Mixture of 2-Butanone + 1-Propanamine, N-propyl-

Excel

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-Propanamine, N-propyl-

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
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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-Propanamine, N-propyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1042 0.1550
0.1978 0.2530
0.3016 0.3340
0.3852 0.3700
0.4950 0.3970
0.5459 0.3960
0.5908 0.3920
0.6833 0.3560
0.7647 0.2990
0.8559 0.2040

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

Operational conditions:

Mole fraction of 1-Propanamine, N-propyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1042 0.1550
0.1978 0.2530
0.3016 0.3340
0.3852 0.3700
0.4950 0.3970
0.5459 0.3960
0.5908 0.3920
0.6833 0.3560
0.7647 0.2990
0.8559 0.2040

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 0.0539 740.359
293.15 0.1021 742.443
293.15 0.1497 744.612
293.15 0.1982 746.936
293.15 0.2459 749.311
293.15 0.2983 752.034
293.15 0.3504 754.874
293.15 0.4012 757.757
293.15 0.4495 760.619
293.15 0.5068 764.2
293.15 0.5551 767.388
293.15 0.6014 770.563
293.15 0.6568 774.567
293.15 0.6968 777.603
293.15 0.7555 782.275
293.15 0.8009 786.111
293.15 0.8573 791.158
293.15 0.9010 795.276
293.15 0.9479 799.908
298.15 0.0592 736.042
298.15 0.1027 737.924
298.15 0.1509 740.108
298.15 0.2001 742.441
298.15 0.2446 744.623
298.15 0.2958 747.263
298.15 0.3545 750.41
298.15 0.4003 753.0
298.15 0.4625 756.591
298.15 0.5006 759.04
298.15 0.5539 762.376
298.15 0.5992 765.587
298.15 0.6474 769.011
298.15 0.6987 772.61
298.15 0.7531 777.151
298.15 0.8048 781.469
298.15 0.8557 785.991
298.15 0.9041 790.463
298.15 0.9471 794.714
303.15 0.0658 731.678
303.15 0.0988 733.107
303.15 0.1106 733.626
303.15 0.2146 738.432
303.15 0.2595 740.626
303.15 0.3098 743.197
303.15 0.3630 746.053
303.15 0.4131 748.859
303.15 0.4570 751.472
303.15 0.5154 755.069
303.15 0.5554 757.601
303.15 0.6081 761.161
303.15 0.6657 765.248
303.15 0.7041 768.129
303.15 0.7517 771.855
303.15 0.8032 776.094
303.15 0.8513 780.312
303.15 0.8958 784.355
303.15 0.9448 789.085

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 0.0539 740.359
293.15 0.1021 742.443
293.15 0.1497 744.612
293.15 0.1982 746.936
293.15 0.2459 749.311
293.15 0.2983 752.034
293.15 0.3504 754.874
293.15 0.4012 757.757
293.15 0.4495 760.619
293.15 0.5068 764.2
293.15 0.5551 767.388
293.15 0.6014 770.563
293.15 0.6568 774.567
293.15 0.6968 777.603
293.15 0.7555 782.275
293.15 0.8009 786.111
293.15 0.8573 791.158
293.15 0.9010 795.276
293.15 0.9479 799.908
298.15 0.0592 736.042
298.15 0.1027 737.924
298.15 0.1509 740.108
298.15 0.2001 742.441
298.15 0.2446 744.623
298.15 0.2958 747.263
298.15 0.3545 750.41
298.15 0.4003 753.0
298.15 0.4625 756.591
298.15 0.5006 759.04
298.15 0.5539 762.376
298.15 0.5992 765.587
298.15 0.6474 769.011
298.15 0.6987 772.61
298.15 0.7531 777.151
298.15 0.8048 781.469
298.15 0.8557 785.991
298.15 0.9041 790.463
298.15 0.9471 794.714
303.15 0.0658 731.678
303.15 0.0988 733.107
303.15 0.1106 733.626
303.15 0.2146 738.432
303.15 0.2595 740.626
303.15 0.3098 743.197
303.15 0.3630 746.053
303.15 0.4131 748.859
303.15 0.4570 751.472
303.15 0.5154 755.069
303.15 0.5554 757.601
303.15 0.6081 761.161
303.15 0.6657 765.248
303.15 0.7041 768.129
303.15 0.7517 771.855
303.15 0.8032 776.094
303.15 0.8513 780.312
303.15 0.8958 784.355
303.15 0.9448 789.085

