Mixture of n-Hexane + Ethyl Acetate

Datasets

1. Mole fraction (4)
2. Excess molar enthalpy (molar enthalpy (4)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (4)
5. c_sound,fluid - Speed of Sound, m/s (2)
6. T_boil - Boiling temperature at pressure P, K (2)
7. Vapor Liquid Equilibrium at Constant Pressure (2)
8. Vapor Liquid Equilibrium at Constant Temperature
9. Azeotropic temperature, K (2)

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	0.0000
0.0110	0.0180
0.0320	0.0510
0.0630	0.0970
0.1010	0.1450
0.1510	0.1990
0.2090	0.2530
0.2870	0.3060
0.3560	0.3510
0.4240	0.3890
0.4850	0.4220
0.5410	0.4520
0.6000	0.4820
0.6440	0.4900
0.6970	0.5450
0.7300	0.5740
0.7700	0.6050
0.8140	0.6540
0.8590	0.7150
0.8950	0.7710
0.9260	0.8250
0.9470	0.8720
0.9730	0.9150
1.0000	1.0000

Azeotropic composition: mole fraction of Ethyl Acetate (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethyl Acetate (2) - Liquid
101.32	0.3390

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	0.0000
0.0110	0.0180
0.0320	0.0510
0.0630	0.0970
0.1010	0.1450
0.1510	0.1990
0.2090	0.2530
0.2870	0.3060
0.3560	0.3510
0.4240	0.3890
0.4850	0.4220
0.5410	0.4520
0.6000	0.4820
0.6440	0.4900
0.6970	0.5450
0.7300	0.5740
0.7700	0.6050
0.8140	0.6540
0.8590	0.7150
0.8950	0.7710
0.9260	0.8250
0.9470	0.8720
0.9730	0.9150
1.0000	1.0000

Azeotropic composition: mole fraction of Ethyl Acetate (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethyl Acetate (2) - Liquid
101.32	0.3390

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

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of n-Hexane (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
363.15	1583.00	0.0377	0.1757
363.15	1583.00	0.0764	0.3562
363.15	1583.00	0.1162	0.5337
363.15	1583.00	0.1570	0.6871
363.15	1583.00	0.1989	0.8208
363.15	1583.00	0.2420	0.9528
363.15	1583.00	0.2862	1.0607
363.15	1583.00	0.3318	1.1494
363.15	1583.00	0.3786	1.2203
363.15	1583.00	0.4269	1.2763
363.15	1583.00	0.4765	1.2929
363.15	1583.00	0.5277	1.2963
363.15	1583.00	0.5804	1.2705
363.15	1583.00	0.6347	1.2183
363.15	1583.00	0.6908	1.1162
363.15	1583.00	0.7487	0.9923
363.15	1583.00	0.8084	0.8244
363.15	1583.00	0.8702	0.6094
363.15	1583.00	0.9340	0.3342
413.15	1376.00	0.0377	0.1894
413.15	1376.00	0.0765	0.3612
413.15	1376.00	0.1162	0.5274
413.15	1376.00	0.1571	0.6794
413.15	1376.00	0.1990	0.8151
413.15	1376.00	0.2421	0.9385
413.15	1376.00	0.2864	1.0481
413.15	1376.00	0.3320	1.1359
413.15	1376.00	0.3788	1.2056
413.15	1376.00	0.4270	1.2589
413.15	1376.00	0.4767	1.2771
413.15	1376.00	0.5279	1.2793
413.15	1376.00	0.5806	1.2545
413.15	1376.00	0.6349	1.2041
413.15	1376.00	0.6910	1.1144
413.15	1376.00	0.7488	0.9886
413.15	1376.00	0.8086	0.8186
413.15	1376.00	0.8703	0.6027
413.15	1376.00	0.9340	0.3298

