Mixture of Ethanol, 2-butoxy- + 1-Decanol

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Ethanol, 2-butoxy-

Name
Ethanol, 2-butoxy-
InChI
InChI=1S/C6H14O2/c1-2-3-5-8-6-4-7/h7H,2-6H2,1H3
InChI Key
POAOYUHQDCAZBD-UHFFFAOYSA-N
Formula
C6H14O2
SMILES
CCCCOCCO
Mol. Weight (g/mol)
118.17
CAS
111-76-2

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)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0563 0.0107
298.15 0.1024 0.0099
298.15 0.1544 0.0091
298.15 0.2049 0.0084
298.15 0.2531 0.0078
298.15 0.3066 0.0073
298.15 0.4028 0.0064
298.15 0.5033 0.0055
298.15 0.6031 0.0049
298.15 0.7009 0.0043
298.15 0.8043 0.0037
298.15 0.8532 0.0034
298.15 0.8996 0.0033
298.15 0.9447 0.0031
303.15 0.0563 0.0088
303.15 0.1024 0.0082
303.15 0.1544 0.0076
303.15 0.2049 0.0070
303.15 0.2531 0.0066
303.15 0.3066 0.0061
303.15 0.4028 0.0053
303.15 0.5033 0.0047
303.15 0.6031 0.0041
303.15 0.7009 0.0036
303.15 0.8043 0.0032
303.15 0.8532 0.0030
303.15 0.8996 0.0028
303.15 0.9447 0.0027
308.15 0.0563 0.0075
308.15 0.1024 0.0069
308.15 0.1544 0.0064
308.15 0.2049 0.0060
308.15 0.2531 0.0056
308.15 0.3066 0.0052
308.15 0.4028 0.0046
308.15 0.5033 0.0041
308.15 0.6031 0.0036
308.15 0.7009 0.0032
308.15 0.8043 0.0028
308.15 0.8532 0.0026
308.15 0.8996 0.0025
308.15 0.9447 0.0023

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0563 0.0107
298.15 0.1024 0.0099
298.15 0.1544 0.0091
298.15 0.2049 0.0084
298.15 0.2531 0.0078
298.15 0.3066 0.0073
298.15 0.4028 0.0064
298.15 0.5033 0.0055
298.15 0.6031 0.0049
298.15 0.7009 0.0043
298.15 0.8043 0.0037
298.15 0.8532 0.0034
298.15 0.8996 0.0033
298.15 0.9447 0.0031
303.15 0.0563 0.0088
303.15 0.1024 0.0082
303.15 0.1544 0.0076
303.15 0.2049 0.0070
303.15 0.2531 0.0066
303.15 0.3066 0.0061
303.15 0.4028 0.0053
303.15 0.5033 0.0047
303.15 0.6031 0.0041
303.15 0.7009 0.0036
303.15 0.8043 0.0032
303.15 0.8532 0.0030
303.15 0.8996 0.0028
303.15 0.9447 0.0027
308.15 0.0563 0.0075
308.15 0.1024 0.0069
308.15 0.1544 0.0064
308.15 0.2049 0.0060
308.15 0.2531 0.0056
308.15 0.3066 0.0052
308.15 0.4028 0.0046
308.15 0.5033 0.0041
308.15 0.6031 0.0036
308.15 0.7009 0.0032
308.15 0.8043 0.0028
308.15 0.8532 0.0026
308.15 0.8996 0.0025
308.15 0.9447 0.0023

