Mixture of Tributylamine + Diethylene glycol hexyl ether

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Tributylamine

Name
Tributylamine
InChI
InChI=1S/C12H27N/c1-4-7-10-13(11-8-5-2)12-9-6-3/h4-12H2,1-3H3
InChI Key
IMFACGCPASFAPR-UHFFFAOYSA-N
Formula
C12H27N
SMILES
CCCCN(CCCC)CCCC
Mol. Weight (g/mol)
185.35
CAS
102-82-9

Diethylene glycol hexyl ether

Name
Diethylene glycol hexyl ether
InChI
InChI=1S/C10H22O3/c1-2-3-4-5-7-12-9-10-13-8-6-11/h11H,2-10H2,1H3
InChI Key
GZMAAYIALGURDQ-UHFFFAOYSA-N
Formula
C10H22O3
SMILES
CCCCCCOCCOCCO
Mol. Weight (g/mol)
190.28
CAS
112-59-4
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Datasets

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

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.1168 288.15 797.427
0.1168 293.15 793.696
0.1168 298.15 789.759
0.1168 303.15 785.812
0.1168 308.15 782.055
0.1659 288.15 804.49
0.1659 293.15 800.716
0.1659 298.15 796.756
0.1659 303.15 792.8
0.1659 308.15 788.975
0.2092 288.15 810.815
0.2092 293.15 806.993
0.2092 298.15 803.027
0.2092 303.15 799.078
0.2092 308.15 795.2
0.2589 288.15 818.158
0.2589 293.15 814.291
0.2589 298.15 810.334
0.2589 303.15 806.371
0.2589 308.15 802.458
0.3155 288.15 826.596
0.3155 293.15 822.69
0.3155 298.15 818.738
0.3155 303.15 814.795
0.3155 308.15 810.825
0.3564 288.15 832.755
0.3564 293.15 828.829
0.3564 298.15 824.867
0.3564 303.15 820.924
0.3564 308.15 816.944
0.3830 288.15 836.791
0.3830 293.15 832.842
0.3830 298.15 828.881
0.3830 303.15 824.93
0.3830 308.15 820.957
0.4544 288.15 847.683
0.4544 293.15 843.729
0.4544 298.15 839.761
0.4544 303.15 835.783
0.4544 308.15 831.821
0.5108 288.15 856.418
0.5108 293.15 852.463
0.5108 298.15 848.467
0.5108 303.15 844.479
0.5108 308.15 840.528
0.5568 288.15 863.63
0.5568 293.15 859.691
0.5568 298.15 855.668
0.5568 303.15 851.665
0.5568 308.15 847.701
0.6107 288.15 872.206
0.6107 293.15 868.299
0.6107 298.15 864.217
0.6107 303.15 860.198
0.6107 308.15 856.228
0.6683 288.15 881.543
0.6683 293.15 877.641
0.6683 298.15 873.531
0.6683 303.15 869.475
0.6683 308.15 865.486
0.6924 288.15 885.505
0.6924 293.15 881.587
0.6924 298.15 877.468
0.6924 303.15 873.41
0.6924 308.15 869.396
0.7544 288.15 895.808
0.7544 293.15 891.893
0.7544 298.15 887.746
0.7544 303.15 883.674
0.7544 308.15 879.592
0.7963 288.15 902.873
0.7963 293.15 898.935
0.7963 298.15 894.791
0.7963 303.15 890.73
0.7963 308.15 886.574
0.8580 288.15 913.335
0.8580 293.15 909.366
0.8580 298.15 905.245
0.8580 303.15 901.206
0.8580 308.15 896.983
0.9079 288.15 921.784
0.9079 293.15 917.773
0.9079 298.15 913.7
0.9079 303.15 909.674
0.9079 308.15 905.434
0.9553 288.15 929.676
0.9553 293.15 925.674
0.9553 298.15 921.63
0.9553 303.15 917.622
0.9553 308.15 913.46

