Mixture of Benzene + Tetrachloroethylene

Datasets

1. η - Viscosity, Pa*s
2. P_vap - Vapor or sublimation pressure, kPa
3. ρ_l - Mass density, kg/m3

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrachloroethylene (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0006
0.0883	0.0006
0.1788	0.0006
0.2720	0.0006
0.3674	0.0007
0.4655	0.0007
0.5671	0.0007
0.6706	0.0007
0.7770	0.0008
0.8873	0.0008
1.0000	0.0008

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrachloroethylene (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
283.15	0.0798	5.76
283.15	0.1262	5.54
283.15	0.2205	5.14
283.15	0.3153	4.72
283.15	0.3909	4.39
283.15	0.4419	4.16
283.15	0.4981	3.91
283.15	0.6046	3.41
283.15	0.6779	3.03
283.15	0.7759	2.48
283.15	0.8844	1.80
288.15	0.0798	7.42
288.15	0.1262	7.14
288.15	0.2206	6.63
288.15	0.3154	6.10
288.15	0.3909	5.68
288.15	0.4420	5.41
288.15	0.4982	5.06
288.15	0.6047	4.42
288.15	0.6780	3.92
288.15	0.7760	3.23
288.15	0.8844	2.40
293.15	0.0799	9.45
293.15	0.1262	9.12
293.15	0.2207	8.48
293.15	0.3154	7.81
293.15	0.3911	7.27
293.15	0.4422	6.91
293.15	0.4984	6.49
293.15	0.6047	5.64
293.15	0.6780	5.04
293.15	0.7761	4.16
293.15	0.8845	3.12
298.15	0.0799	11.98
298.15	0.1262	11.59
298.15	0.2207	10.75
298.15	0.3155	9.89
298.15	0.3912	9.22
298.15	0.4426	8.75
298.15	0.4986	8.22
298.15	0.6049	7.20
298.15	0.6781	6.44
298.15	0.7762	5.31
298.15	0.8845	4.00
303.15	0.0799	15.07
303.15	0.1262	14.55
303.15	0.2206	13.52
303.15	0.3154	12.47
303.15	0.3915	11.60
303.15	0.4431	11.00
303.15	0.4989	10.34
303.15	0.6050	9.04
303.15	0.6782	8.11
303.15	0.7765	6.73
303.15	0.8846	5.12
308.15	0.0799	18.72
308.15	0.1262	18.10
308.15	0.2207	16.82
308.15	0.3155	15.51
308.15	0.3912	14.47
308.15	0.4426	13.75
308.15	0.4994	12.87
308.15	0.6052	11.29
308.15	0.6784	10.13
308.15	0.7767	8.46
308.15	0.8848	6.47
313.15	0.0799	23.06
313.15	0.1262	22.31
313.15	0.2208	20.75
313.15	0.3155	19.14
313.15	0.3914	17.89
313.15	0.4431	16.96
313.15	0.4988	15.97
313.15	0.6050	13.98
313.15	0.6786	12.54
313.15	0.7771	10.48
313.15	0.8849	8.10
318.15	0.0799	28.22
318.15	0.1263	27.27
318.15	0.2208	25.36
318.15	0.3157	23.42
318.15	0.3916	21.84
318.15	0.4432	20.76
318.15	0.4990	19.59
318.15	0.6051	17.16
318.15	0.6783	15.47
318.15	0.7776	12.91
318.15	0.8851	10.04
323.15	0.0800	34.23
323.15	0.1264	33.07
323.15	0.2210	30.84
323.15	0.3157	28.57
323.15	0.3917	26.65
323.15	0.4438	25.20
323.15	0.4994	23.84
323.15	0.6052	20.90
323.15	0.6784	18.86
323.15	0.7769	15.88
323.15	0.8855	12.30

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrachloroethylene (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	869.7
0.0883	939.8
0.1788	1011.5
0.2720	1084.6
0.3674	1156.7
0.4655	1228.8
0.5671	1302.3
0.6706	1377.4
0.7770	1453.2
0.8873	1531.7
1.0000	1610.2

Sources

• Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents

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