Mixture of Ethanol, 2-(2-ethoxyethoxy)- + 1-Decanol

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Ethanol, 2-(2-ethoxyethoxy)-

Name
Ethanol, 2-(2-ethoxyethoxy)-
InChI
InChI=1S/C6H14O3/c1-2-8-5-6-9-4-3-7/h7H,2-6H2,1H3
InChI Key
XXJWXESWEXIICW-UHFFFAOYSA-N
Formula
C6H14O3
SMILES
CCOCCOCCO
Mol. Weight (g/mol)
134.17
CAS
111-90-0

1-Decanol

Name
1-Decanol
InChI
InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3
InChI Key
MWKFXSUHUHTGQN-UHFFFAOYSA-N
Formula
C10H22O
SMILES
CCCCCCCCCCO
Mol. Weight (g/mol)
158.28
CAS
112-30-1
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)
  3. csound,fluid - Speed of Sound, m/s (2)
  4. Excess molar volume, m3/mol (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0130
293.15 0.0607 0.0114
293.15 0.1090 0.0103
293.15 0.1561 0.0094
293.15 0.2105 0.0087
293.15 0.2599 0.0078
293.15 0.3089 0.0074
293.15 0.3533 0.0063
293.15 0.4923 0.0057
293.15 0.5986 0.0051
293.15 0.7153 0.0045
293.15 0.7918 0.0042
293.15 0.9010 0.0039
293.15 1.0000 0.0036
298.15 0.0000 0.0112
298.15 0.0607 0.0097
298.15 0.1090 0.0088
298.15 0.1561 0.0081
298.15 0.2105 0.0076
298.15 0.2599 0.0069
298.15 0.3089 0.0064
298.15 0.3533 0.0060
298.15 0.4923 0.0050
298.15 0.5986 0.0045
298.15 0.7153 0.0040
298.15 0.7918 0.0037
298.15 0.9010 0.0034
298.15 1.0000 0.0033
303.15 0.0000 0.0091
303.15 0.0607 0.0081
303.15 0.1090 0.0073
303.15 0.1561 0.0067
303.15 0.2105 0.0064
303.15 0.2599 0.0059
303.15 0.3089 0.0054
303.15 0.3533 0.0051
303.15 0.4923 0.0043
303.15 0.5986 0.0039
303.15 0.7153 0.0035
303.15 0.7918 0.0032
303.15 0.9010 0.0030
303.15 1.0000 0.0029
308.15 0.0000 0.0075
308.15 0.0607 0.0067
308.15 0.1090 0.0061
308.15 0.1561 0.0058
308.15 0.2105 0.0054
308.15 0.2599 0.0048
308.15 0.3089 0.0045
308.15 0.3533 0.0043
308.15 0.4923 0.0037
308.15 0.5986 0.0033
308.15 0.7153 0.0030
308.15 0.7918 0.0028
308.15 0.9010 0.0027
308.15 1.0000 0.0025

