Mixture of Benzene + n-Hexane + Benzene, 1,3-dichloro-

Datasets

1. Excess molar enthalpy (molar enthalpy (2)
2. ρ_l - Mass density, kg/m3 (2)

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

Operational conditions:

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

Fixed		Measured
Solvent: Amount ratio of component to other component of binary solvent of Benzene, 1,3-dichloro- (3) - Liquid	Mole fraction of n-Hexane (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.3266	0.0365	0.1180
0.3266	0.0661	0.2080
0.3266	0.1142	0.3290
0.3266	0.1542	0.4110
0.3266	0.1886	0.4820
0.3266	0.2431	0.5780
0.3266	0.3192	0.6630
0.3266	0.3504	0.6880
0.3266	0.4333	0.7290
0.3266	0.4908	0.7450
0.3266	0.5275	0.7400
0.3266	0.5743	0.7260
0.3266	0.6265	0.6890
0.3266	0.6837	0.6310
0.3266	0.7352	0.5650
0.3266	0.8055	0.4490
0.3266	0.8856	0.2790
0.3266	0.9359	0.1670
1.0169	0.0456	0.1270
1.0169	0.0831	0.2000
1.0169	0.1192	0.2850
1.0169	0.1587	0.3660
1.0169	0.2134	0.4580
1.0169	0.2767	0.5220
1.0169	0.3403	0.6020
1.0169	0.3853	0.6300
1.0169	0.4472	0.6490
1.0169	0.4813	0.6560
1.0169	0.5510	0.6530
1.0169	0.6587	0.6120
1.0169	0.7027	0.5460
1.0169	0.7715	0.4590
1.0169	0.8703	0.3100
1.0169	0.9290	0.1810
3.1701	0.0450	0.1050
3.1701	0.0770	0.1770
3.1701	0.1268	0.2790
3.1701	0.1572	0.3430
3.1701	0.2077	0.4290
3.1701	0.2501	0.4800
3.1701	0.3106	0.5390
3.1701	0.3498	0.5710
3.1701	0.3945	0.6060
3.1701	0.4443	0.6210
3.1701	0.5199	0.6260
3.1701	0.5648	0.6110
3.1701	0.6093	0.6020
3.1701	0.6567	0.5620
3.1701	0.7096	0.5170
3.1701	0.7687	0.4500
3.1701	0.8246	0.3710
3.1701	0.8749	0.2840
3.1701	0.9228	0.1930

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

Operational conditions:

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

Fixed		Measured
Solvent: Amount ratio of component to other component of binary solvent of Benzene, 1,3-dichloro- (3) - Liquid	Mole fraction of n-Hexane (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.3266	0.0365	0.1180
0.3266	0.0661	0.2080
0.3266	0.1142	0.3290
0.3266	0.1542	0.4110
0.3266	0.1886	0.4820
0.3266	0.2431	0.5780
0.3266	0.3192	0.6630
0.3266	0.3504	0.6880
0.3266	0.4333	0.7290
0.3266	0.4908	0.7450
0.3266	0.5275	0.7400
0.3266	0.5743	0.7260
0.3266	0.6265	0.6890
0.3266	0.6837	0.6310
0.3266	0.7352	0.5650
0.3266	0.8055	0.4490
0.3266	0.8856	0.2790
0.3266	0.9359	0.1670
1.0169	0.0456	0.1270
1.0169	0.0831	0.2000
1.0169	0.1192	0.2850
1.0169	0.1587	0.3660
1.0169	0.2134	0.4580
1.0169	0.2767	0.5220
1.0169	0.3403	0.6020
1.0169	0.3853	0.6300
1.0169	0.4472	0.6490
1.0169	0.4813	0.6560
1.0169	0.5510	0.6530
1.0169	0.6587	0.6120
1.0169	0.7027	0.5460
1.0169	0.7715	0.4590
1.0169	0.8703	0.3100
1.0169	0.9290	0.1810
3.1701	0.0450	0.1050
3.1701	0.0770	0.1770
3.1701	0.1268	0.2790
3.1701	0.1572	0.3430
3.1701	0.2077	0.4290
3.1701	0.2501	0.4800
3.1701	0.3106	0.5390
3.1701	0.3498	0.5710
3.1701	0.3945	0.6060
3.1701	0.4443	0.6210
3.1701	0.5199	0.6260
3.1701	0.5648	0.6110
3.1701	0.6093	0.6020
3.1701	0.6567	0.5620
3.1701	0.7096	0.5170
3.1701	0.7687	0.4500
3.1701	0.8246	0.3710
3.1701	0.8749	0.2840
3.1701	0.9228	0.1930

