Mixture of Benzene + 1-Propanol + Glycerin

Datasets

1. Temperature, K x Mole fraction (2)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Glycerin (3) - Liquid mixture 2	Mole fraction of Benzene (1) - Liquid mixture 2	Mole fraction of Glycerin (3) - Liquid mixture 1	Mole fraction of Benzene (1) - Liquid mixture 1
288.15	0.9914	0.0086	0.0000	1.0000
308.15	0.8346	0.0239	0.0152	0.7481
308.15	0.8236	0.0258	0.0295	0.6889
298.15	0.8573	0.0219	0.0000	0.8410
308.15	0.7990	0.0299	0.0350	0.6288
308.15	0.7904	0.0317	0.0610	0.5735
308.15	0.7603	0.0377	0.0571	0.5324
288.15	0.7524	0.0377	0.0980	0.4433
308.15	0.7478	0.0412	0.0915	0.4769
308.15	0.7256	0.0463	0.1040	0.4420
308.15	0.6982	0.0530	0.1390	0.4010
298.15	0.7197	0.0459	0.1310	0.4030
308.15	0.6764	0.0617	0.1630	0.3610
288.15	0.8673	0.0195	0.0000	0.8410
288.15	0.8316	0.0258	0.0160	0.7455
298.15	0.8393	0.0218	0.0134	0.7471
288.15	0.8215	0.0252	0.0250	0.6883
288.15	0.8070	0.0267	0.0499	0.5746
288.15	0.8047	0.0266	0.0390	0.6194
288.15	0.7868	0.0306	0.0620	0.5250
288.15	0.7383	0.0411	0.1030	0.4170
288.15	0.7210	0.0471	0.1230	0.3790
298.15	0.6992	0.0518	0.1350	0.3820
288.15	0.7058	0.0506	0.1680	0.3250
298.15	0.9914	0.0086	0.0000	1.0000
298.15	0.9314	0.0130	0.0000	0.9620
298.15	0.8815	0.0199	0.0000	0.9030
288.15	0.9276	0.0153	0.0000	0.9650
298.15	0.8267	0.0249	0.0275	0.6897
298.15	0.8025	0.0282	0.0371	0.6237
298.15	0.7905	0.0300	0.0531	0.5787
298.15	0.7759	0.0330	0.0672	0.5262
298.15	0.7449	0.0402	0.1150	0.4330
288.15	0.7716	0.0333	0.0786	0.4890
308.15	0.9907	0.0093	0.0000	1.0000
308.15	0.9351	0.0137	0.0000	0.9590
308.15	0.8911	0.0173	0.0010	0.8956
288.15	0.8865	0.0163	0.0000	0.9050
308.15	0.8717	0.0191	0.0000	0.8400

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Glycerin (3) - Liquid mixture 2	Mole fraction of Benzene (1) - Liquid mixture 2	Mole fraction of Glycerin (3) - Liquid mixture 1	Mole fraction of Benzene (1) - Liquid mixture 1
288.15	0.9914	0.0086	0.0000	1.0000
308.15	0.8346	0.0239	0.0152	0.7481
308.15	0.8236	0.0258	0.0295	0.6889
298.15	0.8573	0.0219	0.0000	0.8410
308.15	0.7990	0.0299	0.0350	0.6288
308.15	0.7904	0.0317	0.0610	0.5735
308.15	0.7603	0.0377	0.0571	0.5324
288.15	0.7524	0.0377	0.0980	0.4433
308.15	0.7478	0.0412	0.0915	0.4769
308.15	0.7256	0.0463	0.1040	0.4420
308.15	0.6982	0.0530	0.1390	0.4010
298.15	0.7197	0.0459	0.1310	0.4030
308.15	0.6764	0.0617	0.1630	0.3610
288.15	0.8673	0.0195	0.0000	0.8410
288.15	0.8316	0.0258	0.0160	0.7455
298.15	0.8393	0.0218	0.0134	0.7471
288.15	0.8215	0.0252	0.0250	0.6883
288.15	0.8070	0.0267	0.0499	0.5746
288.15	0.8047	0.0266	0.0390	0.6194
288.15	0.7868	0.0306	0.0620	0.5250
288.15	0.7383	0.0411	0.1030	0.4170
288.15	0.7210	0.0471	0.1230	0.3790
298.15	0.6992	0.0518	0.1350	0.3820
288.15	0.7058	0.0506	0.1680	0.3250
298.15	0.9914	0.0086	0.0000	1.0000
298.15	0.9314	0.0130	0.0000	0.9620
298.15	0.8815	0.0199	0.0000	0.9030
288.15	0.9276	0.0153	0.0000	0.9650
298.15	0.8267	0.0249	0.0275	0.6897
298.15	0.8025	0.0282	0.0371	0.6237
298.15	0.7905	0.0300	0.0531	0.5787
298.15	0.7759	0.0330	0.0672	0.5262
298.15	0.7449	0.0402	0.1150	0.4330
288.15	0.7716	0.0333	0.0786	0.4890
308.15	0.9907	0.0093	0.0000	1.0000
308.15	0.9351	0.0137	0.0000	0.9590
308.15	0.8911	0.0173	0.0010	0.8956
288.15	0.8865	0.0163	0.0000	0.9050
308.15	0.8717	0.0191	0.0000	0.8400

Sources

• Liquid Liquid Equilibria of Three Ternary Systems: {Glycerol + Benzene + Methanol}, {Glycerol + Benzene + Ethanol}, and {Glycerol + Benzene + 1-Propanol}