Mixture of Ethane, 1,2-dibromo- + 1-Decanol

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Ethane, 1,2-dibromo-

Name
Ethane, 1,2-dibromo-
InChI
InChI=1S/C2H4Br2/c3-1-2-4/h1-2H2
InChI Key
PAAZPARNPHGIKF-UHFFFAOYSA-N
Formula
C2H4Br2
SMILES
BrCCBr
Mol. Weight (g/mol)
187.86
CAS
106-93-4

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

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 829.991
293.15 0.0713 873.696
293.15 0.1171 903.742
293.15 0.1704 940.915
293.15 0.2858 1030.687
293.15 0.3911 1125.696
293.15 0.5100 1252.151
293.15 0.5430 1291.442
293.15 0.5903 1351.801
293.15 0.6875 1492.469
293.15 0.7289 1560.167
293.15 0.7873 1665.231
293.15 0.8411 1773.358
293.15 0.9006 1908.196
293.15 0.9495 2033.543
293.15 1.0000 2179.604
313.15 0.0000 816.264
313.15 0.0713 859.289
313.15 0.1171 888.874
313.15 0.1704 925.398
313.15 0.2858 1013.602
313.15 0.3911 1106.722
313.15 0.5100 1230.296
313.15 0.5430 1268.705
313.15 0.5903 1327.542
313.15 0.6875 1464.538
313.15 0.7289 1530.454
313.15 0.7873 1632.901
313.15 0.8411 1738.483
313.15 0.9006 1870.501
313.15 0.9495 1993.499
313.15 1.0000 2137.698

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 829.991
293.15 0.0713 873.696
293.15 0.1171 903.742
293.15 0.1704 940.915
293.15 0.2858 1030.687
293.15 0.3911 1125.696
293.15 0.5100 1252.151
293.15 0.5430 1291.442
293.15 0.5903 1351.801
293.15 0.6875 1492.469
293.15 0.7289 1560.167
293.15 0.7873 1665.231
293.15 0.8411 1773.358
293.15 0.9006 1908.196
293.15 0.9495 2033.543
293.15 1.0000 2179.604
313.15 0.0000 816.264
313.15 0.0713 859.289
313.15 0.1171 888.874
313.15 0.1704 925.398
313.15 0.2858 1013.602
313.15 0.3911 1106.722
313.15 0.5100 1230.296
313.15 0.5430 1268.705
313.15 0.5903 1327.542
313.15 0.6875 1464.538
313.15 0.7289 1530.454
313.15 0.7873 1632.901
313.15 0.8411 1738.483
313.15 0.9006 1870.501
313.15 0.9495 1993.499
313.15 1.0000 2137.698

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0000 1396.37
293.15 0.0713 1363.08
293.15 0.1171 1341.81
293.15 0.1704 1317.21
293.15 0.2858 1265.99
293.15 0.3911 1218.27
293.15 0.5100 1167.73
293.15 0.5430 1153.37
293.15 0.5903 1134.09
293.15 0.6875 1095.33
293.15 0.7289 1079.96
293.15 0.7873 1059.7
293.15 0.8411 1042.2
293.15 0.9006 1025.52
293.15 0.9495 1015.59
293.15 1.0000 1006.95
313.15 0.0000 1328.65
313.15 0.0713 1296.39
313.15 0.1171 1275.41
313.15 0.1704 1251.81
313.15 0.2858 1202.94
313.15 0.3911 1157.19
313.15 0.5100 1108.86
313.15 0.5430 1094.95
313.15 0.5903 1076.8
313.15 0.6875 1040.49
313.15 0.7289 1025.91
313.15 0.7873 1006.6
313.15 0.8411 990.48
313.15 0.9006 975.34
313.15 0.9495 965.65
313.15 1.0000 955.97

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0000 1396.37
293.15 0.0713 1363.08
293.15 0.1171 1341.81
293.15 0.1704 1317.21
293.15 0.2858 1265.99
293.15 0.3911 1218.27
293.15 0.5100 1167.73
293.15 0.5430 1153.37
293.15 0.5903 1134.09
293.15 0.6875 1095.33
293.15 0.7289 1079.96
293.15 0.7873 1059.7
293.15 0.8411 1042.2
293.15 0.9006 1025.52
293.15 0.9495 1015.59
293.15 1.0000 1006.95
313.15 0.0000 1328.65
313.15 0.0713 1296.39
313.15 0.1171 1275.41
313.15 0.1704 1251.81
313.15 0.2858 1202.94
313.15 0.3911 1157.19
313.15 0.5100 1108.86
313.15 0.5430 1094.95
313.15 0.5903 1076.8
313.15 0.6875 1040.49
313.15 0.7289 1025.91
313.15 0.7873 1006.6
313.15 0.8411 990.48
313.15 0.9006 975.34
313.15 0.9495 965.65
313.15 1.0000 955.97

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0000 0.0000
293.15 0.0713 3.2620e-07
293.15 0.1171 5.0870e-07
293.15 0.1704 6.8410e-07
293.15 0.2858 9.3820e-07
293.15 0.3911 1.0568e-06
293.15 0.5100 1.0542e-06
293.15 0.5430 1.0466e-06
293.15 0.5903 9.9720e-07
293.15 0.6875 8.2890e-07
293.15 0.7289 7.4750e-07
293.15 0.7873 6.1560e-07
293.15 0.8411 4.8750e-07
293.15 0.9006 3.2990e-07
293.15 0.9495 1.7830e-07
293.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0713 3.0520e-07
313.15 0.1171 4.7300e-07
313.15 0.1704 6.4610e-07
313.15 0.2858 8.9160e-07
313.15 0.3911 1.0301e-06
313.15 0.5100 1.0806e-06
313.15 0.5430 1.0829e-06
313.15 0.5903 1.0616e-06
313.15 0.6875 9.4750e-07
313.15 0.7289 8.8450e-07
313.15 0.7873 7.6200e-07
313.15 0.8411 6.2870e-07
313.15 0.9006 4.4230e-07
313.15 0.9495 2.5300e-07
313.15 1.0000 0.0000

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0000 0.0000
293.15 0.0713 3.2620e-07
293.15 0.1171 5.0870e-07
293.15 0.1704 6.8410e-07
293.15 0.2858 9.3820e-07
293.15 0.3911 1.0568e-06
293.15 0.5100 1.0542e-06
293.15 0.5430 1.0466e-06
293.15 0.5903 9.9720e-07
293.15 0.6875 8.2890e-07
293.15 0.7289 7.4750e-07
293.15 0.7873 6.1560e-07
293.15 0.8411 4.8750e-07
293.15 0.9006 3.2990e-07
293.15 0.9495 1.7830e-07
293.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0713 3.0520e-07
313.15 0.1171 4.7300e-07
313.15 0.1704 6.4610e-07
313.15 0.2858 8.9160e-07
313.15 0.3911 1.0301e-06
313.15 0.5100 1.0806e-06
313.15 0.5430 1.0829e-06
313.15 0.5903 1.0616e-06
313.15 0.6875 9.4750e-07
313.15 0.7289 8.8450e-07
313.15 0.7873 7.6200e-07
313.15 0.8411 6.2870e-07
313.15 0.9006 4.4230e-07
313.15 0.9495 2.5300e-07
313.15 1.0000 0.0000

Sources