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
291.15	0.0535	0.2820
291.15	0.1148	0.5810
291.15	0.1974	0.9010
291.15	0.2736	1.149
291.15	0.3368	1.293
291.15	0.3855	1.381
291.15	0.4401	1.44
291.15	0.4918	1.456
291.15	0.5333	1.443
291.15	0.5714	1.425
291.15	0.6212	1.378
291.15	0.6753	1.294
291.15	0.7220	1.181
291.15	0.7805	1.032
291.15	0.8412	0.8340
291.15	0.8816	0.6410
291.15	0.9343	0.3920
291.15	0.9802	0.1460
298.15	0.0668	0.3620
298.15	0.1168	0.5720
298.15	0.1920	0.8780
298.15	0.2621	1.094
298.15	0.3186	1.21
298.15	0.3929	1.334
298.15	0.4390	1.375
298.15	0.4950	1.364
298.15	0.5309	1.357
298.15	0.5767	1.319
298.15	0.6196	1.271
298.15	0.6757	1.195
298.15	0.7368	1.065
298.15	0.7954	0.8990
298.15	0.8424	0.7100
298.15	0.8998	0.4900
298.15	0.9521	0.2530
318.15	0.0760	0.4620
318.15	0.1524	0.8150
318.15	0.2306	1.084
318.15	0.3029	1.256
318.15	0.3659	1.36
318.15	0.4345	1.419
318.15	0.4880	1.415
318.15	0.5143	1.403
318.15	0.5368	1.393
318.15	0.5617	1.384
318.15	0.6098	1.339
318.15	0.6645	1.259
318.15	0.7202	1.144
318.15	0.7788	0.9840
318.15	0.8406	0.7680
318.15	0.9004	0.5230
318.15	0.9547	0.2670

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

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of n-Hexane (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
363.15	1583.00	0.0377	0.1757
363.15	1583.00	0.0764	0.3562
363.15	1583.00	0.1162	0.5337
363.15	1583.00	0.1570	0.6871
363.15	1583.00	0.1989	0.8208
363.15	1583.00	0.2420	0.9528
363.15	1583.00	0.2862	1.0607
363.15	1583.00	0.3318	1.1494
363.15	1583.00	0.3786	1.2203
363.15	1583.00	0.4269	1.2763
363.15	1583.00	0.4765	1.2929
363.15	1583.00	0.5277	1.2963
363.15	1583.00	0.5804	1.2705
363.15	1583.00	0.6347	1.2183
363.15	1583.00	0.6908	1.1162
363.15	1583.00	0.7487	0.9923
363.15	1583.00	0.8084	0.8244
363.15	1583.00	0.8702	0.6094
363.15	1583.00	0.9340	0.3342
413.15	1376.00	0.0377	0.1894
413.15	1376.00	0.0765	0.3612
413.15	1376.00	0.1162	0.5274
413.15	1376.00	0.1571	0.6794
413.15	1376.00	0.1990	0.8151
413.15	1376.00	0.2421	0.9385
413.15	1376.00	0.2864	1.0481
413.15	1376.00	0.3320	1.1359
413.15	1376.00	0.3788	1.2056
413.15	1376.00	0.4270	1.2589
413.15	1376.00	0.4767	1.2771
413.15	1376.00	0.5279	1.2793
413.15	1376.00	0.5806	1.2545
413.15	1376.00	0.6349	1.2041
413.15	1376.00	0.6910	1.1144
413.15	1376.00	0.7488	0.9886
413.15	1376.00	0.8086	0.8186
413.15	1376.00	0.8703	0.6027
413.15	1376.00	0.9340	0.3298

