Mixture of Triethylamine + 2-Heptanone

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Triethylamine

Name
Triethylamine
InChI
InChI=1S/C6H15N/c1-4-7(5-2)6-3/h4-6H2,1-3H3
InChI Key
ZMANZCXQSJIPKH-UHFFFAOYSA-N
Formula
C6H15N
SMILES
CCN(CC)CC
Mol. Weight (g/mol)
101.19
CAS
121-44-8

2-Heptanone

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
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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)
  4. Excess molar volume, m3/mol (2)

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

Operational conditions:

Mole fraction of Triethylamine (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1292 0.1190
0.2196 0.2160
0.3104 0.2910
0.4092 0.3740
0.5080 0.4190
0.5973 0.4320
0.7061 0.4120
0.8014 0.3440
0.8954 0.2310

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

Operational conditions:

Mole fraction of Triethylamine (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1292 0.1190
0.2196 0.2160
0.3104 0.2910
0.4092 0.3740
0.5080 0.4190
0.5973 0.4320
0.7061 0.4120
0.8014 0.3440
0.8954 0.2310

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 0.0636 733.182
293.15 0.1061 737.185
293.15 0.1585 741.934
293.15 0.2077 746.426
293.15 0.2536 750.6
293.15 0.3091 755.621
293.15 0.3614 760.322
293.15 0.4043 764.18
293.15 0.4621 769.325
293.15 0.5022 772.887
293.15 0.5577 777.79
293.15 0.6078 782.199
293.15 0.6604 786.734
293.15 0.7001 790.167
293.15 0.7490 794.387
293.15 0.7968 798.46
293.15 0.8517 803.051
293.15 0.9008 807.18
293.15 0.9507 811.366
298.15 0.0574 727.994
298.15 0.1050 732.47
298.15 0.1619 737.667
298.15 0.2068 741.77
298.15 0.2598 746.582
298.15 0.3075 750.925
298.15 0.3578 755.443
298.15 0.4081 759.984
298.15 0.4548 764.166
298.15 0.5032 768.476
298.15 0.5545 773.017
298.15 0.6103 777.928
298.15 0.6579 782.088
298.15 0.6994 785.697
298.15 0.7484 789.941
298.15 0.8031 794.633
298.15 0.8576 799.228
298.15 0.9014 802.909
298.15 0.9462 806.662
303.15 0.0612 723.838
303.15 0.1056 727.95
303.15 0.1602 732.935
303.15 0.2068 737.166
303.15 0.2606 742.09
303.15 0.3086 746.453
303.15 0.3583 750.968
303.15 0.4082 755.492
303.15 0.4553 759.737
303.15 0.5042 764.098
303.15 0.5983 772.43
303.15 0.6536 777.279
303.15 0.7031 781.622
303.15 0.7452 785.267
303.15 0.8088 790.717
303.15 0.8489 794.102
303.15 0.9007 798.491
303.15 0.9503 802.71

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 0.0636 733.182
293.15 0.1061 737.185
293.15 0.1585 741.934
293.15 0.2077 746.426
293.15 0.2536 750.6
293.15 0.3091 755.621
293.15 0.3614 760.322
293.15 0.4043 764.18
293.15 0.4621 769.325
293.15 0.5022 772.887
293.15 0.5577 777.79
293.15 0.6078 782.199
293.15 0.6604 786.734
293.15 0.7001 790.167
293.15 0.7490 794.387
293.15 0.7968 798.46
293.15 0.8517 803.051
293.15 0.9008 807.18
293.15 0.9507 811.366
298.15 0.0574 727.994
298.15 0.1050 732.47
298.15 0.1619 737.667
298.15 0.2068 741.77
298.15 0.2598 746.582
298.15 0.3075 750.925
298.15 0.3578 755.443
298.15 0.4081 759.984
298.15 0.4548 764.166
298.15 0.5032 768.476
298.15 0.5545 773.017
298.15 0.6103 777.928
298.15 0.6579 782.088
298.15 0.6994 785.697
298.15 0.7484 789.941
298.15 0.8031 794.633
298.15 0.8576 799.228
298.15 0.9014 802.909
298.15 0.9462 806.662
303.15 0.0612 723.838
303.15 0.1056 727.95
303.15 0.1602 732.935
303.15 0.2068 737.166
303.15 0.2606 742.09
303.15 0.3086 746.453
303.15 0.3583 750.968
303.15 0.4082 755.492
303.15 0.4553 759.737
303.15 0.5042 764.098
303.15 0.5983 772.43
303.15 0.6536 777.279
303.15 0.7031 781.622
303.15 0.7452 785.267
303.15 0.8088 790.717
303.15 0.8489 794.102
303.15 0.9007 798.491
303.15 0.9503 802.71

