Mixture of Ethanol + Ethyl Acetate

Datasets

1. Mole fraction (14)
2. η - Viscosity, Pa*s (6)
3. Excess molar enthalpy (molar enthalpy (6)
4. P_c - Critical pressure, kPa (2)
5. P_vap - Vapor or sublimation pressure, kPa (2)
6. n₀ - Refractive index (Na D-line) (2)
7. ρ_l - Mass density, kg/m3 (8)
8. c_sound,fluid - Speed of Sound, m/s (2)
9. T_boil - Boiling temperature at pressure P, K (18)
10. T_c - Critical temperature, K (2)
11. Vapor Liquid Equilibrium at Constant Pressure
12. Vapor Liquid Equilibrium at Constant Temperature (2)
13. Azeotropic pressure, kPa (4)

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0239	0.0602
0.0437	0.1024
0.0651	0.1367
0.1005	0.1936
0.1633	0.2778
0.1886	0.3066
0.2220	0.3389
0.2905	0.3899
0.3406	0.4296
0.3697	0.4407
0.3916	0.4586
0.4150	0.4729
0.4342	0.4844
0.4643	0.4981
0.4990	0.5178
0.5369	0.5410
0.5792	0.5657
0.6241	0.5930
0.6594	0.6165
0.7002	0.6438
0.7447	0.6762
0.7919	0.7164
0.8420	0.7699
0.8992	0.8357

Mole fraction of Ethyl Acetate (2) [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	323.15	0.0000
0.0000	348.15	0.0000
0.0095	323.15	0.0333
0.0110	348.15	0.0263
0.0307	323.15	0.0963
0.0354	348.15	0.0794
0.0755	323.15	0.1973
0.0829	348.15	0.1622
0.1113	323.15	0.2560
0.1181	348.15	0.2137
0.1483	323.15	0.3074
0.1553	348.15	0.2554
0.2088	323.15	0.3713
0.2169	348.15	0.3170
0.3016	323.15	0.4431
0.3102	348.15	0.3913
0.3715	323.15	0.4889
0.3830	348.15	0.4393
0.4487	323.15	0.5318
0.4589	348.15	0.4859
0.5329	323.15	0.5759
0.5418	348.15	0.5364
0.6268	323.15	0.6267
0.6341	348.15	0.5955
0.7399	323.15	0.6941
0.7475	348.15	0.6764
0.8263	323.15	0.7638
0.8304	348.15	0.7535
0.8834	323.15	0.8212
0.8861	348.15	0.8183
0.9385	348.15	0.8908
0.9386	323.15	0.8931
0.9814	348.15	0.9641
0.9816	323.15	0.9640
1.0000	323.15	1.0000
1.0000	348.15	1.0000

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
1.0000	1.0000
0.9690	0.9390
0.9390	0.8900
0.8830	0.8120
0.8260	0.7500
0.7350	0.6700
0.6200	0.5910
0.5180	0.5290
0.4010	0.4590
0.3080	0.3970
0.2260	0.3310
0.1590	0.2650
0.1070	0.1990
0.0670	0.1380
0.0370	0.0820
0.0000	0.0000

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0300	0.1160
0.0620	0.2100
0.1290	0.3340
0.2030	0.4170
0.2740	0.4730
0.2830	0.4770
0.3270	0.5020
0.3720	0.5270
0.4200	0.5470
0.4710	0.5710
0.5240	0.5930
0.5800	0.6170
0.6400	0.6460
0.7030	0.6750
0.7710	0.7160
0.8420	0.7710
0.9180	0.8570

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	0.0000
0.0502	0.1173
0.0968	0.2071
0.1990	0.3313
0.2923	0.4288
0.3913	0.4750
0.4962	0.5317
0.6000	0.5817
0.7038	0.6096
0.8192	0.7154
1.0000	1.0000

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	0.0000
0.0210	0.0480
0.0430	0.0910
0.0740	0.1470
0.1210	0.2120
0.1680	0.2720
0.2170	0.3170
0.2600	0.3580
0.3030	0.3920
0.3550	0.4280
0.4020	0.4580
0.4480	0.4860
0.4930	0.5140
0.5400	0.5420
0.5840	0.5680
0.6240	0.5930
0.6660	0.6210
0.6900	0.6370
0.7170	0.6570
0.7440	0.6790
0.7670	0.6990
0.7900	0.7200
0.8180	0.7400
0.8350	0.7590
0.8510	0.7740
0.8750	0.8030
0.9000	0.8330
0.9370	0.8880
0.9750	0.9510
1.0000	1.0000

