Mixture of 1-Pentanol + Diethylene glycol hexyl ether

Excel

1-Pentanol

Name
1-Pentanol
InChI
InChI=1S/C5H12O/c1-2-3-4-5-6/h6H,2-5H2,1H3
InChI Key
AMQJEAYHLZJPGS-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCCCO
Mol. Weight (g/mol)
88.15
CAS
71-41-0

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 0.1112 837.545
288.15 0.1587 846.35
288.15 0.2096 855.128
288.15 0.2584 862.625
288.15 0.3012 868.44
288.15 0.3558 874.88
288.15 0.4022 879.672
288.15 0.4506 884.17
288.15 0.5069 889.049
288.15 0.5410 891.897
288.15 0.5971 896.445
288.15 0.6456 900.337
288.15 0.6998 904.59
288.15 0.7470 908.177
288.15 0.8052 912.354
288.15 0.8501 915.348
288.15 0.9008 918.511
288.15 0.9459 921.161
298.15 0.1112 830.059
298.15 0.1587 838.122
298.15 0.2096 846.145
298.15 0.2584 853.171
298.15 0.3012 858.72
298.15 0.3558 865.166
298.15 0.4022 870.098
298.15 0.4506 874.849
298.15 0.5069 880.057
298.15 0.5410 883.079
298.15 0.5971 887.853
298.15 0.6456 891.848
298.15 0.6998 896.131
298.15 0.7470 899.702
298.15 0.8052 903.888
298.15 0.8501 906.892
298.15 0.9008 910.007
298.15 0.9459 912.609
308.15 0.1112 822.319
308.15 0.1587 830.389
308.15 0.2096 838.566
308.15 0.2584 845.659
308.15 0.3012 851.35
308.15 0.3558 857.77
308.15 0.4022 862.642
308.15 0.4506 867.245
308.15 0.5069 872.125
308.15 0.5410 874.951
308.15 0.5971 879.382
308.15 0.6456 883.098
308.15 0.6998 887.198
308.15 0.7470 890.721
308.15 0.8052 894.96
308.15 0.8501 898.056
308.15 0.9008 901.375
308.15 0.9459 903.991

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 0.1078 841.1
288.15 0.1622 850.687
288.15 0.2069 858.039
288.15 0.2553 865.554
288.15 0.2980 871.838
288.15 0.3646 880.994
288.15 0.4027 885.886
288.15 0.4509 891.699
288.15 0.4972 896.896
288.15 0.5422 901.582
288.15 0.6161 908.619
288.15 0.6680 913.212
288.15 0.6985 915.788
288.15 0.7544 920.338
288.15 0.8055 924.361
288.15 0.8476 927.543
288.15 0.8950 930.931
288.15 0.9529 934.588
293.15 0.1078 837.386
293.15 0.1622 846.94
293.15 0.2069 854.267
293.15 0.2553 861.758
293.15 0.2980 868.024
293.15 0.3646 877.155
293.15 0.4027 882.034
293.15 0.4509 887.834
293.15 0.4972 892.991
293.15 0.5422 897.684
293.15 0.6161 904.704
293.15 0.6680 909.288
293.15 0.6985 911.857
293.15 0.7544 916.395
293.15 0.8055 920.411
293.15 0.8476 923.58
293.15 0.8950 926.961
293.15 0.9529 930.609
298.15 0.1078 833.637
298.15 0.1622 843.17
298.15 0.2069 850.477
298.15 0.2553 857.946
298.15 0.2980 864.196
298.15 0.3646 873.301
298.15 0.4027 878.17
298.15 0.4509 883.952
298.15 0.4972 889.123
298.15 0.5422 893.794
298.15 0.6161 900.801
298.15 0.6680 905.354
298.15 0.6985 907.915
298.15 0.7544 912.444
298.15 0.8055 916.444
298.15 0.8476 919.614
298.15 0.8950 922.988
298.15 0.9529 926.624
303.15 0.1078 829.874
303.15 0.1622 839.38
303.15 0.2069 846.668
303.15 0.2553 854.12
303.15 0.2980 860.35
303.15 0.3646 869.461
303.15 0.4027 874.29
303.15 0.4509 880.058
303.15 0.4972 885.216
303.15 0.5422 889.855
303.15 0.6161 896.846
303.15 0.6680 901.411
303.15 0.6985 903.967
303.15 0.7544 908.482
303.15 0.8055 912.476
303.15 0.8476 915.638
303.15 0.8950 919.003
303.15 0.9529 922.635
308.15 0.1078 825.998
308.15 0.1622 835.531
308.15 0.2069 842.838
308.15 0.2553 850.275
308.15 0.2980 856.491
308.15 0.3646 865.566
308.15 0.4027 870.397
308.15 0.4509 876.149
308.15 0.4972 881.265
308.15 0.5422 885.892
308.15 0.6161 892.904
308.15 0.6680 897.456
308.15 0.6985 900.011
308.15 0.7544 904.53
308.15 0.8055 908.502
308.15 0.8476 911.655
308.15 0.8950 915.012
308.15 0.9529 918.64