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 0.0636 1141.82
293.15 0.1061 1148.36
293.15 0.1585 1156.04
293.15 0.2077 1163.48
293.15 0.2536 1170.37
293.15 0.3091 1178.72
293.15 0.3614 1186.62
293.15 0.4043 1193.12
293.15 0.4621 1201.88
293.15 0.5022 1207.95
293.15 0.5577 1216.29
293.15 0.6078 1223.91
293.15 0.6604 1231.78
293.15 0.7001 1237.75
293.15 0.7490 1245.02
293.15 0.7968 1252.12
293.15 0.8517 1260.17
293.15 0.9008 1267.35
293.15 0.9507 1274.72
298.15 0.0574 1119.42
298.15 0.1050 1126.78
298.15 0.1619 1135.49
298.15 0.2068 1142.09
298.15 0.2598 1150.17
298.15 0.3075 1157.5
298.15 0.3578 1165.15
298.15 0.4081 1172.91
298.15 0.4548 1180.07
298.15 0.5032 1187.47
298.15 0.5545 1195.38
298.15 0.6103 1203.98
298.15 0.6579 1211.26
298.15 0.6994 1217.6
298.15 0.7484 1225.06
298.15 0.8031 1233.32
298.15 0.8576 1241.45
298.15 0.9014 1247.94
298.15 0.9462 1254.58
303.15 0.0612 1100.07
303.15 0.1056 1106.84
303.15 0.1602 1115.12
303.15 0.2068 1122.19
303.15 0.2606 1130.5
303.15 0.3086 1137.9
303.15 0.3583 1145.66
303.15 0.4082 1153.49
303.15 0.4553 1160.83
303.15 0.5042 1168.43
303.15 0.5983 1183.08
303.15 0.6536 1191.63
303.15 0.7031 1199.29
303.15 0.7452 1205.85
303.15 0.8088 1215.49
303.15 0.8489 1221.55
303.15 0.9007 1229.24
303.15 0.9503 1235.84

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 0.0636 1141.82
293.15 0.1061 1148.36
293.15 0.1585 1156.04
293.15 0.2077 1163.48
293.15 0.2536 1170.37
293.15 0.3091 1178.72
293.15 0.3614 1186.62
293.15 0.4043 1193.12
293.15 0.4621 1201.88
293.15 0.5022 1207.95
293.15 0.5577 1216.29
293.15 0.6078 1223.91
293.15 0.6604 1231.78
293.15 0.7001 1237.75
293.15 0.7490 1245.02
293.15 0.7968 1252.12
293.15 0.8517 1260.17
293.15 0.9008 1267.35
293.15 0.9507 1274.72
298.15 0.0574 1119.42
298.15 0.1050 1126.78
298.15 0.1619 1135.49
298.15 0.2068 1142.09
298.15 0.2598 1150.17
298.15 0.3075 1157.5
298.15 0.3578 1165.15
298.15 0.4081 1172.91
298.15 0.4548 1180.07
298.15 0.5032 1187.47
298.15 0.5545 1195.38
298.15 0.6103 1203.98
298.15 0.6579 1211.26
298.15 0.6994 1217.6
298.15 0.7484 1225.06
298.15 0.8031 1233.32
298.15 0.8576 1241.45
298.15 0.9014 1247.94
298.15 0.9462 1254.58
303.15 0.0612 1100.07
303.15 0.1056 1106.84
303.15 0.1602 1115.12
303.15 0.2068 1122.19
303.15 0.2606 1130.5
303.15 0.3086 1137.9
303.15 0.3583 1145.66
303.15 0.4082 1153.49
303.15 0.4553 1160.83
303.15 0.5042 1168.43
303.15 0.5983 1183.08
303.15 0.6536 1191.63
303.15 0.7031 1199.29
303.15 0.7452 1205.85
303.15 0.8088 1215.49
303.15 0.8489 1221.55
303.15 0.9007 1229.24
303.15 0.9503 1235.84