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
0.0490	0.1060
0.1070	0.1920
0.1950	0.2990
0.3230	0.3890
0.4180	0.4680
0.5170	0.5300
0.6100	0.5920
0.7090	0.6540
0.8050	0.7300
0.9130	0.8360
0.9620	0.9240
1.0000	1.0000

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0239	0.0602
0.0437	0.1024
0.0651	0.1367
0.1005	0.1936
0.1633	0.2778
0.1886	0.3066
0.2220	0.3389
0.2905	0.3899
0.3406	0.4296
0.3697	0.4407
0.3916	0.4586
0.4150	0.4729
0.4342	0.4844
0.4643	0.4981
0.4990	0.5178
0.5369	0.5410
0.5792	0.5657
0.6241	0.5930
0.6594	0.6165
0.7002	0.6438
0.7447	0.6762
0.7919	0.7164
0.8420	0.7699
0.8992	0.8357

Mole fraction of Ethyl Acetate (2) [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	323.15	0.0000
0.0000	348.15	0.0000
0.0095	323.15	0.0333
0.0110	348.15	0.0263
0.0307	323.15	0.0963
0.0354	348.15	0.0794
0.0755	323.15	0.1973
0.0829	348.15	0.1622
0.1113	323.15	0.2560
0.1181	348.15	0.2137
0.1483	323.15	0.3074
0.1553	348.15	0.2554
0.2088	323.15	0.3713
0.2169	348.15	0.3170
0.3016	323.15	0.4431
0.3102	348.15	0.3913
0.3715	323.15	0.4889
0.3830	348.15	0.4393
0.4487	323.15	0.5318
0.4589	348.15	0.4859
0.5329	323.15	0.5759
0.5418	348.15	0.5364
0.6268	323.15	0.6267
0.6341	348.15	0.5955
0.7399	323.15	0.6941
0.7475	348.15	0.6764
0.8263	323.15	0.7638
0.8304	348.15	0.7535
0.8834	323.15	0.8212
0.8861	348.15	0.8183
0.9385	348.15	0.8908
0.9386	323.15	0.8931
0.9814	348.15	0.9641
0.9816	323.15	0.9640
1.0000	323.15	1.0000
1.0000	348.15	1.0000

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
1.0000	1.0000
0.9690	0.9390
0.9390	0.8900
0.8830	0.8120
0.8260	0.7500
0.7350	0.6700
0.6200	0.5910
0.5180	0.5290
0.4010	0.4590
0.3080	0.3970
0.2260	0.3310
0.1590	0.2650
0.1070	0.1990
0.0670	0.1380
0.0370	0.0820
0.0000	0.0000

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0300	0.1160
0.0620	0.2100
0.1290	0.3340
0.2030	0.4170
0.2740	0.4730
0.2830	0.4770
0.3270	0.5020
0.3720	0.5270
0.4200	0.5470
0.4710	0.5710
0.5240	0.5930
0.5800	0.6170
0.6400	0.6460
0.7030	0.6750
0.7710	0.7160
0.8420	0.7710
0.9180	0.8570

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	0.0000
0.0502	0.1173
0.0968	0.2071
0.1990	0.3313
0.2923	0.4288
0.3913	0.4750
0.4962	0.5317
0.6000	0.5817
0.7038	0.6096
0.8192	0.7154
1.0000	1.0000

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	0.0000
0.0210	0.0480
0.0430	0.0910
0.0740	0.1470
0.1210	0.2120
0.1680	0.2720
0.2170	0.3170
0.2600	0.3580
0.3030	0.3920
0.3550	0.4280
0.4020	0.4580
0.4480	0.4860
0.4930	0.5140
0.5400	0.5420
0.5840	0.5680
0.6240	0.5930
0.6660	0.6210
0.6900	0.6370
0.7170	0.6570
0.7440	0.6790
0.7670	0.6990
0.7900	0.7200
0.8180	0.7400
0.8350	0.7590
0.8510	0.7740
0.8750	0.8030
0.9000	0.8330
0.9370	0.8880
0.9750	0.9510
1.0000	1.0000

