Mixture of 1-Propanol + Diethylene glycol hexyl ether

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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 (4)
  2. csound,fluid - Speed of Sound, m/s (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.1085 837.518
288.15 0.1608 848.615
288.15 0.2102 857.751
288.15 0.2477 863.891
288.15 0.2972 871.227
288.15 0.3493 878.129
288.15 0.4048 884.6
288.15 0.4600 890.404
288.15 0.5003 894.261
288.15 0.5584 899.282
288.15 0.6066 903.088
288.15 0.6604 906.948
288.15 0.6964 909.32
288.15 0.7532 912.745
288.15 0.8054 915.595
288.15 0.8563 918.152
288.15 0.9044 920.357
288.15 0.9593 922.69
298.15 0.1085 829.325
298.15 0.1608 840.381
298.15 0.2102 849.425
298.15 0.2477 855.521
298.15 0.2972 862.829
298.15 0.3493 869.65
298.15 0.4048 876.088
298.15 0.4600 881.84
298.15 0.5003 885.64
298.15 0.5584 890.668
298.15 0.6066 894.428
298.15 0.6604 898.225
298.15 0.6964 900.561
298.15 0.7532 903.981
298.15 0.8054 906.826
298.15 0.8563 909.394
298.15 0.9044 911.598
298.15 0.9593 913.937
308.15 0.1085 820.919
308.15 0.1608 831.968
308.15 0.2102 841.022
308.15 0.2477 847.161
308.15 0.2972 854.397
308.15 0.3493 861.101
308.15 0.4048 867.464
308.15 0.4600 873.153
308.15 0.5003 876.925
308.15 0.5584 881.873
308.15 0.6066 885.633
308.15 0.6604 889.461
308.15 0.6964 891.847
308.15 0.7532 895.267
308.15 0.8054 898.1
308.15 0.8563 900.587
308.15 0.9044 902.735
308.15 0.9593 905.015

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.1062 843.052
288.15 0.1678 856.676
288.15 0.2147 865.458
288.15 0.2748 875.451
288.15 0.3074 880.428
288.15 0.3594 887.763
288.15 0.4007 893.137
288.15 0.4540 899.478
288.15 0.5065 905.116
288.15 0.5476 909.104
288.15 0.6141 914.857
288.15 0.6648 918.787
288.15 0.7057 921.697
288.15 0.7615 925.378
288.15 0.8008 927.797
288.15 0.8663 931.55
288.15 0.9129 933.87
288.15 0.9611 935.832
293.15 0.1062 839.34
293.15 0.1678 852.869
293.15 0.2147 861.572
293.15 0.2748 871.495
293.15 0.3074 876.423
293.15 0.3594 883.755
293.15 0.4007 889.131
293.15 0.4540 895.473
293.15 0.5065 901.108
293.15 0.5476 905.089
293.15 0.6141 910.869
293.15 0.6648 914.772
293.15 0.7057 917.7
293.15 0.7615 921.402
293.15 0.8008 923.841
293.15 0.8663 927.598
293.15 0.9129 929.946
293.15 0.9611 931.895
298.15 0.1062 835.067
298.15 0.1678 848.695
298.15 0.2147 857.456
298.15 0.2748 867.42
298.15 0.3074 872.391
298.15 0.3594 879.735
298.15 0.4007 885.109
298.15 0.4540 891.458
298.15 0.5065 897.101
298.15 0.5476 901.088
298.15 0.6141 906.849
298.15 0.6648 910.769
298.15 0.7057 913.696
298.15 0.7615 917.412
298.15 0.8008 919.869
298.15 0.8663 923.643
298.15 0.9129 925.995
298.15 0.9611 927.934
303.15 0.1062 831.089
303.15 0.1678 844.674
303.15 0.2147 853.42
303.15 0.2748 863.377
303.15 0.3074 868.329
303.15 0.3594 875.695
303.15 0.4007 881.072
303.15 0.4540 887.425
303.15 0.5065 893.072
303.15 0.5476 897.062
303.15 0.6141 902.826
303.15 0.6648 906.756
303.15 0.7057 909.679
303.15 0.7615 913.4
303.15 0.8008 915.862
303.15 0.8663 919.659
303.15 0.9129 922.009
303.15 0.9611 923.955
308.15 0.1062 827.206
308.15 0.1678 840.696
308.15 0.2147 849.384
308.15 0.2748 859.316
308.15 0.3074 864.284
308.15 0.3594 871.64
308.15 0.4007 877.016
308.15 0.4540 883.38
308.15 0.5065 889.029
308.15 0.5476 893.028
308.15 0.6141 898.797
308.15 0.6648 902.724
308.15 0.7057 905.653
308.15 0.7615 909.372
308.15 0.8008 911.828
308.15 0.8663 915.63
308.15 0.9129 918.002
308.15 0.9611 919.943