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0130
293.15 0.0607 0.0114
293.15 0.1090 0.0103
293.15 0.1561 0.0094
293.15 0.2105 0.0087
293.15 0.2599 0.0078
293.15 0.3089 0.0074
293.15 0.3533 0.0063
293.15 0.4923 0.0057
293.15 0.5986 0.0051
293.15 0.7153 0.0045
293.15 0.7918 0.0042
293.15 0.9010 0.0039
293.15 1.0000 0.0036
298.15 0.0000 0.0112
298.15 0.0607 0.0097
298.15 0.1090 0.0088
298.15 0.1561 0.0081
298.15 0.2105 0.0076
298.15 0.2599 0.0069
298.15 0.3089 0.0064
298.15 0.3533 0.0060
298.15 0.4923 0.0050
298.15 0.5986 0.0045
298.15 0.7153 0.0040
298.15 0.7918 0.0037
298.15 0.9010 0.0034
298.15 1.0000 0.0033
303.15 0.0000 0.0091
303.15 0.0607 0.0081
303.15 0.1090 0.0073
303.15 0.1561 0.0067
303.15 0.2105 0.0064
303.15 0.2599 0.0059
303.15 0.3089 0.0054
303.15 0.3533 0.0051
303.15 0.4923 0.0043
303.15 0.5986 0.0039
303.15 0.7153 0.0035
303.15 0.7918 0.0032
303.15 0.9010 0.0030
303.15 1.0000 0.0029
308.15 0.0000 0.0075
308.15 0.0607 0.0067
308.15 0.1090 0.0061
308.15 0.1561 0.0058
308.15 0.2105 0.0054
308.15 0.2599 0.0048
308.15 0.3089 0.0045
308.15 0.3533 0.0043
308.15 0.4923 0.0037
308.15 0.5986 0.0033
308.15 0.7153 0.0030
308.15 0.7918 0.0028
308.15 0.9010 0.0027
308.15 1.0000 0.0025

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0607 836.419
293.15 0.1090 841.997
293.15 0.1561 847.628
293.15 0.2105 854.439
293.15 0.2599 862.044
293.15 0.3089 867.859
293.15 0.3533 874.329
293.15 0.4923 896.636
293.15 0.5986 916.267
293.15 0.7153 940.786
293.15 0.7918 959.008
293.15 0.9010 988.518
298.15 0.0607 832.969
298.15 0.1090 838.521
298.15 0.1561 844.112
298.15 0.2105 850.88
298.15 0.2599 858.441
298.15 0.3089 864.217
298.15 0.3533 870.65
298.15 0.4923 892.825
298.15 0.5986 912.348
298.15 0.7153 936.739
298.15 0.7918 954.872
298.15 0.9010 984.244
303.15 0.0607 829.51
303.15 0.1090 835.031
303.15 0.1561 840.589
303.15 0.2105 847.315
303.15 0.2599 854.826
303.15 0.3089 860.567
303.15 0.3533 866.962
303.15 0.4923 889.005
303.15 0.5986 908.42
303.15 0.7153 932.679
303.15 0.7918 950.728
303.15 0.9010 979.965
308.15 0.0607 826.037
308.15 0.1090 831.525
308.15 0.1561 837.051
308.15 0.2105 843.734
308.15 0.2599 851.204
308.15 0.3089 856.908
308.15 0.3533 863.255
308.15 0.4923 885.17
308.15 0.5986 904.477
308.15 0.7153 928.613
308.15 0.7918 946.566
308.15 0.9010 975.664

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0607 836.419
293.15 0.1090 841.997
293.15 0.1561 847.628
293.15 0.2105 854.439
293.15 0.2599 862.044
293.15 0.3089 867.859
293.15 0.3533 874.329
293.15 0.4923 896.636
293.15 0.5986 916.267
293.15 0.7153 940.786
293.15 0.7918 959.008
293.15 0.9010 988.518
298.15 0.0607 832.969
298.15 0.1090 838.521
298.15 0.1561 844.112
298.15 0.2105 850.88
298.15 0.2599 858.441
298.15 0.3089 864.217
298.15 0.3533 870.65
298.15 0.4923 892.825
298.15 0.5986 912.348
298.15 0.7153 936.739
298.15 0.7918 954.872
298.15 0.9010 984.244
303.15 0.0607 829.51
303.15 0.1090 835.031
303.15 0.1561 840.589
303.15 0.2105 847.315
303.15 0.2599 854.826
303.15 0.3089 860.567
303.15 0.3533 866.962
303.15 0.4923 889.005
303.15 0.5986 908.42
303.15 0.7153 932.679
303.15 0.7918 950.728
303.15 0.9010 979.965
308.15 0.0607 826.037
308.15 0.1090 831.525
308.15 0.1561 837.051
308.15 0.2105 843.734
308.15 0.2599 851.204
308.15 0.3089 856.908
308.15 0.3533 863.255
308.15 0.4923 885.17
308.15 0.5986 904.477
308.15 0.7153 928.613
308.15 0.7918 946.566
308.15 0.9010 975.664