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
0.0490	0.1060
0.1070	0.1920
0.1950	0.2990
0.3230	0.3890
0.4180	0.4680
0.5170	0.5300
0.6100	0.5920
0.7090	0.6540
0.8050	0.7300
0.9130	0.8360
0.9620	0.9240
1.0000	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0005
293.15	0.0491	0.0004
293.15	0.0990	0.0005
293.15	0.1958	0.0005
293.15	0.2961	0.0005
293.15	0.3947	0.0005
293.15	0.4948	0.0005
293.15	0.5995	0.0006
293.15	0.7004	0.0007
293.15	0.8004	0.0008
293.15	0.9003	0.0009
293.15	0.9505	0.0010
293.15	1.0000	0.0012
298.15	0.0000	0.0004
298.15	0.0491	0.0004
298.15	0.0990	0.0004
298.15	0.1958	0.0004
298.15	0.2961	0.0004
298.15	0.3947	0.0005
298.15	0.4948	0.0005
298.15	0.5995	0.0005
298.15	0.7004	0.0006
298.15	0.8004	0.0007
298.15	0.9003	0.0008
298.15	0.9505	0.0010
298.15	1.0000	0.0011
303.15	0.0000	0.0004
303.15	0.0491	0.0004
303.15	0.0990	0.0004
303.15	0.1958	0.0004
303.15	0.2961	0.0004
303.15	0.3947	0.0004
303.15	0.4948	0.0005
303.15	0.5995	0.0005
303.15	0.7004	0.0006
303.15	0.8004	0.0006
303.15	0.9003	0.0008
303.15	0.9505	0.0009
303.15	1.0000	0.0010

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.1000	0.0008
298.15	0.2000	0.0007
298.15	0.3000	0.0006
298.15	0.4000	0.0006
298.15	0.5000	0.0005
298.15	0.6000	0.0005
298.15	0.7000	0.0005
298.15	0.8000	0.0004
298.15	0.9000	0.0004
318.15	0.1000	0.0006
318.15	0.2000	0.0005
318.15	0.3007	0.0005
318.15	0.4000	0.0004
318.15	0.5000	0.0004
318.15	0.6003	0.0004
318.15	0.7006	0.0004
318.15	0.8000	0.0004
318.15	0.9000	0.0004

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0941	0.0009
0.1919	0.0007
0.2836	0.0006
0.4044	0.0005
0.5014	0.0005
0.6085	0.0005
0.6949	0.0004
0.7929	0.0004
0.8957	0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0005
293.15	0.0491	0.0004
293.15	0.0990	0.0005
293.15	0.1958	0.0005
293.15	0.2961	0.0005
293.15	0.3947	0.0005
293.15	0.4948	0.0005
293.15	0.5995	0.0006
293.15	0.7004	0.0007
293.15	0.8004	0.0008
293.15	0.9003	0.0009
293.15	0.9505	0.0010
293.15	1.0000	0.0012
298.15	0.0000	0.0004
298.15	0.0491	0.0004
298.15	0.0990	0.0004
298.15	0.1958	0.0004
298.15	0.2961	0.0004
298.15	0.3947	0.0005
298.15	0.4948	0.0005
298.15	0.5995	0.0005
298.15	0.7004	0.0006
298.15	0.8004	0.0007
298.15	0.9003	0.0008
298.15	0.9505	0.0010
298.15	1.0000	0.0011
303.15	0.0000	0.0004
303.15	0.0491	0.0004
303.15	0.0990	0.0004
303.15	0.1958	0.0004
303.15	0.2961	0.0004
303.15	0.3947	0.0004
303.15	0.4948	0.0005
303.15	0.5995	0.0005
303.15	0.7004	0.0006
303.15	0.8004	0.0006
303.15	0.9003	0.0008
303.15	0.9505	0.0009
303.15	1.0000	0.0010

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.1000	0.0008
298.15	0.2000	0.0007
298.15	0.3000	0.0006
298.15	0.4000	0.0006
298.15	0.5000	0.0005
298.15	0.6000	0.0005
298.15	0.7000	0.0005
298.15	0.8000	0.0004
298.15	0.9000	0.0004
318.15	0.1000	0.0006
318.15	0.2000	0.0005
318.15	0.3007	0.0005
318.15	0.4000	0.0004
318.15	0.5000	0.0004
318.15	0.6003	0.0004
318.15	0.7006	0.0004
318.15	0.8000	0.0004
318.15	0.9000	0.0004

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0941	0.0009
0.1919	0.0007
0.2836	0.0006
0.4044	0.0005
0.5014	0.0005
0.6085	0.0005
0.6949	0.0004
0.7929	0.0004
0.8957	0.0004