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.1085 837.518
288.15 0.1608 848.615
288.15 0.2102 857.751
288.15 0.2477 863.891
288.15 0.2972 871.227
288.15 0.3493 878.129
288.15 0.4048 884.6
288.15 0.4600 890.404
288.15 0.5003 894.261
288.15 0.5584 899.282
288.15 0.6066 903.088
288.15 0.6604 906.948
288.15 0.6964 909.32
288.15 0.7532 912.745
288.15 0.8054 915.595
288.15 0.8563 918.152
288.15 0.9044 920.357
288.15 0.9593 922.69
298.15 0.1085 829.325
298.15 0.1608 840.381
298.15 0.2102 849.425
298.15 0.2477 855.521
298.15 0.2972 862.829
298.15 0.3493 869.65
298.15 0.4048 876.088
298.15 0.4600 881.84
298.15 0.5003 885.64
298.15 0.5584 890.668
298.15 0.6066 894.428
298.15 0.6604 898.225
298.15 0.6964 900.561
298.15 0.7532 903.981
298.15 0.8054 906.826
298.15 0.8563 909.394
298.15 0.9044 911.598
298.15 0.9593 913.937
308.15 0.1085 820.919
308.15 0.1608 831.968
308.15 0.2102 841.022
308.15 0.2477 847.161
308.15 0.2972 854.397
308.15 0.3493 861.101
308.15 0.4048 867.464
308.15 0.4600 873.153
308.15 0.5003 876.925
308.15 0.5584 881.873
308.15 0.6066 885.633
308.15 0.6604 889.461
308.15 0.6964 891.847
308.15 0.7532 895.267
308.15 0.8054 898.1
308.15 0.8563 900.587
308.15 0.9044 902.735
308.15 0.9593 905.015

