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

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,1,2,2-tetrabromo- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0071
293.15	0.0990	0.0073
293.15	0.1999	0.0076
293.15	0.3001	0.0079
293.15	0.3995	0.0082
293.15	0.5006	0.0085
293.15	0.5987	0.0089
293.15	0.6993	0.0094
293.15	0.7990	0.0098
293.15	0.8992	0.0104
293.15	1.0000	0.0109
303.15	0.0000	0.0048
303.15	0.0990	0.0050
303.15	0.1999	0.0053
303.15	0.3001	0.0055
303.15	0.3995	0.0058
303.15	0.5006	0.0061
303.15	0.5987	0.0065
303.15	0.6993	0.0069
303.15	0.7990	0.0073
303.15	0.8992	0.0079
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- (2) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.424
293.15	0.0990	1.4406
293.15	0.1999	1.4582
293.15	0.3001	1.4766
293.15	0.3995	1.4957
293.15	0.5006	1.5159
293.15	0.5987	1.5368
293.15	0.6993	1.5594
293.15	0.7990	1.5831
293.15	0.8992	1.6083
293.15	1.0000	1.6354
303.15	0.0000	1.42
303.15	0.0990	1.4362
303.15	0.1999	1.4535
303.15	0.3001	1.4716
303.15	0.3995	1.4904
303.15	0.5006	1.5105
303.15	0.5987	1.5312
303.15	0.6993	1.5537
303.15	0.7990	1.5773
303.15	0.8992	1.6024
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- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	822.39
293.15	0.0990	1001.11
293.15	0.1999	1189.38
293.15	0.3001	1383.2
293.15	0.3995	1582.25
293.15	0.5006	1792.24
293.15	0.5987	2003.6
293.15	0.6993	2229.07
293.15	0.7990	2461.79
293.15	0.8992	2706.0
293.15	1.0000	2963.2
303.15	0.0000	815.41
303.15	0.0990	992.57
303.15	0.1999	1179.18
303.15	0.3001	1371.29
303.15	0.3995	1568.62
303.15	0.5006	1776.88
303.15	0.5987	1986.59
303.15	0.6993	2210.42
303.15	0.7990	2441.56
303.15	0.8992	2684.21
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- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	822.39
293.15	0.0990	1001.11
293.15	0.1999	1189.38
293.15	0.3001	1383.2
293.15	0.3995	1582.25
293.15	0.5006	1792.24
293.15	0.5987	2003.6
293.15	0.6993	2229.07
293.15	0.7990	2461.79
293.15	0.8992	2706.0
293.15	1.0000	2963.2
303.15	0.0000	815.41
303.15	0.0990	992.57
303.15	0.1999	1179.18
303.15	0.3001	1371.29
303.15	0.3995	1568.62
303.15	0.5006	1776.88
303.15	0.5987	1986.59
303.15	0.6993	2210.42
303.15	0.7990	2441.56
303.15	0.8992	2684.21
303.15	1.0000	2939.86

Sources

• Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures

Note: These property values are available through the Cheméo API. A free account gives you an access key.