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 0.1112 837.545
288.15 0.1587 846.35
288.15 0.2096 855.128
288.15 0.2584 862.625
288.15 0.3012 868.44
288.15 0.3558 874.88
288.15 0.4022 879.672
288.15 0.4506 884.17
288.15 0.5069 889.049
288.15 0.5410 891.897
288.15 0.5971 896.445
288.15 0.6456 900.337
288.15 0.6998 904.59
288.15 0.7470 908.177
288.15 0.8052 912.354
288.15 0.8501 915.348
288.15 0.9008 918.511
288.15 0.9459 921.161
298.15 0.1112 830.059
298.15 0.1587 838.122
298.15 0.2096 846.145
298.15 0.2584 853.171
298.15 0.3012 858.72
298.15 0.3558 865.166
298.15 0.4022 870.098
298.15 0.4506 874.849
298.15 0.5069 880.057
298.15 0.5410 883.079
298.15 0.5971 887.853
298.15 0.6456 891.848
298.15 0.6998 896.131
298.15 0.7470 899.702
298.15 0.8052 903.888
298.15 0.8501 906.892
298.15 0.9008 910.007
298.15 0.9459 912.609
308.15 0.1112 822.319
308.15 0.1587 830.389
308.15 0.2096 838.566
308.15 0.2584 845.659
308.15 0.3012 851.35
308.15 0.3558 857.77
308.15 0.4022 862.642
308.15 0.4506 867.245
308.15 0.5069 872.125
308.15 0.5410 874.951
308.15 0.5971 879.382
308.15 0.6456 883.098
308.15 0.6998 887.198
308.15 0.7470 890.721
308.15 0.8052 894.96
308.15 0.8501 898.056
308.15 0.9008 901.375
308.15 0.9459 903.991