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.1168 288.15 797.427
0.1168 293.15 793.696
0.1168 298.15 789.759
0.1168 303.15 785.812
0.1168 308.15 782.055
0.1659 288.15 804.49
0.1659 293.15 800.716
0.1659 298.15 796.756
0.1659 303.15 792.8
0.1659 308.15 788.975
0.2092 288.15 810.815
0.2092 293.15 806.993
0.2092 298.15 803.027
0.2092 303.15 799.078
0.2092 308.15 795.2
0.2589 288.15 818.158
0.2589 293.15 814.291
0.2589 298.15 810.334
0.2589 303.15 806.371
0.2589 308.15 802.458
0.3155 288.15 826.596
0.3155 293.15 822.69
0.3155 298.15 818.738
0.3155 303.15 814.795
0.3155 308.15 810.825
0.3564 288.15 832.755
0.3564 293.15 828.829
0.3564 298.15 824.867
0.3564 303.15 820.924
0.3564 308.15 816.944
0.3830 288.15 836.791
0.3830 293.15 832.842
0.3830 298.15 828.881
0.3830 303.15 824.93
0.3830 308.15 820.957
0.4544 288.15 847.683
0.4544 293.15 843.729
0.4544 298.15 839.761
0.4544 303.15 835.783
0.4544 308.15 831.821
0.5108 288.15 856.418
0.5108 293.15 852.463
0.5108 298.15 848.467
0.5108 303.15 844.479
0.5108 308.15 840.528
0.5568 288.15 863.63
0.5568 293.15 859.691
0.5568 298.15 855.668
0.5568 303.15 851.665
0.5568 308.15 847.701
0.6107 288.15 872.206
0.6107 293.15 868.299
0.6107 298.15 864.217
0.6107 303.15 860.198
0.6107 308.15 856.228
0.6683 288.15 881.543
0.6683 293.15 877.641
0.6683 298.15 873.531
0.6683 303.15 869.475
0.6683 308.15 865.486
0.6924 288.15 885.505
0.6924 293.15 881.587
0.6924 298.15 877.468
0.6924 303.15 873.41
0.6924 308.15 869.396
0.7544 288.15 895.808
0.7544 293.15 891.893
0.7544 298.15 887.746
0.7544 303.15 883.674
0.7544 308.15 879.592
0.7963 288.15 902.873
0.7963 293.15 898.935
0.7963 298.15 894.791
0.7963 303.15 890.73
0.7963 308.15 886.574
0.8580 288.15 913.335
0.8580 293.15 909.366
0.8580 298.15 905.245
0.8580 303.15 901.206
0.8580 308.15 896.983
0.9079 288.15 921.784
0.9079 293.15 917.773
0.9079 298.15 913.7
0.9079 303.15 909.674
0.9079 308.15 905.434
0.9553 288.15 929.676
0.9553 293.15 925.674
0.9553 298.15 921.63
0.9553 303.15 917.622
0.9553 308.15 913.46

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
0.1168 288.15 1294.0
0.1168 293.15 1274.86
0.1168 298.15 1255.97
0.1168 303.15 1237.35
0.1168 308.15 1219.04
0.1659 288.15 1298.17
0.1659 293.15 1279.15
0.1659 298.15 1260.3
0.1659 303.15 1241.7
0.1659 308.15 1223.38
0.2092 288.15 1302.06
0.2092 293.15 1283.1
0.2092 298.15 1264.34
0.2092 303.15 1245.84
0.2092 308.15 1227.47
0.2589 288.15 1306.8
0.2589 293.15 1287.92
0.2589 298.15 1269.25
0.2589 303.15 1250.78
0.2589 308.15 1232.48
0.3155 288.15 1312.56
0.3155 293.15 1293.77
0.3155 298.15 1275.16
0.3155 303.15 1256.82
0.3155 308.15 1238.57
0.3564 288.15 1316.92
0.3564 293.15 1298.2
0.3564 298.15 1279.68
0.3564 303.15 1261.41
0.3564 308.15 1243.23
0.3830 288.15 1319.83
0.3830 293.15 1301.19
0.3830 298.15 1282.7
0.3830 303.15 1264.51
0.3830 308.15 1246.36
0.4544 288.15 1328.05
0.4544 293.15 1309.53
0.4544 298.15 1291.2
0.4544 303.15 1273.2
0.4544 308.15 1255.19
0.5108 288.15 1334.89
0.5108 293.15 1316.53
0.5108 298.15 1298.27
0.5108 303.15 1280.4
0.5108 308.15 1262.57
0.5568 288.15 1340.69
0.5568 293.15 1322.44
0.5568 298.15 1304.29
0.5568 303.15 1286.52
0.5568 308.15 1268.83
0.6107 288.15 1347.74
0.6107 293.15 1329.59
0.6107 298.15 1311.58
0.6107 303.15 1293.98
0.6107 308.15 1276.38
0.6683 288.15 1355.56
0.6683 293.15 1337.54
0.6683 298.15 1319.68
0.6683 303.15 1302.25
0.6683 308.15 1284.77
0.6924 288.15 1358.91
0.6924 293.15 1340.94
0.6924 298.15 1323.16
0.6924 303.15 1305.8
0.6924 308.15 1288.36
0.7544 288.15 1367.76
0.7544 293.15 1349.97
0.7544 298.15 1332.33
0.7544 303.15 1315.15
0.7544 308.15 1297.81
0.7963 288.15 1373.92
0.7963 293.15 1356.22
0.7963 298.15 1338.74
0.7963 303.15 1321.64
0.7963 308.15 1304.36
0.8580 288.15 1383.21
0.8580 293.15 1365.72
0.8580 298.15 1348.35
0.8580 303.15 1331.46
0.8580 308.15 1314.21
0.9079 288.15 1390.94
0.9079 293.15 1373.58
0.9079 298.15 1356.38
0.9079 303.15 1339.62
0.9079 308.15 1322.35
0.9553 288.15 1398.43
0.9553 293.15 1381.26
0.9553 298.15 1364.2
0.9553 303.15 1347.56
0.9553 308.15 1330.18