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
291.15	0.0535	0.2820
291.15	0.1148	0.5810
291.15	0.1974	0.9010
291.15	0.2736	1.149
291.15	0.3368	1.293
291.15	0.3855	1.381
291.15	0.4401	1.44
291.15	0.4918	1.456
291.15	0.5333	1.443
291.15	0.5714	1.425
291.15	0.6212	1.378
291.15	0.6753	1.294
291.15	0.7220	1.181
291.15	0.7805	1.032
291.15	0.8412	0.8340
291.15	0.8816	0.6410
291.15	0.9343	0.3920
291.15	0.9802	0.1460
298.15	0.0668	0.3620
298.15	0.1168	0.5720
298.15	0.1920	0.8780
298.15	0.2621	1.094
298.15	0.3186	1.21
298.15	0.3929	1.334
298.15	0.4390	1.375
298.15	0.4950	1.364
298.15	0.5309	1.357
298.15	0.5767	1.319
298.15	0.6196	1.271
298.15	0.6757	1.195
298.15	0.7368	1.065
298.15	0.7954	0.8990
298.15	0.8424	0.7100
298.15	0.8998	0.4900
298.15	0.9521	0.2530
318.15	0.0760	0.4620
318.15	0.1524	0.8150
318.15	0.2306	1.084
318.15	0.3029	1.256
318.15	0.3659	1.36
318.15	0.4345	1.419
318.15	0.4880	1.415
318.15	0.5143	1.403
318.15	0.5368	1.393
318.15	0.5617	1.384
318.15	0.6098	1.339
318.15	0.6645	1.259
318.15	0.7202	1.144
318.15	0.7788	0.9840
318.15	0.8406	0.7680
318.15	0.9004	0.5230
318.15	0.9547	0.2670

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3724
293.15	0.0469	1.3719
293.15	0.0969	1.3716
293.15	0.1898	1.3711
293.15	0.2962	1.3706
293.15	0.3907	1.3705
293.15	0.5028	1.3707
293.15	0.5980	1.371
293.15	0.6995	1.3718
293.15	0.8030	1.3727
293.15	0.9005	1.3738
293.15	0.9514	1.3744
293.15	1.0000	1.3749
298.15	0.0000	1.3698
298.15	0.0469	1.3693
298.15	0.0969	1.3689
298.15	0.1898	1.3683
298.15	0.2962	1.3679
298.15	0.3907	1.3678
298.15	0.5028	1.3679
298.15	0.5980	1.3682
298.15	0.6995	1.369
298.15	0.8030	1.3698
298.15	0.9005	1.371
298.15	0.9514	1.3716
298.15	1.0000	1.3722
303.15	0.0000	1.3671
303.15	0.0469	1.3666
303.15	0.0969	1.3662
303.15	0.1898	1.3656
303.15	0.2962	1.3651
303.15	0.3907	1.365
303.15	0.5028	1.3651
303.15	0.5980	1.3655
303.15	0.6995	1.3661
303.15	0.8030	1.3669
303.15	0.9005	1.368
303.15	0.9514	1.3687
303.15	1.0000	1.3694

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3724
293.15	0.0469	1.3719
293.15	0.0969	1.3716
293.15	0.1898	1.3711
293.15	0.2962	1.3706
293.15	0.3907	1.3705
293.15	0.5028	1.3707
293.15	0.5980	1.371
293.15	0.6995	1.3718
293.15	0.8030	1.3727
293.15	0.9005	1.3738
293.15	0.9514	1.3744
293.15	1.0000	1.3749
298.15	0.0000	1.3698
298.15	0.0469	1.3693
298.15	0.0969	1.3689
298.15	0.1898	1.3683
298.15	0.2962	1.3679
298.15	0.3907	1.3678
298.15	0.5028	1.3679
298.15	0.5980	1.3682
298.15	0.6995	1.369
298.15	0.8030	1.3698
298.15	0.9005	1.371
298.15	0.9514	1.3716
298.15	1.0000	1.3722
303.15	0.0000	1.3671
303.15	0.0469	1.3666
303.15	0.0969	1.3662
303.15	0.1898	1.3656
303.15	0.2962	1.3651
303.15	0.3907	1.365
303.15	0.5028	1.3651
303.15	0.5980	1.3655
303.15	0.6995	1.3661
303.15	0.8030	1.3669
303.15	0.9005	1.368
303.15	0.9514	1.3687
303.15	1.0000	1.3694