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 0.0636 -4.0900e-08
293.15 0.1061 -8.5400e-08
293.15 0.1585 -1.0640e-07
293.15 0.2077 -1.3210e-07
293.15 0.2536 -1.5240e-07
293.15 0.3091 -1.7370e-07
293.15 0.3614 -1.8840e-07
293.15 0.4043 -1.9980e-07
293.15 0.4621 -2.0870e-07
293.15 0.5022 -2.1270e-07
293.15 0.5577 -2.1460e-07
293.15 0.6078 -2.1280e-07
293.15 0.6604 -1.9700e-07
293.15 0.7001 -1.8630e-07
293.15 0.7490 -1.7140e-07
293.15 0.7968 -1.4860e-07
293.15 0.8517 -1.0930e-07
293.15 0.9008 -7.8200e-08
293.15 0.9507 -4.6900e-08
298.15 0.0574 -3.2200e-08
298.15 0.1050 -7.9800e-08
298.15 0.1619 -1.0700e-07
298.15 0.2068 -1.2960e-07
298.15 0.2598 -1.4950e-07
298.15 0.3075 -1.7040e-07
298.15 0.3578 -1.8210e-07
298.15 0.4081 -1.9630e-07
298.15 0.4548 -2.0450e-07
298.15 0.5032 -2.0920e-07
298.15 0.5545 -2.0930e-07
298.15 0.6103 -2.0570e-07
298.15 0.6579 -1.9670e-07
298.15 0.6994 -1.8740e-07
298.15 0.7484 -1.7280e-07
298.15 0.8031 -1.4950e-07
298.15 0.8576 -1.1130e-07
298.15 0.9014 -8.1000e-08
298.15 0.9462 -4.7100e-08
303.15 0.0612 -5.6300e-08
303.15 0.1056 -8.7800e-08
303.15 0.1602 -1.0940e-07
303.15 0.2068 -1.2630e-07
303.15 0.2606 -1.5110e-07
303.15 0.3086 -1.6800e-07
303.15 0.3583 -1.8600e-07
303.15 0.4082 -2.0160e-07
303.15 0.4553 -2.1190e-07
303.15 0.5042 -2.1440e-07
303.15 0.5983 -2.0870e-07
303.15 0.6536 -1.9840e-07
303.15 0.7031 -1.8860e-07
303.15 0.7452 -1.7270e-07
303.15 0.8088 -1.3900e-07
303.15 0.8489 -1.0970e-07
303.15 0.9007 -7.3800e-08
303.15 0.9503 -4.4400e-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 0.0636 -4.0900e-08
293.15 0.1061 -8.5400e-08
293.15 0.1585 -1.0640e-07
293.15 0.2077 -1.3210e-07
293.15 0.2536 -1.5240e-07
293.15 0.3091 -1.7370e-07
293.15 0.3614 -1.8840e-07
293.15 0.4043 -1.9980e-07
293.15 0.4621 -2.0870e-07
293.15 0.5022 -2.1270e-07
293.15 0.5577 -2.1460e-07
293.15 0.6078 -2.1280e-07
293.15 0.6604 -1.9700e-07
293.15 0.7001 -1.8630e-07
293.15 0.7490 -1.7140e-07
293.15 0.7968 -1.4860e-07
293.15 0.8517 -1.0930e-07
293.15 0.9008 -7.8200e-08
293.15 0.9507 -4.6900e-08
298.15 0.0574 -3.2200e-08
298.15 0.1050 -7.9800e-08
298.15 0.1619 -1.0700e-07
298.15 0.2068 -1.2960e-07
298.15 0.2598 -1.4950e-07
298.15 0.3075 -1.7040e-07
298.15 0.3578 -1.8210e-07
298.15 0.4081 -1.9630e-07
298.15 0.4548 -2.0450e-07
298.15 0.5032 -2.0920e-07
298.15 0.5545 -2.0930e-07
298.15 0.6103 -2.0570e-07
298.15 0.6579 -1.9670e-07
298.15 0.6994 -1.8740e-07
298.15 0.7484 -1.7280e-07
298.15 0.8031 -1.4950e-07
298.15 0.8576 -1.1130e-07
298.15 0.9014 -8.1000e-08
298.15 0.9462 -4.7100e-08
303.15 0.0612 -5.6300e-08
303.15 0.1056 -8.7800e-08
303.15 0.1602 -1.0940e-07
303.15 0.2068 -1.2630e-07
303.15 0.2606 -1.5110e-07
303.15 0.3086 -1.6800e-07
303.15 0.3583 -1.8600e-07
303.15 0.4082 -2.0160e-07
303.15 0.4553 -2.1190e-07
303.15 0.5042 -2.1440e-07
303.15 0.5983 -2.0870e-07
303.15 0.6536 -1.9840e-07
303.15 0.7031 -1.8860e-07
303.15 0.7452 -1.7270e-07
303.15 0.8088 -1.3900e-07
303.15 0.8489 -1.0970e-07
303.15 0.9007 -7.3800e-08
303.15 0.9503 -4.4400e-08

Sources