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0563 832.457
293.15 0.1024 834.521
293.15 0.1544 836.95
293.15 0.2049 839.424
293.15 0.2531 841.903
293.15 0.3066 844.775
293.15 0.4028 850.363
293.15 0.5033 856.773
293.15 0.6031 863.803
293.15 0.7009 871.448
293.15 0.8043 880.396
293.15 0.8532 884.962
293.15 0.8996 889.528
293.15 0.9447 894.239
298.15 0.0563 829.0
298.15 0.1024 831.148
298.15 0.1544 833.643
298.15 0.2049 836.177
298.15 0.2531 838.694
298.15 0.3066 841.628
298.15 0.4028 847.26
298.15 0.5033 853.675
298.15 0.6031 860.637
298.15 0.7009 868.128
298.15 0.8043 876.828
298.15 0.8532 881.288
298.15 0.8996 885.737
298.15 0.9447 890.317
303.15 0.0563 825.535
303.15 0.1024 827.625
303.15 0.1544 830.09
303.15 0.2049 832.6
303.15 0.2531 835.09
303.15 0.3066 837.986
303.15 0.4028 843.566
303.15 0.5033 849.927
303.15 0.6031 856.84
303.15 0.7009 864.279
303.15 0.8043 872.98
303.15 0.8532 877.42
303.15 0.8996 881.86
303.15 0.9447 886.371
308.15 0.0563 822.068
308.15 0.1024 824.141
308.15 0.1544 826.569
308.15 0.2049 829.044
308.15 0.2531 831.491
308.15 0.3066 834.361
308.15 0.4028 839.86
308.15 0.5033 846.141
308.15 0.6031 852.988
308.15 0.7009 860.384
308.15 0.8043 869.011
308.15 0.8532 873.415
308.15 0.8996 877.785
308.15 0.9447 882.225
313.15 0.0563 818.532
313.15 0.1024 820.551
313.15 0.1544 822.945
313.15 0.2049 825.399
313.15 0.2531 827.825
313.15 0.3066 830.657
313.15 0.4028 836.098
313.15 0.5033 842.307
313.15 0.6031 849.078
313.15 0.7009 856.416
313.15 0.8043 864.959
313.15 0.8532 869.328
313.15 0.8996 873.661
313.15 0.9447 878.012

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0563 832.457
293.15 0.1024 834.521
293.15 0.1544 836.95
293.15 0.2049 839.424
293.15 0.2531 841.903
293.15 0.3066 844.775
293.15 0.4028 850.363
293.15 0.5033 856.773
293.15 0.6031 863.803
293.15 0.7009 871.448
293.15 0.8043 880.396
293.15 0.8532 884.962
293.15 0.8996 889.528
293.15 0.9447 894.239
298.15 0.0563 829.0
298.15 0.1024 831.148
298.15 0.1544 833.643
298.15 0.2049 836.177
298.15 0.2531 838.694
298.15 0.3066 841.628
298.15 0.4028 847.26
298.15 0.5033 853.675
298.15 0.6031 860.637
298.15 0.7009 868.128
298.15 0.8043 876.828
298.15 0.8532 881.288
298.15 0.8996 885.737
298.15 0.9447 890.317
303.15 0.0563 825.535
303.15 0.1024 827.625
303.15 0.1544 830.09
303.15 0.2049 832.6
303.15 0.2531 835.09
303.15 0.3066 837.986
303.15 0.4028 843.566
303.15 0.5033 849.927
303.15 0.6031 856.84
303.15 0.7009 864.279
303.15 0.8043 872.98
303.15 0.8532 877.42
303.15 0.8996 881.86
303.15 0.9447 886.371
308.15 0.0563 822.068
308.15 0.1024 824.141
308.15 0.1544 826.569
308.15 0.2049 829.044
308.15 0.2531 831.491
308.15 0.3066 834.361
308.15 0.4028 839.86
308.15 0.5033 846.141
308.15 0.6031 852.988
308.15 0.7009 860.384
308.15 0.8043 869.011
308.15 0.8532 873.415
308.15 0.8996 877.785
308.15 0.9447 882.225
313.15 0.0563 818.532
313.15 0.1024 820.551
313.15 0.1544 822.945
313.15 0.2049 825.399
313.15 0.2531 827.825
313.15 0.3066 830.657
313.15 0.4028 836.098
313.15 0.5033 842.307
313.15 0.6031 849.078
313.15 0.7009 856.416
313.15 0.8043 864.959
313.15 0.8532 869.328
313.15 0.8996 873.661
313.15 0.9447 878.012