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 0.1078 841.1
288.15 0.1622 850.687
288.15 0.2069 858.039
288.15 0.2553 865.554
288.15 0.2980 871.838
288.15 0.3646 880.994
288.15 0.4027 885.886
288.15 0.4509 891.699
288.15 0.4972 896.896
288.15 0.5422 901.582
288.15 0.6161 908.619
288.15 0.6680 913.212
288.15 0.6985 915.788
288.15 0.7544 920.338
288.15 0.8055 924.361
288.15 0.8476 927.543
288.15 0.8950 930.931
288.15 0.9529 934.588
293.15 0.1078 837.386
293.15 0.1622 846.94
293.15 0.2069 854.267
293.15 0.2553 861.758
293.15 0.2980 868.024
293.15 0.3646 877.155
293.15 0.4027 882.034
293.15 0.4509 887.834
293.15 0.4972 892.991
293.15 0.5422 897.684
293.15 0.6161 904.704
293.15 0.6680 909.288
293.15 0.6985 911.857
293.15 0.7544 916.395
293.15 0.8055 920.411
293.15 0.8476 923.58
293.15 0.8950 926.961
293.15 0.9529 930.609
298.15 0.1078 833.637
298.15 0.1622 843.17
298.15 0.2069 850.477
298.15 0.2553 857.946
298.15 0.2980 864.196
298.15 0.3646 873.301
298.15 0.4027 878.17
298.15 0.4509 883.952
298.15 0.4972 889.123
298.15 0.5422 893.794
298.15 0.6161 900.801
298.15 0.6680 905.354
298.15 0.6985 907.915
298.15 0.7544 912.444
298.15 0.8055 916.444
298.15 0.8476 919.614
298.15 0.8950 922.988
298.15 0.9529 926.624
303.15 0.1078 829.874
303.15 0.1622 839.38
303.15 0.2069 846.668
303.15 0.2553 854.12
303.15 0.2980 860.35
303.15 0.3646 869.461
303.15 0.4027 874.29
303.15 0.4509 880.058
303.15 0.4972 885.216
303.15 0.5422 889.855
303.15 0.6161 896.846
303.15 0.6680 901.411
303.15 0.6985 903.967
303.15 0.7544 908.482
303.15 0.8055 912.476
303.15 0.8476 915.638
303.15 0.8950 919.003
303.15 0.9529 922.635
308.15 0.1078 825.998
308.15 0.1622 835.531
308.15 0.2069 842.838
308.15 0.2553 850.275
308.15 0.2980 856.491
308.15 0.3646 865.566
308.15 0.4027 870.397
308.15 0.4509 876.149
308.15 0.4972 881.265
308.15 0.5422 885.892
308.15 0.6161 892.904
308.15 0.6680 897.456
308.15 0.6985 900.011
308.15 0.7544 904.53
308.15 0.8055 908.502
308.15 0.8476 911.655
308.15 0.8950 915.012
308.15 0.9529 918.64

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 0.1078 1327.31
288.15 0.1622 1335.1
288.15 0.2069 1341.08
288.15 0.2553 1347.1
288.15 0.2980 1352.12
288.15 0.3646 1359.43
288.15 0.4027 1363.3
288.15 0.4509 1367.87
288.15 0.4972 1372.1
288.15 0.5422 1375.93
288.15 0.6161 1381.7
288.15 0.6680 1385.46
288.15 0.6985 1387.59
288.15 0.7544 1391.33
288.15 0.8055 1394.44
288.15 0.8476 1396.98
288.15 0.8950 1399.8
288.15 0.9529 1402.94
293.15 0.1078 1310.31
293.15 0.1622 1318.16
293.15 0.2069 1324.1
293.15 0.2553 1330.13
293.15 0.2980 1335.19
293.15 0.3646 1342.5
293.15 0.4027 1346.33
293.15 0.4509 1351.05
293.15 0.4972 1355.15
293.15 0.5422 1359.0
293.15 0.6161 1364.7
293.15 0.6680 1368.57
293.15 0.6985 1370.58
293.15 0.7544 1374.3
293.15 0.8055 1377.49
293.15 0.8476 1379.92
293.15 0.8950 1382.7
293.15 0.9529 1385.88
298.15 0.1078 1293.5
298.15 0.1622 1301.3
298.15 0.2069 1307.29
298.15 0.2553 1313.31
298.15 0.2980 1318.33
298.15 0.3646 1325.75
298.15 0.4027 1329.57
298.15 0.4509 1334.24
298.15 0.4972 1338.46
298.15 0.5422 1342.3
298.15 0.6161 1347.91
298.15 0.6680 1351.73
298.15 0.6985 1353.78
298.15 0.7544 1357.5
298.15 0.8055 1360.51
298.15 0.8476 1363.0
298.15 0.8950 1365.86
298.15 0.9529 1368.92
303.15 0.1078 1276.85
303.15 0.1622 1284.68
303.15 0.2069 1290.6
303.15 0.2553 1296.61
303.15 0.2980 1301.64
303.15 0.3646 1308.99
303.15 0.4027 1312.79
303.15 0.4509 1317.5
303.15 0.4972 1321.6
303.15 0.5422 1325.38
303.15 0.6161 1331.11
303.15 0.6680 1334.94
303.15 0.6985 1336.97
303.15 0.7544 1340.65
303.15 0.8055 1343.76
303.15 0.8476 1346.23
303.15 0.8950 1349.0
303.15 0.9529 1352.15
308.15 0.1078 1260.15
308.15 0.1622 1268.0
308.15 0.2069 1274.01
308.15 0.2553 1280.02
308.15 0.2980 1285.16
308.15 0.3646 1292.44
308.15 0.4027 1296.22
308.15 0.4509 1300.91
308.15 0.4972 1305.06
308.15 0.5422 1308.81
308.15 0.6161 1314.54
308.15 0.6680 1318.25
308.15 0.6985 1320.38
308.15 0.7544 1324.02
308.15 0.8055 1327.13
308.15 0.8476 1329.65
308.15 0.8950 1332.32
308.15 0.9529 1335.47

