Mixture of Benzene + Ethanol + 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 2	Mole fraction of Benzene (1) - Liquid mixture 1	Mole fraction of Glycerin (3) - Liquid mixture 1	Mole fraction of Benzene (1) - Liquid mixture 2	Mole fraction of Glycerin (3) - Liquid mixture 2
288.15	1.0000	0.0000	0.0086	0.9914
288.15	0.8838	0.0016	0.0333	0.7044
288.15	0.8478	0.0032	0.0390	0.6713
308.15	1.0000	0.0000	0.0093	0.9907
288.15	0.7886	0.0082	0.0515	0.6158
288.15	0.7475	0.0154	0.0578	0.5956
288.15	0.7031	0.0163	0.0728	0.5423
298.15	0.7801	0.0092	0.0513	0.6205
288.15	0.5326	0.0682	0.1230	0.4370
298.15	1.0000	0.0000	0.0086	0.9914
298.15	0.9750	0.0000	0.0163	0.8791
308.15	0.7704	0.0135	0.0534	0.6258
298.15	0.9500	0.0000	0.0195	0.8230
298.15	0.9200	0.0000	0.0232	0.7725
298.15	0.8756	0.0019	0.0324	0.7164
308.15	0.9710	0.0000	0.0153	0.8857
288.15	0.9780	0.0000	0.0138	0.8864
298.15	0.7377	0.0174	0.0626	0.5832
298.15	0.6939	0.0193	0.0711	0.5633
298.15	0.6467	0.0349	0.0857	0.5195
298.15	0.5718	0.0499	0.1120	0.4580
298.15	0.5256	0.0671	0.1310	0.4290
308.15	0.7312	0.0149	0.0641	0.5851
288.15	0.6549	0.0324	0.0815	0.5247
308.15	0.9450	0.0000	0.0194	0.8292
308.15	0.9130	0.0000	0.0238	0.7815
308.15	0.8690	0.0024	0.0337	0.7168
288.15	0.9560	0.0000	0.0218	0.8060
308.15	0.8273	0.0071	0.0416	0.6746
298.15	0.8392	0.0034	0.0387	0.6789
308.15	0.6806	0.0249	0.0772	0.5484
308.15	0.6409	0.0321	0.0906	0.5120
308.15	0.5553	0.0695	0.1170	0.4590
288.15	0.5870	0.0432	0.1070	0.4620
288.15	0.9270	0.0000	0.0247	0.7639

Temperature, K x Mole fraction [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 2	Mole fraction of Benzene (1) - Liquid mixture 1	Mole fraction of Glycerin (3) - Liquid mixture 1	Mole fraction of Benzene (1) - Liquid mixture 2	Mole fraction of Glycerin (3) - Liquid mixture 2
288.15	1.0000	0.0000	0.0086	0.9914
288.15	0.8838	0.0016	0.0333	0.7044
288.15	0.8478	0.0032	0.0390	0.6713
308.15	1.0000	0.0000	0.0093	0.9907
288.15	0.7886	0.0082	0.0515	0.6158
288.15	0.7475	0.0154	0.0578	0.5956
288.15	0.7031	0.0163	0.0728	0.5423
298.15	0.7801	0.0092	0.0513	0.6205
288.15	0.5326	0.0682	0.1230	0.4370
298.15	1.0000	0.0000	0.0086	0.9914
298.15	0.9750	0.0000	0.0163	0.8791
308.15	0.7704	0.0135	0.0534	0.6258
298.15	0.9500	0.0000	0.0195	0.8230
298.15	0.9200	0.0000	0.0232	0.7725
298.15	0.8756	0.0019	0.0324	0.7164
308.15	0.9710	0.0000	0.0153	0.8857
288.15	0.9780	0.0000	0.0138	0.8864
298.15	0.7377	0.0174	0.0626	0.5832
298.15	0.6939	0.0193	0.0711	0.5633
298.15	0.6467	0.0349	0.0857	0.5195
298.15	0.5718	0.0499	0.1120	0.4580
298.15	0.5256	0.0671	0.1310	0.4290
308.15	0.7312	0.0149	0.0641	0.5851
288.15	0.6549	0.0324	0.0815	0.5247
308.15	0.9450	0.0000	0.0194	0.8292
308.15	0.9130	0.0000	0.0238	0.7815
308.15	0.8690	0.0024	0.0337	0.7168
288.15	0.9560	0.0000	0.0218	0.8060
308.15	0.8273	0.0071	0.0416	0.6746
298.15	0.8392	0.0034	0.0387	0.6789
308.15	0.6806	0.0249	0.0772	0.5484
308.15	0.6409	0.0321	0.0906	0.5120
308.15	0.5553	0.0695	0.1170	0.4590
288.15	0.5870	0.0432	0.1070	0.4620
288.15	0.9270	0.0000	0.0247	0.7639

Sources

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