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

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
363.15	1548.00	0.0151	0.0973
363.15	1548.00	0.0305	0.1980
363.15	1548.00	0.0624	0.3920
363.15	1548.00	0.0956	0.5780
363.15	1548.00	0.1302	0.7570
363.15	1548.00	0.1664	0.9260
363.15	1548.00	0.2042	1.083
363.15	1548.00	0.2438	1.228
363.15	1548.00	0.2853	1.374
363.15	1548.00	0.3288	1.489
363.15	1548.00	0.3745	1.582
363.15	1548.00	0.4226	1.667
363.15	1548.00	0.4732	1.717
363.15	1548.00	0.5265	1.71
363.15	1548.00	0.5828	1.69
363.15	1548.00	0.6424	1.618
363.15	1548.00	0.7054	1.486
363.15	1548.00	0.7724	1.276
363.15	1548.00	0.8435	0.9720
363.15	1548.00	0.9192	0.5550
363.15	1548.00	0.9589	0.2920
413.15	1307.00	0.0151	0.1080
413.15	1307.00	0.0306	0.2220
413.15	1307.00	0.0624	0.4390
413.15	1307.00	0.0956	0.6460
413.15	1307.00	0.1302	0.8410
413.15	1307.00	0.1664	1.028
413.15	1307.00	0.2042	1.198
413.15	1307.00	0.2438	1.36
413.15	1307.00	0.2853	1.502
413.15	1307.00	0.3288	1.623
413.15	1307.00	0.3745	1.725
413.15	1307.00	0.4226	1.773
413.15	1307.00	0.4732	1.815
413.15	1307.00	0.5265	1.812
413.15	1307.00	0.5829	1.765
413.15	1307.00	0.6424	1.663
413.15	1307.00	0.7055	1.502
413.15	1307.00	0.7724	1.261
413.15	1307.00	0.8435	0.9390
413.15	1307.00	0.9192	0.5240
413.15	1307.00	0.9589	0.2760

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 10000 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0300	0.1410
0.0540	0.2474
0.0780	0.3659
0.1040	0.4696
0.1300	0.5660
0.1570	0.6609
0.1840	0.7551
0.2130	0.8459
0.2430	0.9311
0.2740	1.0073
0.3060	1.0823
0.3390	1.148
0.3730	1.2042
0.4090	1.2507
0.4460	1.2976
0.4850	1.3282
0.5250	1.3375
0.5670	1.3304
0.6110	1.3093
0.6570	1.2592
0.7050	1.1927
0.7540	1.0879
0.8070	0.9471
0.8610	0.7632
0.9190	0.5089
0.9390	0.3995
0.9600	0.2744

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.2980
0.1000	0.5640
0.1500	0.7750
0.2000	0.9300
0.2500	1.048
0.3000	1.131
0.3500	1.185
0.4000	1.216
0.4500	1.224
0.5000	1.211
0.5500	1.189
0.6000	1.153
0.6500	1.095
0.7000	0.9770
0.7500	0.8590
0.8000	0.7280
0.8500	0.5770
0.9000	0.4200
0.9500	0.2320

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

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
363.15	1548.00	0.0151	0.0973
363.15	1548.00	0.0305	0.1980
363.15	1548.00	0.0624	0.3920
363.15	1548.00	0.0956	0.5780
363.15	1548.00	0.1302	0.7570
363.15	1548.00	0.1664	0.9260
363.15	1548.00	0.2042	1.083
363.15	1548.00	0.2438	1.228
363.15	1548.00	0.2853	1.374
363.15	1548.00	0.3288	1.489
363.15	1548.00	0.3745	1.582
363.15	1548.00	0.4226	1.667
363.15	1548.00	0.4732	1.717
363.15	1548.00	0.5265	1.71
363.15	1548.00	0.5828	1.69
363.15	1548.00	0.6424	1.618
363.15	1548.00	0.7054	1.486
363.15	1548.00	0.7724	1.276
363.15	1548.00	0.8435	0.9720
363.15	1548.00	0.9192	0.5550
363.15	1548.00	0.9589	0.2920
413.15	1307.00	0.0151	0.1080
413.15	1307.00	0.0306	0.2220
413.15	1307.00	0.0624	0.4390
413.15	1307.00	0.0956	0.6460
413.15	1307.00	0.1302	0.8410
413.15	1307.00	0.1664	1.028
413.15	1307.00	0.2042	1.198
413.15	1307.00	0.2438	1.36
413.15	1307.00	0.2853	1.502
413.15	1307.00	0.3288	1.623
413.15	1307.00	0.3745	1.725
413.15	1307.00	0.4226	1.773
413.15	1307.00	0.4732	1.815
413.15	1307.00	0.5265	1.812
413.15	1307.00	0.5829	1.765
413.15	1307.00	0.6424	1.663
413.15	1307.00	0.7055	1.502
413.15	1307.00	0.7724	1.261
413.15	1307.00	0.8435	0.9390
413.15	1307.00	0.9192	0.5240
413.15	1307.00	0.9589	0.2760

