Mixture of Benzene + Ethane, 1,1,2,2-tetrachloro-

Datasets

1. Excess molar enthalpy (molar enthalpy
2. P_vap - Vapor or sublimation pressure, kPa

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0955	-0.1890
0.1744	-0.3110
0.2406	-0.4060
0.2970	-0.4790
0.3879	-0.5620
0.4580	-0.5990
0.5298	-0.5970
0.5590	-0.5760
0.6283	-0.5570
0.6926	-0.5110
0.7171	-0.4780
0.7717	-0.3970
0.8942	-0.2080

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
283.15	0.0679	5.67
283.15	0.1613	5.07
283.15	0.2371	4.55
283.15	0.3366	3.90
283.15	0.4657	3.06
283.15	0.5502	2.53
283.15	0.6470	1.96
283.15	0.6595	1.89
283.15	0.7771	1.24
283.15	0.8391	0.95
283.15	0.9212	0.57
288.15	0.0680	7.31
288.15	0.1613	6.55
288.15	0.2372	5.90
288.15	0.3367	5.05
288.15	0.4658	3.97
288.15	0.5503	3.29
288.15	0.6471	2.56
288.15	0.6595	2.46
288.15	0.7771	1.66
288.15	0.8392	1.27
288.15	0.9212	0.79
293.15	0.0680	9.36
293.15	0.1614	8.39
293.15	0.2373	7.56
293.15	0.3369	6.47
293.15	0.4659	5.10
293.15	0.5504	4.25
293.15	0.6472	3.32
293.15	0.6596	3.20
293.15	0.7772	2.17
293.15	0.8392	1.65
293.15	0.9212	1.06
298.15	0.0680	11.85
298.15	0.1614	10.65
298.15	0.2375	9.58
298.15	0.3372	8.23
298.15	0.4660	6.52
298.15	0.5506	5.43
298.15	0.6473	4.25
298.15	0.6597	4.10
298.15	0.7773	2.80
298.15	0.8393	2.18
298.15	0.9213	1.40
303.15	0.0680	14.89
303.15	0.1616	13.35
303.15	0.2377	12.06
303.15	0.3375	10.36
303.15	0.4663	8.22
303.15	0.5509	6.91
303.15	0.6475	5.39
303.15	0.6599	5.23
303.15	0.7774	3.62
303.15	0.8395	2.82
303.15	0.9213	1.83
308.15	0.0680	18.49
308.15	0.1615	16.65
308.15	0.2375	15.04
308.15	0.3380	12.92
308.15	0.4666	10.30
308.15	0.5512	8.63
308.15	0.6478	6.81
308.15	0.6600	6.57
308.15	0.7776	4.61
308.15	0.8396	3.60
308.15	0.9214	2.35
313.15	0.0680	22.80
313.15	0.1615	20.53
313.15	0.2376	18.57
313.15	0.3375	16.04
313.15	0.4663	12.79
313.15	0.5517	10.70
313.15	0.6482	8.50
313.15	0.6603	8.22
313.15	0.7778	5.79
313.15	0.8397	4.52
313.15	0.9215	3.04
318.15	0.0681	27.88
318.15	0.1616	25.08
318.15	0.2379	22.71
318.15	0.3378	19.62
318.15	0.4666	15.71
318.15	0.5512	13.27
318.15	0.6486	10.51
318.15	0.6606	10.19
318.15	0.7781	7.20
318.15	0.8400	5.67
318.15	0.9216	3.86
323.15	0.0681	33.85
323.15	0.1616	30.44
323.15	0.2381	27.64
323.15	0.3382	23.85
323.15	0.4669	19.15
323.15	0.5515	16.23
323.15	0.6493	12.86
323.15	0.6610	12.50
323.15	0.7785	8.88
323.15	0.8403	7.04
323.15	0.9217	4.84

Sources

• Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
• Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies

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