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
0.1168 288.15 1294.0
0.1168 293.15 1274.86
0.1168 298.15 1255.97
0.1168 303.15 1237.35
0.1168 308.15 1219.04
0.1659 288.15 1298.17
0.1659 293.15 1279.15
0.1659 298.15 1260.3
0.1659 303.15 1241.7
0.1659 308.15 1223.38
0.2092 288.15 1302.06
0.2092 293.15 1283.1
0.2092 298.15 1264.34
0.2092 303.15 1245.84
0.2092 308.15 1227.47
0.2589 288.15 1306.8
0.2589 293.15 1287.92
0.2589 298.15 1269.25
0.2589 303.15 1250.78
0.2589 308.15 1232.48
0.3155 288.15 1312.56
0.3155 293.15 1293.77
0.3155 298.15 1275.16
0.3155 303.15 1256.82
0.3155 308.15 1238.57
0.3564 288.15 1316.92
0.3564 293.15 1298.2
0.3564 298.15 1279.68
0.3564 303.15 1261.41
0.3564 308.15 1243.23
0.3830 288.15 1319.83
0.3830 293.15 1301.19
0.3830 298.15 1282.7
0.3830 303.15 1264.51
0.3830 308.15 1246.36
0.4544 288.15 1328.05
0.4544 293.15 1309.53
0.4544 298.15 1291.2
0.4544 303.15 1273.2
0.4544 308.15 1255.19
0.5108 288.15 1334.89
0.5108 293.15 1316.53
0.5108 298.15 1298.27
0.5108 303.15 1280.4
0.5108 308.15 1262.57
0.5568 288.15 1340.69
0.5568 293.15 1322.44
0.5568 298.15 1304.29
0.5568 303.15 1286.52
0.5568 308.15 1268.83
0.6107 288.15 1347.74
0.6107 293.15 1329.59
0.6107 298.15 1311.58
0.6107 303.15 1293.98
0.6107 308.15 1276.38
0.6683 288.15 1355.56
0.6683 293.15 1337.54
0.6683 298.15 1319.68
0.6683 303.15 1302.25
0.6683 308.15 1284.77
0.6924 288.15 1358.91
0.6924 293.15 1340.94
0.6924 298.15 1323.16
0.6924 303.15 1305.8
0.6924 308.15 1288.36
0.7544 288.15 1367.76
0.7544 293.15 1349.97
0.7544 298.15 1332.33
0.7544 303.15 1315.15
0.7544 308.15 1297.81
0.7963 288.15 1373.92
0.7963 293.15 1356.22
0.7963 298.15 1338.74
0.7963 303.15 1321.64
0.7963 308.15 1304.36
0.8580 288.15 1383.21
0.8580 293.15 1365.72
0.8580 298.15 1348.35
0.8580 303.15 1331.46
0.8580 308.15 1314.21
0.9079 288.15 1390.94
0.9079 293.15 1373.58
0.9079 298.15 1356.38
0.9079 303.15 1339.62
0.9079 308.15 1322.35
0.9553 288.15 1398.43
0.9553 293.15 1381.26
0.9553 298.15 1364.2
0.9553 303.15 1347.56
0.9553 308.15 1330.18

Sources