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 10000 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0300	0.1410
0.0540	0.2474
0.0780	0.3659
0.1040	0.4696
0.1300	0.5660
0.1570	0.6609
0.1840	0.7551
0.2130	0.8459
0.2430	0.9311
0.2740	1.0073
0.3060	1.0823
0.3390	1.148
0.3730	1.2042
0.4090	1.2507
0.4460	1.2976
0.4850	1.3282
0.5250	1.3375
0.5670	1.3304
0.6110	1.3093
0.6570	1.2592
0.7050	1.1927
0.7540	1.0879
0.8070	0.9471
0.8610	0.7632
0.9190	0.5089
0.9390	0.3995
0.9600	0.2744

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.2980
0.1000	0.5640
0.1500	0.7750
0.2000	0.9300
0.2500	1.048
0.3000	1.131
0.3500	1.185
0.4000	1.216
0.4500	1.224
0.5000	1.211
0.5500	1.189
0.6000	1.153
0.6500	1.095
0.7000	0.9770
0.7500	0.8590
0.8000	0.7280
0.8500	0.5770
0.9000	0.4200
0.9500	0.2320

Critical pressure, kPa [ref]

Mole fraction of Ethanol (1) - Liquid	Critical pressure, kPa - Liquid
0.2000	4320.00
0.4000	4770.00
0.5900	5170.00
0.6800	5350.00
0.7500	5520.00
0.8500	5780.00

Critical pressure, kPa [ref]

Mole fraction of Ethanol (1) - Liquid	Critical pressure, kPa - Liquid
0.2000	4320.00
0.4000	4770.00
0.5900	5170.00
0.6800	5350.00
0.7500	5520.00
0.8500	5780.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	323.15	29.48
0.0000	348.15	88.84
0.0095	323.15	30.22
0.0110	348.15	90.35
0.0307	323.15	31.70
0.0354	348.15	93.37
0.0755	323.15	34.28
0.0829	348.15	98.28
0.1113	323.15	35.91
0.1181	348.15	101.35
0.1483	323.15	37.37
0.1553	348.15	104.05
0.2088	323.15	39.17
0.2169	348.15	107.22
0.3016	323.15	41.13
0.3102	348.15	110.64
0.3715	323.15	42.14
0.3830	348.15	112.18
0.4487	323.15	42.89
0.4589	348.15	113.12
0.5329	323.15	43.40
0.5418	348.15	113.40
0.6268	323.15	43.60
0.6341	348.15	112.74
0.7399	323.15	43.27
0.7475	348.15	110.41
0.8263	323.15	42.42
0.8304	348.15	107.06
0.8834	323.15	41.48
0.8861	348.15	104.02
0.9385	348.15	100.26
0.9386	323.15	40.12
0.9814	348.15	96.51
0.9816	323.15	38.68
1.0000	323.15	37.95
1.0000	348.15	94.62

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	323.15	29.48
0.0000	348.15	88.84
0.0095	323.15	30.22
0.0110	348.15	90.35
0.0307	323.15	31.70
0.0354	348.15	93.37
0.0755	323.15	34.28
0.0829	348.15	98.28
0.1113	323.15	35.91
0.1181	348.15	101.35
0.1483	323.15	37.37
0.1553	348.15	104.05
0.2088	323.15	39.17
0.2169	348.15	107.22
0.3016	323.15	41.13
0.3102	348.15	110.64
0.3715	323.15	42.14
0.3830	348.15	112.18
0.4487	323.15	42.89
0.4589	348.15	113.12
0.5329	323.15	43.40
0.5418	348.15	113.40
0.6268	323.15	43.60
0.6341	348.15	112.74
0.7399	323.15	43.27
0.7475	348.15	110.41
0.8263	323.15	42.42
0.8304	348.15	107.06
0.8834	323.15	41.48
0.8861	348.15	104.02
0.9385	348.15	100.26
0.9386	323.15	40.12
0.9814	348.15	96.51
0.9816	323.15	38.68
1.0000	323.15	37.95
1.0000	348.15	94.62

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0941	1.3606
0.1919	1.3619
0.2836	1.3631
0.4044	1.3645
0.5014	1.3655
0.6085	1.3665
0.6949	1.3672
0.7929	1.3681
0.8957	1.3689

