Mixture of Benzene, (trifluoromethyl)- + Ethanol + Water

Datasets

1. Mole fraction (4)

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
288.15	0.0797	0.2489
288.15	0.0903	0.2666
288.15	0.1023	0.2854
288.15	0.1165	0.3026
288.15	0.1327	0.3206
288.15	0.1515	0.3397
288.15	0.1740	0.3566
288.15	0.2000	0.3743
288.15	0.2581	0.4017
288.15	0.2832	0.4121
288.15	0.3030	0.4184
288.15	0.3245	0.4226
288.15	0.3388	0.4283
288.15	0.3599	0.4286
288.15	0.3839	0.4292
288.15	0.4154	0.4298
288.15	0.4430	0.4273
288.15	0.4722	0.4196
288.15	0.5029	0.4079
288.15	0.5297	0.3964
288.15	0.5577	0.3817
288.15	0.5867	0.3634
288.15	0.6148	0.3444
288.15	0.6383	0.3286
288.15	0.6619	0.3112
288.15	0.6857	0.2931
288.15	0.7001	0.2836
298.15	0.0108	0.0116
298.15	0.0908	0.2831
298.15	0.1109	0.3074
298.15	0.1314	0.3320
298.15	0.1597	0.3607
298.15	0.1992	0.3889
298.15	0.2298	0.4029
298.15	0.2440	0.4079
298.15	0.2701	0.4182
298.15	0.2873	0.4253
298.15	0.3146	0.4371
298.15	0.3460	0.4431
298.15	0.3828	0.4438
298.15	0.4227	0.4401
298.15	0.4693	0.4276
298.15	0.5226	0.4050
298.15	0.5721	0.3786
298.15	0.6146	0.3508
298.15	0.6464	0.3295
308.15	0.0604	0.1732
308.15	0.0981	0.2440
308.15	0.1257	0.2731
308.15	0.1762	0.3276
308.15	0.1890	0.3345
308.15	0.1900	0.3331
308.15	0.2369	0.3661
308.15	0.2597	0.3702
308.15	0.3033	0.3824
308.15	0.3179	0.3839
308.15	0.3544	0.3864
308.15	0.4067	0.3881
308.15	0.4626	0.3757
308.15	0.5172	0.3568
308.15	0.5789	0.3235
308.15	0.6445	0.2820
308.15	0.7012	0.2444
308.15	0.7593	0.2008
308.15	0.8160	0.1547
308.15	0.8863	0.0962

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
288.15	0.4460	0.4368	0.3668	0.1682
288.15	0.4970	0.4158	0.3360	0.1282
288.15	0.5950	0.3655	0.2723	0.0719
288.15	0.6500	0.3280	0.2293	0.0459
288.15	0.7030	0.2846	0.1867	0.0270
288.15	0.7580	0.2370	0.1431	0.0055
288.15	0.8075	0.1925	0.1003	0.0048
288.15	0.8512	0.1488	0.0527	0.0027
288.15	0.2993	0.4372	0.4372	0.2993
298.15	0.4790	0.4266	0.3681	0.1805
298.15	0.5195	0.4050	0.3296	0.1414
298.15	0.5683	0.3732	0.2852	0.0993
298.15	0.6328	0.3307	0.2298	0.0629
298.15	0.7208	0.2678	0.1574	0.0335
298.15	0.7506	0.2386	0.1312	0.0221
298.15	0.7805	0.2093	0.0947	0.0051
298.15	0.8596	0.1388	0.0299	0.0030
298.15	0.3274	0.4301	0.4301	0.3274
308.15	0.4890	0.3703	0.3304	0.1684
308.15	0.5425	0.3484	0.3070	0.1433
308.15	0.5781	0.3269	0.2793	0.1256
308.15	0.6452	0.2812	0.2291	0.0861
308.15	0.6901	0.2483	0.1932	0.0677
308.15	0.7536	0.2010	0.1500	0.0399
308.15	0.8310	0.1398	0.0949	0.0223
308.15	0.8908	0.0974	0.0488	0.0078
308.15	0.3254	0.3902	0.3902	0.3254

