
298.15 0.1625 1232.05
298.15 0.2034 1229.94
298.15 0.2603 1226.66
298.15 0.3112 1223.83
298.15 0.3523 1221.6
298.15 0.3937 1219.44
298.15 0.4420 1216.58
298.15 0.5018 1213.32
298.15 0.5455 1211.0
298.15 0.6036 1207.71
298.15 0.6514 1205.23
298.15 0.7003 1202.7
298.15 0.7473 1200.27
298.15 0.7978 1197.91
298.15 0.8456 1195.86
298.15 0.9022 1193.73
298.15 0.9482 1192.26
303.15 0.0621 1218.87
303.15 0.1098 1216.11
303.15 0.1666 1212.59
303.15 0.2074 1210.29
303.15 0.2593 1207.25
303.15 0.3090 1204.69
303.15 0.3551 1201.97
303.15 0.4045 1199.3
303.15 0.4566 1196.39
303.15 0.4957 1194.07
303.15 0.5402 1191.57
303.15 0.6005 1188.2
303.15 0.6493 1185.58
303.15 0.7004 1182.87
303.15 0.7486 1180.45
303.15 0.8005 1177.89
303.15 0.8456 1175.94
303.15 0.8990 1173.7
303.15 0.9530 1171.96

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0568 1258.16
293.15 0.1152 1254.96
293.15 0.1488 1252.9
293.15 0.1968 1250.3
293.15 0.2539 1247.19
293.15 0.3056 1244.42
293.15 0.3564 1241.62
293.15 0.4105 1238.72
293.15 0.4545 1236.36
293.15 0.5005 1233.96
293.15 0.5553 1231.06
293.15 0.6022 1228.89
293.15 0.6554 1225.75
293.15 0.7036 1223.35
293.15 0.7554 1220.79
293.15 0.8022 1218.72
293.15 0.8598 1216.34
293.15 0.9001 1214.96
293.15 0.9513 1213.5
298.15 0.0681 1237.35
298.15 0.1038 1235.31
298.15 0.1625 1232.05
298.15 0.2034 1229.94
298.15 0.2603 1226.66
298.15 0.3112 1223.83
298.15 0.3523 1221.6
298.15 0.3937 1219.44
298.15 0.4420 1216.58
298.15 0.5018 1213.32
298.15 0.5455 1211.0
298.15 0.6036 1207.71
298.15 0.6514 1205.23
298.15 0.7003 1202.7
298.15 0.7473 1200.27
298.15 0.7978 1197.91
298.15 0.8456 1195.86
298.15 0.9022 1193.73
298.15 0.9482 1192.26
303.15 0.0621 1218.87
303.15 0.1098 1216.11
303.15 0.1666 1212.59
303.15 0.2074 1210.29
303.15 0.2593 1207.25
303.15 0.3090 1204.69
303.15 0.3551 1201.97
303.15 0.4045 1199.3
303.15 0.4566 1196.39
303.15 0.4957 1194.07
303.15 0.5402 1191.57
303.15 0.6005 1188.2
303.15 0.6493 1185.58
303.15 0.7004 1182.87
303.15 0.7486 1180.45
303.15 0.8005 1177.89
303.15 0.8456 1175.94
303.15 0.8990 1173.7
303.15 0.9530 1171.96

Sources