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
291.15	0.0000	661.17
291.15	0.0165	663.7
291.15	0.0655	671.62
291.15	0.1077	678.72
291.15	0.1823	692.02
291.15	0.1962	694.54
291.15	0.2716	709.09
291.15	0.3518	725.37
291.15	0.4166	739.37
291.15	0.5519	770.91
291.15	0.6225	788.69
291.15	0.6795	803.74
291.15	0.7429	821.35
291.15	0.8048	839.41
291.15	0.8980	868.3
291.15	0.9604	888.98
291.15	0.9833	896.93
291.15	1.0000	902.88
298.15	0.0000	654.9
298.15	0.0704	666.2
298.15	0.1270	675.7
298.15	0.1930	687.4
298.15	0.2383	695.9
298.15	0.2909	706.1
298.15	0.3466	717.4
298.15	0.4440	738.3
298.15	0.4935	749.5
298.15	0.5355	759.4
298.15	0.5869	772.0
298.15	0.6255	781.8
298.15	0.7012	801.9
298.15	0.7532	816.4
298.15	0.8292	838.8
298.15	0.8612	848.7
298.15	0.9233	868.5
298.15	0.9469	876.3
298.15	1.0000	894.4
318.15	0.0000	636.5
318.15	0.0336	641.5
318.15	0.0764	648.1
318.15	0.1448	659.3
318.15	0.2606	679.9
318.15	0.2760	682.8
318.15	0.3316	693.5
318.15	0.3976	707.0
318.15	0.4495	718.1
318.15	0.5054	730.6
318.15	0.5551	742.2
318.15	0.6085	755.1
318.15	0.7048	779.9
318.15	0.7523	792.9
318.15	0.7984	806.0
318.15	0.8419	818.8
318.15	0.8854	832.2
318.15	0.9305	846.4
318.15	1.0000	869.6
328.15	0.0000	627.0
328.15	0.0433	633.2
328.15	0.0847	639.6
328.15	0.1691	653.4
328.15	0.2349	664.88
328.15	0.3070	678.0
328.15	0.3708	690.6
328.15	0.4318	703.25
328.15	0.4918	716.3
328.15	0.5567	731.2
328.15	0.6075	743.4
328.15	0.6523	754.6
328.15	0.7238	773.4
328.15	0.7577	782.7
328.15	0.8221	800.9
328.15	0.8723	815.8
328.15	0.9135	828.6
328.15	0.9832	851.3
328.15	1.0000	857.17

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	900.5
293.15	0.0469	884.3
293.15	0.0969	868.0
293.15	0.1898	838.9
293.15	0.2962	808.6
293.15	0.3907	783.5
293.15	0.5028	756.0
293.15	0.5980	734.5
293.15	0.6995	713.1
293.15	0.8030	693.3
293.15	0.9005	675.8
293.15	0.9514	667.3
293.15	1.0000	659.5
298.15	0.0000	894.4
298.15	0.0469	878.2
298.15	0.0969	862.0
298.15	0.1898	833.1
298.15	0.2962	803.0
298.15	0.3907	778.0
298.15	0.5028	750.7
298.15	0.5980	729.3
298.15	0.6995	708.1
298.15	0.8030	688.4
298.15	0.9005	671.1
298.15	0.9514	662.7
298.15	1.0000	654.9
303.15	0.0000	888.2
303.15	0.0469	872.2
303.15	0.0969	855.9
303.15	0.1898	827.3
303.15	0.2962	797.3
303.15	0.3907	772.4
303.15	0.5028	745.3
303.15	0.5980	724.1
303.15	0.6995	703.1
303.15	0.8030	683.5
303.15	0.9005	666.4
303.15	0.9514	658.1
303.15	1.0000	650.4