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.1062 843.052
288.15 0.1678 856.676
288.15 0.2147 865.458
288.15 0.2748 875.451
288.15 0.3074 880.428
288.15 0.3594 887.763
288.15 0.4007 893.137
288.15 0.4540 899.478
288.15 0.5065 905.116
288.15 0.5476 909.104
288.15 0.6141 914.857
288.15 0.6648 918.787
288.15 0.7057 921.697
288.15 0.7615 925.378
288.15 0.8008 927.797
288.15 0.8663 931.55
288.15 0.9129 933.87
288.15 0.9611 935.832
293.15 0.1062 839.34
293.15 0.1678 852.869
293.15 0.2147 861.572
293.15 0.2748 871.495
293.15 0.3074 876.423
293.15 0.3594 883.755
293.15 0.4007 889.131
293.15 0.4540 895.473
293.15 0.5065 901.108
293.15 0.5476 905.089
293.15 0.6141 910.869
293.15 0.6648 914.772
293.15 0.7057 917.7
293.15 0.7615 921.402
293.15 0.8008 923.841
293.15 0.8663 927.598
293.15 0.9129 929.946
293.15 0.9611 931.895
298.15 0.1062 835.067
298.15 0.1678 848.695
298.15 0.2147 857.456
298.15 0.2748 867.42
298.15 0.3074 872.391
298.15 0.3594 879.735
298.15 0.4007 885.109
298.15 0.4540 891.458
298.15 0.5065 897.101
298.15 0.5476 901.088
298.15 0.6141 906.849
298.15 0.6648 910.769
298.15 0.7057 913.696
298.15 0.7615 917.412
298.15 0.8008 919.869
298.15 0.8663 923.643
298.15 0.9129 925.995
298.15 0.9611 927.934
303.15 0.1062 831.089
303.15 0.1678 844.674
303.15 0.2147 853.42
303.15 0.2748 863.377
303.15 0.3074 868.329
303.15 0.3594 875.695
303.15 0.4007 881.072
303.15 0.4540 887.425
303.15 0.5065 893.072
303.15 0.5476 897.062
303.15 0.6141 902.826
303.15 0.6648 906.756
303.15 0.7057 909.679
303.15 0.7615 913.4
303.15 0.8008 915.862
303.15 0.8663 919.659
303.15 0.9129 922.009
303.15 0.9611 923.955
308.15 0.1062 827.206
308.15 0.1678 840.696
308.15 0.2147 849.384
308.15 0.2748 859.316
308.15 0.3074 864.284
308.15 0.3594 871.64
308.15 0.4007 877.016
308.15 0.4540 883.38
308.15 0.5065 889.029
308.15 0.5476 893.028
308.15 0.6141 898.797
308.15 0.6648 902.724
308.15 0.7057 905.653
308.15 0.7615 909.372
308.15 0.8008 911.828
308.15 0.8663 915.63
308.15 0.9129 918.002
308.15 0.9611 919.943

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Speed of sound, m/s - Liquid
288.15 0.1062 1284.22
288.15 0.1678 1301.99
288.15 0.2147 1313.7
288.15 0.2748 1327.19
288.15 0.3074 1333.75
288.15 0.3594 1343.29
288.15 0.4007 1350.05
288.15 0.4540 1357.9
288.15 0.5065 1364.8
288.15 0.5476 1369.75
288.15 0.6141 1376.84
288.15 0.6648 1381.92
288.15 0.7057 1385.42
288.15 0.7615 1389.94
288.15 0.8008 1392.91
288.15 0.8663 1397.41
288.15 0.9129 1400.26
288.15 0.9611 1402.93
293.15 0.1062 1267.34
293.15 0.1678 1284.56
293.15 0.2147 1296.26
293.15 0.2748 1309.65
293.15 0.3074 1316.35
293.15 0.3594 1326.02
293.15 0.4007 1332.9
293.15 0.4540 1340.94
293.15 0.5065 1348.06
293.15 0.5476 1353.11
293.15 0.6141 1360.22
293.15 0.6648 1365.06
293.15 0.7057 1368.6
293.15 0.7615 1372.95
293.15 0.8008 1375.88
293.15 0.8663 1380.32
293.15 0.9129 1383.37
293.15 0.9611 1386.38
298.15 0.1062 1249.32
298.15 0.1678 1267.64
298.15 0.2147 1279.74
298.15 0.2748 1293.36
298.15 0.3074 1299.91
298.15 0.3594 1309.31
298.15 0.4007 1316.04
298.15 0.4540 1323.95
298.15 0.5065 1330.8
298.15 0.5476 1335.82
298.15 0.6141 1343.05
298.15 0.6648 1348.1
298.15 0.7057 1351.84
298.15 0.7615 1356.56
298.15 0.8008 1359.53
298.15 0.8663 1363.92
298.15 0.9129 1366.51
298.15 0.9611 1368.72
303.15 0.1062 1232.64
303.15 0.1678 1250.96
303.15 0.2147 1262.96
303.15 0.2748 1276.42
303.15 0.3074 1282.96
303.15 0.3594 1292.35
303.15 0.4007 1299.0
303.15 0.4540 1306.91
303.15 0.5065 1313.86
303.15 0.5476 1318.84
303.15 0.6141 1326.22
303.15 0.6648 1331.38
303.15 0.7057 1335.15
303.15 0.7615 1339.89
303.15 0.8008 1342.88
303.15 0.8663 1347.24
303.15 0.9129 1349.8
303.15 0.9611 1351.8
308.15 0.1062 1215.78
308.15 0.1678 1233.96
308.15 0.2147 1245.99
308.15 0.2748 1259.48
308.15 0.3074 1266.02
308.15 0.3594 1275.53
308.15 0.4007 1282.27
308.15 0.4540 1290.14
308.15 0.5065 1297.1
308.15 0.5476 1302.1
308.15 0.6141 1309.36
308.15 0.6648 1314.35
308.15 0.7057 1318.07
308.15 0.7615 1322.75
308.15 0.8008 1325.81
308.15 0.8663 1330.19
308.15 0.9129 1332.92
308.15 0.9611 1335.33