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 0.1078 1327.31
288.15 0.1622 1335.1
288.15 0.2069 1341.08
288.15 0.2553 1347.1
288.15 0.2980 1352.12
288.15 0.3646 1359.43
288.15 0.4027 1363.3
288.15 0.4509 1367.87
288.15 0.4972 1372.1
288.15 0.5422 1375.93
288.15 0.6161 1381.7
288.15 0.6680 1385.46
288.15 0.6985 1387.59
288.15 0.7544 1391.33
288.15 0.8055 1394.44
288.15 0.8476 1396.98
288.15 0.8950 1399.8
288.15 0.9529 1402.94
293.15 0.1078 1310.31
293.15 0.1622 1318.16
293.15 0.2069 1324.1
293.15 0.2553 1330.13
293.15 0.2980 1335.19
293.15 0.3646 1342.5
293.15 0.4027 1346.33
293.15 0.4509 1351.05
293.15 0.4972 1355.15
293.15 0.5422 1359.0
293.15 0.6161 1364.7
293.15 0.6680 1368.57
293.15 0.6985 1370.58
293.15 0.7544 1374.3
293.15 0.8055 1377.49
293.15 0.8476 1379.92
293.15 0.8950 1382.7
293.15 0.9529 1385.88
298.15 0.1078 1293.5
298.15 0.1622 1301.3
298.15 0.2069 1307.29
298.15 0.2553 1313.31
298.15 0.2980 1318.33
298.15 0.3646 1325.75
298.15 0.4027 1329.57
298.15 0.4509 1334.24
298.15 0.4972 1338.46
298.15 0.5422 1342.3
298.15 0.6161 1347.91
298.15 0.6680 1351.73
298.15 0.6985 1353.78
298.15 0.7544 1357.5
298.15 0.8055 1360.51
298.15 0.8476 1363.0
298.15 0.8950 1365.86
298.15 0.9529 1368.92
303.15 0.1078 1276.85
303.15 0.1622 1284.68
303.15 0.2069 1290.6
303.15 0.2553 1296.61
303.15 0.2980 1301.64
303.15 0.3646 1308.99
303.15 0.4027 1312.79
303.15 0.4509 1317.5
303.15 0.4972 1321.6
303.15 0.5422 1325.38
303.15 0.6161 1331.11
303.15 0.6680 1334.94
303.15 0.6985 1336.97
303.15 0.7544 1340.65
303.15 0.8055 1343.76
303.15 0.8476 1346.23
303.15 0.8950 1349.0
303.15 0.9529 1352.15
308.15 0.1078 1260.15
308.15 0.1622 1268.0
308.15 0.2069 1274.01
308.15 0.2553 1280.02
308.15 0.2980 1285.16
308.15 0.3646 1292.44
308.15 0.4027 1296.22
308.15 0.4509 1300.91
308.15 0.4972 1305.06
308.15 0.5422 1308.81
308.15 0.6161 1314.54
308.15 0.6680 1318.25
308.15 0.6985 1320.38
308.15 0.7544 1324.02
308.15 0.8055 1327.13
308.15 0.8476 1329.65
308.15 0.8950 1332.32
308.15 0.9529 1335.47

Sources