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
288.15	0.0797	0.2489
288.15	0.0903	0.2666
288.15	0.1023	0.2854
288.15	0.1165	0.3026
288.15	0.1327	0.3206
288.15	0.1515	0.3397
288.15	0.1740	0.3566
288.15	0.2000	0.3743
288.15	0.2581	0.4017
288.15	0.2832	0.4121
288.15	0.3030	0.4184
288.15	0.3245	0.4226
288.15	0.3388	0.4283
288.15	0.3599	0.4286
288.15	0.3839	0.4292
288.15	0.4154	0.4298
288.15	0.4430	0.4273
288.15	0.4722	0.4196
288.15	0.5029	0.4079
288.15	0.5297	0.3964
288.15	0.5577	0.3817
288.15	0.5867	0.3634
288.15	0.6148	0.3444
288.15	0.6383	0.3286
288.15	0.6619	0.3112
288.15	0.6857	0.2931
288.15	0.7001	0.2836
298.15	0.0108	0.0116
298.15	0.0908	0.2831
298.15	0.1109	0.3074
298.15	0.1314	0.3320
298.15	0.1597	0.3607
298.15	0.1992	0.3889
298.15	0.2298	0.4029
298.15	0.2440	0.4079
298.15	0.2701	0.4182
298.15	0.2873	0.4253
298.15	0.3146	0.4371
298.15	0.3460	0.4431
298.15	0.3828	0.4438
298.15	0.4227	0.4401
298.15	0.4693	0.4276
298.15	0.5226	0.4050
298.15	0.5721	0.3786
298.15	0.6146	0.3508
298.15	0.6464	0.3295
308.15	0.0604	0.1732
308.15	0.0981	0.2440
308.15	0.1257	0.2731
308.15	0.1762	0.3276
308.15	0.1890	0.3345
308.15	0.1900	0.3331
308.15	0.2369	0.3661
308.15	0.2597	0.3702
308.15	0.3033	0.3824
308.15	0.3179	0.3839
308.15	0.3544	0.3864
308.15	0.4067	0.3881
308.15	0.4626	0.3757
308.15	0.5172	0.3568
308.15	0.5789	0.3235
308.15	0.6445	0.2820
308.15	0.7012	0.2444
308.15	0.7593	0.2008
308.15	0.8160	0.1547
308.15	0.8863	0.0962

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
288.15	0.4460	0.4368	0.3668	0.1682
288.15	0.4970	0.4158	0.3360	0.1282
288.15	0.5950	0.3655	0.2723	0.0719
288.15	0.6500	0.3280	0.2293	0.0459
288.15	0.7030	0.2846	0.1867	0.0270
288.15	0.7580	0.2370	0.1431	0.0055
288.15	0.8075	0.1925	0.1003	0.0048
288.15	0.8512	0.1488	0.0527	0.0027
288.15	0.2993	0.4372	0.4372	0.2993
298.15	0.4790	0.4266	0.3681	0.1805
298.15	0.5195	0.4050	0.3296	0.1414
298.15	0.5683	0.3732	0.2852	0.0993
298.15	0.6328	0.3307	0.2298	0.0629
298.15	0.7208	0.2678	0.1574	0.0335
298.15	0.7506	0.2386	0.1312	0.0221
298.15	0.7805	0.2093	0.0947	0.0051
298.15	0.8596	0.1388	0.0299	0.0030
298.15	0.3274	0.4301	0.4301	0.3274
308.15	0.4890	0.3703	0.3304	0.1684
308.15	0.5425	0.3484	0.3070	0.1433
308.15	0.5781	0.3269	0.2793	0.1256
308.15	0.6452	0.2812	0.2291	0.0861
308.15	0.6901	0.2483	0.1932	0.0677
308.15	0.7536	0.2010	0.1500	0.0399
308.15	0.8310	0.1398	0.0949	0.0223
308.15	0.8908	0.0974	0.0488	0.0078
308.15	0.3254	0.3902	0.3902	0.3254

Sources

• Solubilities and liquid liquid equilibria of (water + ethanol + a,a,a-trifluorotoluene) at temperatures T = (288.15, 298.15, and 308.15) K and pressure p = 101.2 kPa