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0607 1394.1
293.15 0.1090 1392.3
293.15 0.1561 1390.6
293.15 0.2105 1388.9
293.15 0.2599 1387.4
293.15 0.3089 1386.6
293.15 0.3533 1385.8
293.15 0.4923 1385.3
293.15 0.5986 1387.2
293.15 0.7153 1392.6
293.15 0.7918 1398.6
293.15 0.9010 1412.6
298.15 0.0607 1377.0
298.15 0.1090 1375.3
298.15 0.1561 1373.6
298.15 0.2105 1371.8
298.15 0.2599 1370.5
298.15 0.3089 1369.6
298.15 0.3533 1368.9
298.15 0.4923 1368.4
298.15 0.5986 1370.3
298.15 0.7153 1375.7
298.15 0.7918 1381.7
298.15 0.9010 1395.6
303.15 0.0607 1360.1
303.15 0.1090 1358.4
303.15 0.1561 1356.8
303.15 0.2105 1355.1
303.15 0.2599 1353.7
303.15 0.3089 1352.8
303.15 0.3533 1352.1
303.15 0.4923 1351.7
303.15 0.5986 1353.7
303.15 0.7153 1358.9
303.15 0.7918 1364.9
303.15 0.9010 1378.8
308.15 0.0607 1343.3
308.15 0.1090 1341.6
308.15 0.1561 1340.1
308.15 0.2105 1338.4
308.15 0.2599 1336.9
308.15 0.3089 1336.2
308.15 0.3533 1335.5
308.15 0.4923 1335.1
308.15 0.5986 1337.0
308.15 0.7153 1342.4
308.15 0.7918 1348.3
308.15 0.9010 1362.1

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0607 1394.1
293.15 0.1090 1392.3
293.15 0.1561 1390.6
293.15 0.2105 1388.9
293.15 0.2599 1387.4
293.15 0.3089 1386.6
293.15 0.3533 1385.8
293.15 0.4923 1385.3
293.15 0.5986 1387.2
293.15 0.7153 1392.6
293.15 0.7918 1398.6
293.15 0.9010 1412.6
298.15 0.0607 1377.0
298.15 0.1090 1375.3
298.15 0.1561 1373.6
298.15 0.2105 1371.8
298.15 0.2599 1370.5
298.15 0.3089 1369.6
298.15 0.3533 1368.9
298.15 0.4923 1368.4
298.15 0.5986 1370.3
298.15 0.7153 1375.7
298.15 0.7918 1381.7
298.15 0.9010 1395.6
303.15 0.0607 1360.1
303.15 0.1090 1358.4
303.15 0.1561 1356.8
303.15 0.2105 1355.1
303.15 0.2599 1353.7
303.15 0.3089 1352.8
303.15 0.3533 1352.1
303.15 0.4923 1351.7
303.15 0.5986 1353.7
303.15 0.7153 1358.9
303.15 0.7918 1364.9
303.15 0.9010 1378.8
308.15 0.0607 1343.3
308.15 0.1090 1341.6
308.15 0.1561 1340.1
308.15 0.2105 1338.4
308.15 0.2599 1336.9
308.15 0.3089 1336.2
308.15 0.3533 1335.5
308.15 0.4923 1335.1
308.15 0.5986 1337.0
308.15 0.7153 1342.4
308.15 0.7918 1348.3
308.15 0.9010 1362.1