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0563 1392.03
293.15 0.1024 1388.25
293.15 0.1544 1383.84
293.15 0.2049 1379.48
293.15 0.2531 1374.77
293.15 0.3066 1369.89
293.15 0.4028 1360.68
293.15 0.5033 1351.49
293.15 0.6031 1343.55
293.15 0.7009 1337.1
293.15 0.8043 1331.25
293.15 0.8532 1328.72
293.15 0.8996 1326.28
293.15 0.9447 1324.55
298.15 0.0563 1374.93
298.15 0.1024 1371.09
298.15 0.1544 1366.78
298.15 0.2049 1362.57
298.15 0.2531 1358.27
298.15 0.3066 1353.7
298.15 0.4028 1344.87
298.15 0.5033 1336.13
298.15 0.6031 1328.17
298.15 0.7009 1321.14
298.15 0.8043 1314.94
298.15 0.8532 1312.58
298.15 0.8996 1310.23
298.15 0.9447 1308.28
303.15 0.0563 1358.14
303.15 0.1024 1354.44
303.15 0.1544 1350.14
303.15 0.2049 1345.9
303.15 0.2531 1341.74
303.15 0.3066 1337.13
303.15 0.4028 1328.92
303.15 0.5033 1320.76
303.15 0.6031 1313.18
303.15 0.7009 1306.3
303.15 0.8043 1299.73
303.15 0.8532 1296.73
303.15 0.8996 1294.15
303.15 0.9447 1291.73
308.15 0.0563 1341.47
308.15 0.1024 1337.83
308.15 0.1544 1333.88
308.15 0.2049 1330.0
308.15 0.2531 1326.06
308.15 0.3066 1321.83
308.15 0.4028 1314.1
308.15 0.5033 1306.02
308.15 0.6031 1298.24
308.15 0.7009 1290.93
308.15 0.8043 1283.72
308.15 0.8532 1280.58
308.15 0.8996 1277.72
308.15 0.9447 1275.26
313.15 0.0563 1324.75
313.15 0.1024 1321.54
313.15 0.1544 1317.78
313.15 0.2049 1314.16
313.15 0.2531 1310.59
313.15 0.3066 1306.57
313.15 0.4028 1299.41
313.15 0.5033 1291.98
313.15 0.6031 1284.48
313.15 0.7009 1277.02
313.15 0.8043 1269.37
313.15 0.8532 1266.15
313.15 0.8996 1262.74
313.15 0.9447 1259.73

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0563 1392.03
293.15 0.1024 1388.25
293.15 0.1544 1383.84
293.15 0.2049 1379.48
293.15 0.2531 1374.77
293.15 0.3066 1369.89
293.15 0.4028 1360.68
293.15 0.5033 1351.49
293.15 0.6031 1343.55
293.15 0.7009 1337.1
293.15 0.8043 1331.25
293.15 0.8532 1328.72
293.15 0.8996 1326.28
293.15 0.9447 1324.55
298.15 0.0563 1374.93
298.15 0.1024 1371.09
298.15 0.1544 1366.78
298.15 0.2049 1362.57
298.15 0.2531 1358.27
298.15 0.3066 1353.7
298.15 0.4028 1344.87
298.15 0.5033 1336.13
298.15 0.6031 1328.17
298.15 0.7009 1321.14
298.15 0.8043 1314.94
298.15 0.8532 1312.58
298.15 0.8996 1310.23
298.15 0.9447 1308.28
303.15 0.0563 1358.14
303.15 0.1024 1354.44
303.15 0.1544 1350.14
303.15 0.2049 1345.9
303.15 0.2531 1341.74
303.15 0.3066 1337.13
303.15 0.4028 1328.92
303.15 0.5033 1320.76
303.15 0.6031 1313.18
303.15 0.7009 1306.3
303.15 0.8043 1299.73
303.15 0.8532 1296.73
303.15 0.8996 1294.15
303.15 0.9447 1291.73
308.15 0.0563 1341.47
308.15 0.1024 1337.83
308.15 0.1544 1333.88
308.15 0.2049 1330.0
308.15 0.2531 1326.06
308.15 0.3066 1321.83
308.15 0.4028 1314.1
308.15 0.5033 1306.02
308.15 0.6031 1298.24
308.15 0.7009 1290.93
308.15 0.8043 1283.72
308.15 0.8532 1280.58
308.15 0.8996 1277.72
308.15 0.9447 1275.26
313.15 0.0563 1324.75
313.15 0.1024 1321.54
313.15 0.1544 1317.78
313.15 0.2049 1314.16
313.15 0.2531 1310.59
313.15 0.3066 1306.57
313.15 0.4028 1299.41
313.15 0.5033 1291.98
313.15 0.6031 1284.48
313.15 0.7009 1277.02
313.15 0.8043 1269.37
313.15 0.8532 1266.15
313.15 0.8996 1262.74
313.15 0.9447 1259.73

Sources