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
291.15	0.0000	661.17
291.15	0.0165	663.7
291.15	0.0655	671.62
291.15	0.1077	678.72
291.15	0.1823	692.02
291.15	0.1962	694.54
291.15	0.2716	709.09
291.15	0.3518	725.37
291.15	0.4166	739.37
291.15	0.5519	770.91
291.15	0.6225	788.69
291.15	0.6795	803.74
291.15	0.7429	821.35
291.15	0.8048	839.41
291.15	0.8980	868.3
291.15	0.9604	888.98
291.15	0.9833	896.93
291.15	1.0000	902.88
298.15	0.0000	654.9
298.15	0.0704	666.2
298.15	0.1270	675.7
298.15	0.1930	687.4
298.15	0.2383	695.9
298.15	0.2909	706.1
298.15	0.3466	717.4
298.15	0.4440	738.3
298.15	0.4935	749.5
298.15	0.5355	759.4
298.15	0.5869	772.0
298.15	0.6255	781.8
298.15	0.7012	801.9
298.15	0.7532	816.4
298.15	0.8292	838.8
298.15	0.8612	848.7
298.15	0.9233	868.5
298.15	0.9469	876.3
298.15	1.0000	894.4
318.15	0.0000	636.5
318.15	0.0336	641.5
318.15	0.0764	648.1
318.15	0.1448	659.3
318.15	0.2606	679.9
318.15	0.2760	682.8
318.15	0.3316	693.5
318.15	0.3976	707.0
318.15	0.4495	718.1
318.15	0.5054	730.6
318.15	0.5551	742.2
318.15	0.6085	755.1
318.15	0.7048	779.9
318.15	0.7523	792.9
318.15	0.7984	806.0
318.15	0.8419	818.8
318.15	0.8854	832.2
318.15	0.9305	846.4
318.15	1.0000	869.6
328.15	0.0000	627.0
328.15	0.0433	633.2
328.15	0.0847	639.6
328.15	0.1691	653.4
328.15	0.2349	664.88
328.15	0.3070	678.0
328.15	0.3708	690.6
328.15	0.4318	703.25
328.15	0.4918	716.3
328.15	0.5567	731.2
328.15	0.6075	743.4
328.15	0.6523	754.6
328.15	0.7238	773.4
328.15	0.7577	782.7
328.15	0.8221	800.9
328.15	0.8723	815.8
328.15	0.9135	828.6
328.15	0.9832	851.3
328.15	1.0000	857.17

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	900.5
293.15	0.0469	884.3
293.15	0.0969	868.0
293.15	0.1898	838.9
293.15	0.2962	808.6
293.15	0.3907	783.5
293.15	0.5028	756.0
293.15	0.5980	734.5
293.15	0.6995	713.1
293.15	0.8030	693.3
293.15	0.9005	675.8
293.15	0.9514	667.3
293.15	1.0000	659.5
298.15	0.0000	894.4
298.15	0.0469	878.2
298.15	0.0969	862.0
298.15	0.1898	833.1
298.15	0.2962	803.0
298.15	0.3907	778.0
298.15	0.5028	750.7
298.15	0.5980	729.3
298.15	0.6995	708.1
298.15	0.8030	688.4
298.15	0.9005	671.1
298.15	0.9514	662.7
298.15	1.0000	654.9
303.15	0.0000	888.2
303.15	0.0469	872.2
303.15	0.0969	855.9
303.15	0.1898	827.3
303.15	0.2962	797.3
303.15	0.3907	772.4
303.15	0.5028	745.3
303.15	0.5980	724.1
303.15	0.6995	703.1
303.15	0.8030	683.5
303.15	0.9005	666.4
303.15	0.9514	658.1
303.15	1.0000	650.4