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 0.0539 1208.02
293.15 0.1021 1207.27
293.15 0.1497 1206.7
293.15 0.1982 1206.17
293.15 0.2459 1205.69
293.15 0.2983 1205.17
293.15 0.3504 1204.86
293.15 0.4012 1204.58
293.15 0.4495 1204.35
293.15 0.5068 1204.3
293.15 0.5551 1204.38
293.15 0.6014 1204.49
293.15 0.6568 1204.76
293.15 0.6968 1205.12
293.15 0.7555 1205.87
293.15 0.8009 1206.59
293.15 0.8573 1207.83
293.15 0.9010 1208.9
293.15 0.9479 1210.29
298.15 0.0592 1186.64
298.15 0.1027 1185.88
298.15 0.1509 1185.19
298.15 0.2001 1184.66
298.15 0.2446 1184.17
298.15 0.2958 1183.84
298.15 0.3545 1183.33
298.15 0.4003 1183.16
298.15 0.4625 1182.49
298.15 0.5006 1182.88
298.15 0.5539 1182.71
298.15 0.5992 1183.16
298.15 0.6474 1183.43
298.15 0.6987 1183.49
298.15 0.7531 1184.56
298.15 0.8048 1185.36
298.15 0.8557 1186.62
298.15 0.9041 1188.02
298.15 0.9471 1189.12
303.15 0.0658 1165.92
303.15 0.0988 1165.4
303.15 0.1106 1165.23
303.15 0.2146 1164.09
303.15 0.2595 1163.49
303.15 0.3098 1163.09
303.15 0.3630 1162.78
303.15 0.4131 1162.5
303.15 0.4570 1162.37
303.15 0.5154 1162.3
303.15 0.5554 1162.39
303.15 0.6081 1162.63
303.15 0.6657 1163.01
303.15 0.7041 1163.52
303.15 0.7517 1163.99
303.15 0.8032 1164.84
303.15 0.8513 1166.07
303.15 0.8958 1166.99
303.15 0.9448 1168.6

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 0.0539 1208.02
293.15 0.1021 1207.27
293.15 0.1497 1206.7
293.15 0.1982 1206.17
293.15 0.2459 1205.69
293.15 0.2983 1205.17
293.15 0.3504 1204.86
293.15 0.4012 1204.58
293.15 0.4495 1204.35
293.15 0.5068 1204.3
293.15 0.5551 1204.38
293.15 0.6014 1204.49
293.15 0.6568 1204.76
293.15 0.6968 1205.12
293.15 0.7555 1205.87
293.15 0.8009 1206.59
293.15 0.8573 1207.83
293.15 0.9010 1208.9
293.15 0.9479 1210.29
298.15 0.0592 1186.64
298.15 0.1027 1185.88
298.15 0.1509 1185.19
298.15 0.2001 1184.66
298.15 0.2446 1184.17
298.15 0.2958 1183.84
298.15 0.3545 1183.33
298.15 0.4003 1183.16
298.15 0.4625 1182.49
298.15 0.5006 1182.88
298.15 0.5539 1182.71
298.15 0.5992 1183.16
298.15 0.6474 1183.43
298.15 0.6987 1183.49
298.15 0.7531 1184.56
298.15 0.8048 1185.36
298.15 0.8557 1186.62
298.15 0.9041 1188.02
298.15 0.9471 1189.12
303.15 0.0658 1165.92
303.15 0.0988 1165.4
303.15 0.1106 1165.23
303.15 0.2146 1164.09
303.15 0.2595 1163.49
303.15 0.3098 1163.09
303.15 0.3630 1162.78
303.15 0.4131 1162.5
303.15 0.4570 1162.37
303.15 0.5154 1162.3
303.15 0.5554 1162.39
303.15 0.6081 1162.63
303.15 0.6657 1163.01
303.15 0.7041 1163.52
303.15 0.7517 1163.99
303.15 0.8032 1164.84
303.15 0.8513 1166.07
303.15 0.8958 1166.99
303.15 0.9448 1168.6

Sources