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of Benzene, 1,3-dichloro- (3) - Liquid	Mole fraction of Benzene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0183	0.1009	680.66
0.0310	0.1704	699.42
0.0351	0.0815	687.33
0.0519	0.2855	732.66
0.0590	0.0717	699.72
0.0612	0.1421	712.71
0.0718	0.3949	767.31
0.0777	0.0250	703.27
0.0781	0.0517	707.79
0.0810	0.0984	717.12
0.0894	0.0076	707.3
0.0898	0.4936	801.42
0.0962	0.5288	814.23
0.0988	0.2296	751.62
0.1009	0.0669	723.74
0.1091	0.6001	841.52
0.1243	0.6838	875.68
0.1300	0.0419	736.67
0.1319	0.0112	732.6
0.1401	0.1701	765.95
0.1405	0.7725	914.72
0.1476	0.3432	806.53
0.1713	0.3982	835.15
0.1847	0.4294	851.89
0.1890	0.1253	787.63
0.2117	0.2571	829.48
0.2120	0.4927	887.43
0.2283	0.0735	801.48
0.2409	0.5599	851.54
0.2538	0.0216	806.76
0.2597	0.3154	875.01
0.2732	0.6351	974.52
0.2763	0.1831	854.77
0.2800	0.3400	894.88
0.3391	0.2247	905.61
0.3446	0.4186	961.5
0.3448	0.1111	882.11
0.3704	0.2454	931.74
0.3705	0.4500	989.49
0.3885	0.0330	891.66
0.4124	0.5009	1036.26
0.4143	0.2745	969.33
0.4186	0.1348	935.17
0.4617	0.1487	966.92
0.4827	0.3198	1030.08
0.5145	0.0437	973.82
0.5199	0.1675	1010.8
0.5466	0.3622	1089.24
0.5621	0.0478	1005.55
0.6068	0.1955	1078.15
0.6214	0.0528	1045.54
0.6814	0.2195	1137.93
0.7441	0.0632	1130.18
0.8393	0.0713	1197.53

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of Benzene, 1,3-dichloro- (3) - Liquid	Mole fraction of Benzene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0183	0.1009	680.66
0.0310	0.1704	699.42
0.0351	0.0815	687.33
0.0519	0.2855	732.66
0.0590	0.0717	699.72
0.0612	0.1421	712.71
0.0718	0.3949	767.31
0.0777	0.0250	703.27
0.0781	0.0517	707.79
0.0810	0.0984	717.12
0.0894	0.0076	707.3
0.0898	0.4936	801.42
0.0962	0.5288	814.23
0.0988	0.2296	751.62
0.1009	0.0669	723.74
0.1091	0.6001	841.52
0.1243	0.6838	875.68
0.1300	0.0419	736.67
0.1319	0.0112	732.6
0.1401	0.1701	765.95
0.1405	0.7725	914.72
0.1476	0.3432	806.53
0.1713	0.3982	835.15
0.1847	0.4294	851.89
0.1890	0.1253	787.63
0.2117	0.2571	829.48
0.2120	0.4927	887.43
0.2283	0.0735	801.48
0.2409	0.5599	851.54
0.2538	0.0216	806.76
0.2597	0.3154	875.01
0.2732	0.6351	974.52
0.2763	0.1831	854.77
0.2800	0.3400	894.88
0.3391	0.2247	905.61
0.3446	0.4186	961.5
0.3448	0.1111	882.11
0.3704	0.2454	931.74
0.3705	0.4500	989.49
0.3885	0.0330	891.66
0.4124	0.5009	1036.26
0.4143	0.2745	969.33
0.4186	0.1348	935.17
0.4617	0.1487	966.92
0.4827	0.3198	1030.08
0.5145	0.0437	973.82
0.5199	0.1675	1010.8
0.5466	0.3622	1089.24
0.5621	0.0478	1005.55
0.6068	0.1955	1078.15
0.6214	0.0528	1045.54
0.6814	0.2195	1137.93
0.7441	0.0632	1130.18
0.8393	0.0713	1197.53

Sources

• Measurement and Prediction of Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,3-dichlorobenzene + Benzene + Hexane at 298.15 K.