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0941	1.3606
0.1919	1.3619
0.2836	1.3631
0.4044	1.3645
0.5014	1.3655
0.6085	1.3665
0.6949	1.3672
0.7929	1.3681
0.8957	1.3689

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	900.52
293.15	0.0491	896.91
293.15	0.0990	893.14
293.15	0.1958	885.48
293.15	0.2961	877.07
293.15	0.3947	868.09
293.15	0.4948	858.16
293.15	0.5995	846.81
293.15	0.7004	834.71
293.15	0.8004	821.45
293.15	0.9003	806.45
293.15	0.9505	798.36
293.15	1.0000	789.75
298.15	0.0000	894.43
298.15	0.0491	890.86
298.15	0.0990	887.11
298.15	0.1958	879.55
298.15	0.2961	871.22
298.15	0.3947	862.38
298.15	0.4948	852.62
298.15	0.5995	841.47
298.15	0.7004	829.57
298.15	0.8004	816.55
298.15	0.9003	801.82
298.15	0.9505	793.91
298.15	1.0000	785.46
303.15	0.0000	888.3
303.15	0.0491	884.76
303.15	0.0990	881.03
303.15	0.1958	873.57
303.15	0.2961	865.34
303.15	0.3947	856.63
303.15	0.4948	847.03
303.15	0.5995	836.07
303.15	0.7004	824.39
303.15	0.8004	811.61
303.15	0.9003	797.15
303.15	0.9505	789.42
303.15	1.0000	781.15

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0124	894.9
298.15	0.0357	894.7
298.15	0.0713	894.4
298.15	0.1025	894.2
298.15	0.2087	893.5
298.15	0.3504	892.6
298.15	0.5065	891.7
298.15	0.6771	890.7
298.15	0.9772	889.1
298.15	1.7008	885.5
298.15	2.7122	880.6
298.15	3.0012	879.4
303.15	0.0124	888.4
303.15	0.0357	888.2
303.15	0.0713	887.9
303.15	0.1025	887.7
303.15	0.2087	887.0
303.15	0.3504	886.1
303.15	0.5065	885.3
303.15	0.6771	884.4
303.15	0.9772	883.0
303.15	1.7008	879.4
303.15	2.7122	874.7
303.15	3.0012	873.5
308.15	0.0124	882.9
308.15	0.0357	882.7
308.15	0.0713	882.4
308.15	0.1025	882.2
308.15	0.2087	881.5
308.15	0.3504	880.6
308.15	0.5065	879.8
308.15	0.6771	878.9
308.15	0.9772	877.4
308.15	1.7008	874.0
308.15	2.7122	869.3
308.15	3.0012	868.1
313.15	0.0124	877.2
313.15	0.0357	877.0
313.15	0.0713	876.4
313.15	0.1025	876.5
313.15	0.2087	875.8
313.15	0.3504	874.9
313.15	0.5065	874.0
313.15	0.6771	873.2
313.15	0.9772	871.8
313.15	1.7008	868.3
313.15	2.7122	863.7
313.15	3.0012	862.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.1000	801.5
298.15	0.1992	816.25
298.15	0.3006	829.52
298.15	0.3949	840.61
298.15	0.5001	852.04
298.15	0.5987	861.64
298.15	0.7000	870.79
298.15	0.7981	879.06
298.15	0.9000	886.96
298.15	0.9501	890.81
318.15	0.1000	783.09
318.15	0.2001	796.45
318.15	0.3000	808.31
318.15	0.4001	819.37
318.15	0.5000	829.53
318.15	0.6000	838.75
318.15	0.7000	847.18
318.15	0.8001	855.16
318.15	0.8999	862.6

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.0941	800.65
0.1919	815.09
0.2836	827.27
0.4044	841.69
0.5014	852.05
0.6085	862.53
0.6949	870.3
0.7929	878.51
0.8957	886.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	900.52
293.15	0.0491	896.91
293.15	0.0990	893.14
293.15	0.1958	885.48
293.15	0.2961	877.07
293.15	0.3947	868.09
293.15	0.4948	858.16
293.15	0.5995	846.81
293.15	0.7004	834.71
293.15	0.8004	821.45
293.15	0.9003	806.45
293.15	0.9505	798.36
293.15	1.0000	789.75
298.15	0.0000	894.43
298.15	0.0491	890.86
298.15	0.0990	887.11
298.15	0.1958	879.55
298.15	0.2961	871.22
298.15	0.3947	862.38
298.15	0.4948	852.62
298.15	0.5995	841.47
298.15	0.7004	829.57
298.15	0.8004	816.55
298.15	0.9003	801.82
298.15	0.9505	793.91
298.15	1.0000	785.46
303.15	0.0000	888.3
303.15	0.0491	884.76
303.15	0.0990	881.03
303.15	0.1958	873.57
303.15	0.2961	865.34
303.15	0.3947	856.63
303.15	0.4948	847.03
303.15	0.5995	836.07
303.15	0.7004	824.39
303.15	0.8004	811.61
303.15	0.9003	797.15
303.15	0.9505	789.42
303.15	1.0000	781.15