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethylene glycol hexyl ether (2) - Liquid Speed of sound, m/s - Liquid
288.15 0.1062 1284.22
288.15 0.1678 1301.99
288.15 0.2147 1313.7
288.15 0.2748 1327.19
288.15 0.3074 1333.75
288.15 0.3594 1343.29
288.15 0.4007 1350.05
288.15 0.4540 1357.9
288.15 0.5065 1364.8
288.15 0.5476 1369.75
288.15 0.6141 1376.84
288.15 0.6648 1381.92
288.15 0.7057 1385.42
288.15 0.7615 1389.94
288.15 0.8008 1392.91
288.15 0.8663 1397.41
288.15 0.9129 1400.26
288.15 0.9611 1402.93
293.15 0.1062 1267.34
293.15 0.1678 1284.56
293.15 0.2147 1296.26
293.15 0.2748 1309.65
293.15 0.3074 1316.35
293.15 0.3594 1326.02
293.15 0.4007 1332.9
293.15 0.4540 1340.94
293.15 0.5065 1348.06
293.15 0.5476 1353.11
293.15 0.6141 1360.22
293.15 0.6648 1365.06
293.15 0.7057 1368.6
293.15 0.7615 1372.95
293.15 0.8008 1375.88
293.15 0.8663 1380.32
293.15 0.9129 1383.37
293.15 0.9611 1386.38
298.15 0.1062 1249.32
298.15 0.1678 1267.64
298.15 0.2147 1279.74
298.15 0.2748 1293.36
298.15 0.3074 1299.91
298.15 0.3594 1309.31
298.15 0.4007 1316.04
298.15 0.4540 1323.95
298.15 0.5065 1330.8
298.15 0.5476 1335.82
298.15 0.6141 1343.05
298.15 0.6648 1348.1
298.15 0.7057 1351.84
298.15 0.7615 1356.56
298.15 0.8008 1359.53
298.15 0.8663 1363.92
298.15 0.9129 1366.51
298.15 0.9611 1368.72
303.15 0.1062 1232.64
303.15 0.1678 1250.96
303.15 0.2147 1262.96
303.15 0.2748 1276.42
303.15 0.3074 1282.96
303.15 0.3594 1292.35
303.15 0.4007 1299.0
303.15 0.4540 1306.91
303.15 0.5065 1313.86
303.15 0.5476 1318.84
303.15 0.6141 1326.22
303.15 0.6648 1331.38
303.15 0.7057 1335.15
303.15 0.7615 1339.89
303.15 0.8008 1342.88
303.15 0.8663 1347.24
303.15 0.9129 1349.8
303.15 0.9611 1351.8
308.15 0.1062 1215.78
308.15 0.1678 1233.96
308.15 0.2147 1245.99
308.15 0.2748 1259.48
308.15 0.3074 1266.02
308.15 0.3594 1275.53
308.15 0.4007 1282.27
308.15 0.4540 1290.14
308.15 0.5065 1297.1
308.15 0.5476 1302.1
308.15 0.6141 1309.36
308.15 0.6648 1314.35
308.15 0.7057 1318.07
308.15 0.7615 1322.75
308.15 0.8008 1325.81
308.15 0.8663 1330.19
308.15 0.9129 1332.92
308.15 0.9611 1335.33

Sources