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1162.0
293.15	0.0469	1152.0
293.15	0.0969	1141.0
293.15	0.1898	1125.0
293.15	0.2962	1111.0
293.15	0.3907	1101.0
293.15	0.5028	1093.0
293.15	0.5980	1090.0
293.15	0.6995	1088.0
293.15	0.8030	1089.0
293.15	0.9005	1093.0
293.15	0.9514	1096.0
293.15	1.0000	1100.0
298.15	0.0000	1141.0
298.15	0.0469	1129.0
298.15	0.0969	1119.0
298.15	0.1898	1103.0
298.15	0.2962	1089.0
298.15	0.3907	1079.0
298.15	0.5028	1071.0
298.15	0.5980	1067.0
298.15	0.6995	1066.0
298.15	0.8030	1067.0
298.15	0.9005	1071.0
298.15	0.9514	1074.0
298.15	1.0000	1078.0
303.15	0.0000	1111.0
303.15	0.0469	1099.0
303.15	0.0969	1089.0
303.15	0.1898	1074.0
303.15	0.2962	1061.0
303.15	0.3907	1053.0
303.15	0.5028	1046.0
303.15	0.5980	1042.0
303.15	0.6995	1041.0
303.15	0.8030	1043.0
303.15	0.9005	1047.0
303.15	0.9514	1051.0
303.15	1.0000	1055.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1162.0
293.15	0.0469	1152.0
293.15	0.0969	1141.0
293.15	0.1898	1125.0
293.15	0.2962	1111.0
293.15	0.3907	1101.0
293.15	0.5028	1093.0
293.15	0.5980	1090.0
293.15	0.6995	1088.0
293.15	0.8030	1089.0
293.15	0.9005	1093.0
293.15	0.9514	1096.0
293.15	1.0000	1100.0
298.15	0.0000	1141.0
298.15	0.0469	1129.0
298.15	0.0969	1119.0
298.15	0.1898	1103.0
298.15	0.2962	1089.0
298.15	0.3907	1079.0
298.15	0.5028	1071.0
298.15	0.5980	1067.0
298.15	0.6995	1066.0
298.15	0.8030	1067.0
298.15	0.9005	1071.0
298.15	0.9514	1074.0
298.15	1.0000	1078.0
303.15	0.0000	1111.0
303.15	0.0469	1099.0
303.15	0.0969	1089.0
303.15	0.1898	1074.0
303.15	0.2962	1061.0
303.15	0.3907	1053.0
303.15	0.5028	1046.0
303.15	0.5980	1042.0
303.15	0.6995	1041.0
303.15	0.8030	1043.0
303.15	0.9005	1047.0
303.15	0.9514	1051.0
303.15	1.0000	1055.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	341.88
0.0110	341.54
0.0320	341.03
0.0630	340.32
0.1010	339.71
0.1510	339.05
0.2090	338.55
0.2870	338.21
0.3560	338.13
0.4240	338.25
0.4850	338.48
0.5410	338.78
0.6000	339.17
0.6440	339.58
0.6970	340.33
0.7300	340.85
0.7700	341.68
0.8140	342.65
0.8590	343.95
0.8950	345.21
0.9260	346.48
0.9470	347.40
0.9730	348.65
1.0000	350.15

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	341.88
0.0110	341.54
0.0320	341.03
0.0630	340.32
0.1010	339.71
0.1510	339.05
0.2090	338.55
0.2870	338.21
0.3560	338.13
0.4240	338.25
0.4850	338.48
0.5410	338.78
0.6000	339.17
0.6440	339.58
0.6970	340.33
0.7300	340.85
0.7700	341.68
0.8140	342.65
0.8590	343.95
0.8950	345.21
0.9260	346.48
0.9470	347.40
0.9730	348.65
1.0000	350.15

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

T [K] - VLE	x1[mol/mol] of n-Hexane (1) - Liquid
350.3	0.0000
345.65	0.0900
342.35	0.2020
340.55	0.3020
339.45	0.4040
338.75	0.5000
338.45	0.5930
338.35	0.7020
338.75	0.8030
339.75	0.9000
342.0	1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

x1[mol/mol] of n-Hexane (1) - Liquid	y1[mol/mol] of n-Hexane (1) - Vapour
0.0400	0.0940
0.0910	0.1910
0.1740	0.3140
0.2660	0.4030
0.3610	0.4790
0.4580	0.5340
0.5570	0.5990
0.6430	0.6490
0.6920	0.6790
0.7980	0.7520
0.9000	0.8490
0.9520	0.9220

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 353.15 (VLE)

x1[mol/mol] of n-Hexane (1) - Liquid	y1[mol/mol] of n-Hexane (1) - Vapour
0.0189	0.0642
0.0392	0.1183
0.0583	0.1561
0.1196	0.2973
0.1653	0.3417
0.2275	0.4174
0.2856	0.4580
0.3462	0.5171
0.3969	0.5208
0.4673	0.5570
0.5287	0.5864
0.5887	0.6171
0.6518	0.6370
0.7086	0.6691
0.7704	0.7108
0.8812	0.7933
0.9147	0.8323
0.9410	0.8784
0.9613	0.9137
0.9784	0.9488

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.32	338.15

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.32	338.15

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
• Phase Equilibria of the Azeotropic Mixture Hexane + Ethyl Acetate with Ionic Liquids at 298.15 K