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0124	894.9
298.15	0.0357	894.7
298.15	0.0713	894.4
298.15	0.1025	894.2
298.15	0.2087	893.5
298.15	0.3504	892.6
298.15	0.5065	891.7
298.15	0.6771	890.7
298.15	0.9772	889.1
298.15	1.7008	885.5
298.15	2.7122	880.6
298.15	3.0012	879.4
303.15	0.0124	888.4
303.15	0.0357	888.2
303.15	0.0713	887.9
303.15	0.1025	887.7
303.15	0.2087	887.0
303.15	0.3504	886.1
303.15	0.5065	885.3
303.15	0.6771	884.4
303.15	0.9772	883.0
303.15	1.7008	879.4
303.15	2.7122	874.7
303.15	3.0012	873.5
308.15	0.0124	882.9
308.15	0.0357	882.7
308.15	0.0713	882.4
308.15	0.1025	882.2
308.15	0.2087	881.5
308.15	0.3504	880.6
308.15	0.5065	879.8
308.15	0.6771	878.9
308.15	0.9772	877.4
308.15	1.7008	874.0
308.15	2.7122	869.3
308.15	3.0012	868.1
313.15	0.0124	877.2
313.15	0.0357	877.0
313.15	0.0713	876.4
313.15	0.1025	876.5
313.15	0.2087	875.8
313.15	0.3504	874.9
313.15	0.5065	874.0
313.15	0.6771	873.2
313.15	0.9772	871.8
313.15	1.7008	868.3
313.15	2.7122	863.7
313.15	3.0012	862.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.1000	801.5
298.15	0.1992	816.25
298.15	0.3006	829.52
298.15	0.3949	840.61
298.15	0.5001	852.04
298.15	0.5987	861.64
298.15	0.7000	870.79
298.15	0.7981	879.06
298.15	0.9000	886.96
298.15	0.9501	890.81
318.15	0.1000	783.09
318.15	0.2001	796.45
318.15	0.3000	808.31
318.15	0.4001	819.37
318.15	0.5000	829.53
318.15	0.6000	838.75
318.15	0.7000	847.18
318.15	0.8001	855.16
318.15	0.8999	862.6

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.0941	800.65
0.1919	815.09
0.2836	827.27
0.4044	841.69
0.5014	852.05
0.6085	862.53
0.6949	870.3
0.7929	878.51
0.8957	886.6