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0607 1.6900e-07
293.15 0.1090 2.6870e-07
293.15 0.1561 3.6870e-07
293.15 0.2105 4.7570e-07
293.15 0.2599 5.4170e-07
293.15 0.3089 6.0900e-07
293.15 0.3533 6.3210e-07
293.15 0.4923 7.6660e-07
293.15 0.5986 7.6140e-07
293.15 0.7153 6.8910e-07
293.15 0.7918 5.8040e-07
293.15 0.9010 3.4450e-07
298.15 0.0607 1.7040e-07
298.15 0.1090 2.6980e-07
298.15 0.1561 3.7250e-07
298.15 0.2105 4.8150e-07
298.15 0.2599 5.4800e-07
298.15 0.3089 6.1770e-07
298.15 0.3533 6.4140e-07
298.15 0.4923 7.7840e-07
298.15 0.5986 7.7340e-07
298.15 0.7153 6.9970e-07
298.15 0.7918 5.8900e-07
298.15 0.9010 3.4900e-07
303.15 0.0607 1.7230e-07
303.15 0.1090 2.7260e-07
303.15 0.1561 3.7660e-07
303.15 0.2105 4.8730e-07
303.15 0.2599 5.4890e-07
303.15 0.3089 6.2700e-07
303.15 0.3533 6.5140e-07
303.15 0.4923 7.9120e-07
303.15 0.5986 7.8630e-07
303.15 0.7153 6.1420e-07
303.15 0.7918 5.9850e-07
303.15 0.9010 3.5400e-07
308.15 0.0607 1.7300e-07
308.15 0.1090 2.2470e-07
308.15 0.1561 3.7970e-07
308.15 0.2105 4.9240e-07
308.15 0.2599 5.6050e-07
308.15 0.3089 6.3420e-07
308.15 0.3533 6.6150e-07
308.15 0.4923 8.0320e-07
308.15 0.5986 7.9840e-07
308.15 0.7153 7.2210e-07
308.15 0.7918 6.0750e-07
308.15 0.9010 3.5890e-07

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-(2-ethoxyethoxy)- (1) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0607 1.6900e-07
293.15 0.1090 2.6870e-07
293.15 0.1561 3.6870e-07
293.15 0.2105 4.7570e-07
293.15 0.2599 5.4170e-07
293.15 0.3089 6.0900e-07
293.15 0.3533 6.3210e-07
293.15 0.4923 7.6660e-07
293.15 0.5986 7.6140e-07
293.15 0.7153 6.8910e-07
293.15 0.7918 5.8040e-07
293.15 0.9010 3.4450e-07
298.15 0.0607 1.7040e-07
298.15 0.1090 2.6980e-07
298.15 0.1561 3.7250e-07
298.15 0.2105 4.8150e-07
298.15 0.2599 5.4800e-07
298.15 0.3089 6.1770e-07
298.15 0.3533 6.4140e-07
298.15 0.4923 7.7840e-07
298.15 0.5986 7.7340e-07
298.15 0.7153 6.9970e-07
298.15 0.7918 5.8900e-07
298.15 0.9010 3.4900e-07
303.15 0.0607 1.7230e-07
303.15 0.1090 2.7260e-07
303.15 0.1561 3.7660e-07
303.15 0.2105 4.8730e-07
303.15 0.2599 5.4890e-07
303.15 0.3089 6.2700e-07
303.15 0.3533 6.5140e-07
303.15 0.4923 7.9120e-07
303.15 0.5986 7.8630e-07
303.15 0.7153 6.1420e-07
303.15 0.7918 5.9850e-07
303.15 0.9010 3.5400e-07
308.15 0.0607 1.7300e-07
308.15 0.1090 2.2470e-07
308.15 0.1561 3.7970e-07
308.15 0.2105 4.9240e-07
308.15 0.2599 5.6050e-07
308.15 0.3089 6.3420e-07
308.15 0.3533 6.6150e-07
308.15 0.4923 8.0320e-07
308.15 0.5986 7.9840e-07
308.15 0.7153 7.2210e-07
308.15 0.7918 6.0750e-07
308.15 0.9010 3.5890e-07

Sources