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

Excel

Ethane, 1,1,2,2-tetrabromo-

Name
Ethane, 1,1,2,2-tetrabromo-
InChI
InChI=1S/C2H2Br4/c3-1(4)2(5)6/h1-2H
InChI Key
QXSZNDIIPUOQMB-UHFFFAOYSA-N
Formula
C2H2Br4
SMILES
BrC(Br)C(Br)Br
Mol. Weight (g/mol)
345.65
CAS
79-27-6

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. η - Viscosity, Pa*s (2)
  2. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (4)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0145
293.15 0.1023 0.0141
293.15 0.2020 0.0137
293.15 0.3012 0.0132
293.15 0.4012 0.0128
293.15 0.5007 0.0124
293.15 0.6006 0.0121
293.15 0.7011 0.0117
293.15 0.8006 0.0115
293.15 0.9006 0.0112
293.15 1.0000 0.0109
303.15 0.0000 0.0097
303.15 0.1023 0.0094
303.15 0.2020 0.0092
303.15 0.3012 0.0090
303.15 0.4012 0.0089
303.15 0.5007 0.0087
303.15 0.6006 0.0086
303.15 0.7011 0.0085
303.15 0.8006 0.0084
303.15 0.9006 0.0084
303.15 1.0000 0.0084

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0145
293.15 0.1023 0.0141
293.15 0.2020 0.0137
293.15 0.3012 0.0132
293.15 0.4012 0.0128
293.15 0.5007 0.0124
293.15 0.6006 0.0121
293.15 0.7011 0.0117
293.15 0.8006 0.0115
293.15 0.9006 0.0112
293.15 1.0000 0.0109
303.15 0.0000 0.0097
303.15 0.1023 0.0094
303.15 0.2020 0.0092
303.15 0.3012 0.0090
303.15 0.4012 0.0089
303.15 0.5007 0.0087
303.15 0.6006 0.0086
303.15 0.7011 0.0085
303.15 0.8006 0.0084
303.15 0.9006 0.0084
303.15 1.0000 0.0084

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Refractive index (Na D-line) - Liquid
293.15 0.0000 1.4371
293.15 0.1023 1.4493
293.15 0.2020 1.4623
293.15 0.3012 1.4764
293.15 0.4012 1.4921
293.15 0.5007 1.5094
293.15 0.6006 1.5289
293.15 0.7011 1.5506
293.15 0.8006 1.5752
293.15 0.9006 1.6032
293.15 1.0000 1.6354
303.15 0.0000 1.433
303.15 0.1023 1.4449
303.15 0.2020 1.4576
303.15 0.3012 1.4715
303.15 0.4012 1.487
303.15 0.5007 1.504
303.15 0.6006 1.5232
303.15 0.7011 1.5449
303.15 0.8006 1.5693
303.15 0.9006 1.5972
303.15 1.0000 1.6293

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Refractive index (Na D-line) - Liquid
293.15 0.0000 1.4371
293.15 0.1023 1.4493
293.15 0.2020 1.4623
293.15 0.3012 1.4764
293.15 0.4012 1.4921
293.15 0.5007 1.5094
293.15 0.6006 1.5289
293.15 0.7011 1.5506
293.15 0.8006 1.5752
293.15 0.9006 1.6032
293.15 1.0000 1.6354
303.15 0.0000 1.433
303.15 0.1023 1.4449
303.15 0.2020 1.4576
303.15 0.3012 1.4715
303.15 0.4012 1.487
303.15 0.5007 1.504
303.15 0.6006 1.5232
303.15 0.7011 1.5449
303.15 0.8006 1.5693
303.15 0.9006 1.5972
303.15 1.0000 1.6293

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 829.7
293.15 0.1023 968.19
293.15 0.2020 1114.37
293.15 0.3012 1272.36
293.15 0.4012 1446.62
293.15 0.5007 1636.66
293.15 0.6006 1847.04
293.15 0.7011 2081.74
293.15 0.8006 2340.68
293.15 0.9006 2632.79
293.15 1.0000 2963.2
303.15 0.0000 822.85
303.15 0.1023 960.09
303.15 0.2020 1104.97
303.15 0.3012 1261.57
303.15 0.4012 1434.34
303.15 0.5007 1622.78
303.15 0.6006 1831.45
303.15 0.7011 2064.32
303.15 0.8006 2321.36
303.15 0.9006 2611.47
303.15 1.0000 2939.86

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 829.7
293.15 0.1023 968.19
293.15 0.2020 1114.37
293.15 0.3012 1272.36
293.15 0.4012 1446.62
293.15 0.5007 1636.66
293.15 0.6006 1847.04
293.15 0.7011 2081.74
293.15 0.8006 2340.68
293.15 0.9006 2632.79
293.15 1.0000 2963.2
303.15 0.0000 822.85
303.15 0.1023 960.09
303.15 0.2020 1104.97
303.15 0.3012 1261.57
303.15 0.4012 1434.34
303.15 0.5007 1622.78
303.15 0.6006 1831.45
303.15 0.7011 2064.32
303.15 0.8006 2321.36
303.15 0.9006 2611.47
303.15 1.0000 2939.86

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 829.7
293.15 0.1023 968.19
293.15 0.2020 1114.37
293.15 0.3012 1272.36
293.15 0.4012 1446.62
293.15 0.5007 1636.66
293.15 0.6006 1847.04
293.15 0.7011 2081.74
293.15 0.8006 2340.68
293.15 0.9006 2632.79
293.15 1.0000 2963.2
303.15 0.0000 822.85
303.15 0.1023 960.09
303.15 0.2020 1104.97
303.15 0.3012 1261.57
303.15 0.4012 1434.34
303.15 0.5007 1622.78
303.15 0.6006 1831.45
303.15 0.7011 2064.32
303.15 0.8006 2321.36
303.15 0.9006 2611.47
303.15 1.0000 2939.86

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,1,2,2-tetrabromo- (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 829.7
293.15 0.1023 968.19
293.15 0.2020 1114.37
293.15 0.3012 1272.36
293.15 0.4012 1446.62
293.15 0.5007 1636.66
293.15 0.6006 1847.04
293.15 0.7011 2081.74
293.15 0.8006 2340.68
293.15 0.9006 2632.79
293.15 1.0000 2963.2
303.15 0.0000 822.85
303.15 0.1023 960.09
303.15 0.2020 1104.97
303.15 0.3012 1261.57
303.15 0.4012 1434.34
303.15 0.5007 1622.78
303.15 0.6006 1831.45
303.15 0.7011 2064.32
303.15 0.8006 2321.36
303.15 0.9006 2611.47
303.15 1.0000 2939.86

Sources