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0124	1152.0
298.15	0.0357	1151.0
298.15	0.0713	1150.0
298.15	0.1025	1149.0
298.15	0.2087	1147.0
298.15	0.3504	1143.0
298.15	0.5065	1140.0
298.15	0.6771	1139.0
298.15	0.9772	1136.0
298.15	1.7008	1131.0
298.15	2.7122	1128.0
298.15	3.0012	1122.0
303.15	0.0124	1135.0
303.15	0.0357	1134.0
303.15	0.0713	1133.0
303.15	0.1025	1130.0
303.15	0.2087	1128.0
303.15	0.3504	1123.0
303.15	0.5065	1119.0
303.15	0.6771	1116.0
303.15	0.9772	1113.0
303.15	1.7008	1110.0
303.15	2.7122	1107.0
303.15	3.0012	1101.0
308.15	0.0124	1116.0
308.15	0.0357	1115.0
308.15	0.0713	1114.0
308.15	0.1025	1110.0
308.15	0.2087	1098.0
308.15	0.3504	1092.0
308.15	0.5065	1091.0
308.15	0.6771	1086.0
308.15	0.9772	1083.0
308.15	1.7008	1080.0
308.15	2.7122	1074.0
308.15	3.0012	1068.0
313.15	0.0124	1093.0
313.15	0.0357	1091.0
313.15	0.0713	1090.0
313.15	0.1025	1089.0
313.15	0.2087	1077.0
313.15	0.3504	1069.0
313.15	0.5065	1067.0
313.15	0.6771	1062.0
313.15	0.9772	1059.0
313.15	1.7008	1056.0
313.15	2.7122	1053.0
313.15	3.0012	1044.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0124	1152.0
298.15	0.0357	1151.0
298.15	0.0713	1150.0
298.15	0.1025	1149.0
298.15	0.2087	1147.0
298.15	0.3504	1143.0
298.15	0.5065	1140.0
298.15	0.6771	1139.0
298.15	0.9772	1136.0
298.15	1.7008	1131.0
298.15	2.7122	1128.0
298.15	3.0012	1122.0
303.15	0.0124	1135.0
303.15	0.0357	1134.0
303.15	0.0713	1133.0
303.15	0.1025	1130.0
303.15	0.2087	1128.0
303.15	0.3504	1123.0
303.15	0.5065	1119.0
303.15	0.6771	1116.0
303.15	0.9772	1113.0
303.15	1.7008	1110.0
303.15	2.7122	1107.0
303.15	3.0012	1101.0
308.15	0.0124	1116.0
308.15	0.0357	1115.0
308.15	0.0713	1114.0
308.15	0.1025	1110.0
308.15	0.2087	1098.0
308.15	0.3504	1092.0
308.15	0.5065	1091.0
308.15	0.6771	1086.0
308.15	0.9772	1083.0
308.15	1.7008	1080.0
308.15	2.7122	1074.0
308.15	3.0012	1068.0
313.15	0.0124	1093.0
313.15	0.0357	1091.0
313.15	0.0713	1090.0
313.15	0.1025	1089.0
313.15	0.2087	1077.0
313.15	0.3504	1069.0
313.15	0.5065	1067.0
313.15	0.6771	1062.0
313.15	0.9772	1059.0
313.15	1.7008	1056.0
313.15	2.7122	1053.0
313.15	3.0012	1044.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0239	350.77
0.0437	350.08
0.0651	349.52
0.1005	348.76
0.1633	347.53
0.1886	347.16
0.2220	346.74
0.2905	346.07
0.3406	345.70
0.3697	345.61
0.3916	345.51
0.4150	345.41
0.4342	345.35
0.4643	345.27
0.4990	345.22
0.5369	345.19
0.5792	345.21
0.6241	345.29
0.6594	345.43
0.7002	345.61
0.7447	345.89
0.7919	346.33
0.8420	346.99
0.8992	347.91

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1870	338.85
0.2580	337.75
0.3610	337.25
0.6050	337.45
0.8040	338.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Gas)

Mole fraction of Ethanol (1) - Gas	Boiling temperature at pressure P, K - Liquid
0.2850	338.85
0.3340	337.75
0.4210	337.25
0.5240	337.45
0.6770	338.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Gas)

Mole fraction of Ethyl Acetate (2) - Gas	Boiling temperature at pressure P, K - Gas
0.0000	351.55
0.0077	351.35
0.0491	350.85
0.0727	350.35
0.1203	349.75
0.1639	349.25
0.2059	348.65
0.2601	348.05
0.3979	346.25
0.4596	345.55
0.6294	345.35
0.6563	345.35
0.7307	345.85
0.7964	346.75
0.7995	346.65
0.8357	347.45
0.8791	348.25
0.8830	348.25
0.9588	349.35

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.55
0.0011	351.35
0.0158	350.85
0.0237	350.35
0.0445	349.75
0.0609	349.25
0.0820	348.65
0.1368	348.05
0.2660	346.25
0.3566	345.55
0.6308	345.35
0.6902	345.35
0.7772	345.85
0.8494	346.65
0.8679	346.75
0.8789	347.45
0.9224	348.25
0.9374	348.25
0.9784	349.35
0.9909	350.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	350.26
0.9690	349.17
0.9390	348.36
0.8830	347.23
0.8260	346.26
0.7350	345.45
0.6200	344.95
0.5180	345.00
0.4010	345.35
0.3080	345.83
0.2260	346.69
0.1590	347.42
0.1070	348.45
0.0670	349.40
0.0370	350.15
0.0000	351.50

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	352.75
0.0502	350.25
0.0968	349.35
0.1990	347.45
0.2923	347.25
0.3913	346.65
0.4962	346.35
0.6000	346.45
0.7038	346.75
0.8192	348.05
1.0000	350.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.21
0.0210	350.45
0.0430	349.74
0.0740	348.85
0.1210	347.82
0.1680	347.02
0.2170	346.39
0.2600	345.89
0.3030	345.53
0.3550	345.18
0.4020	344.98
0.4480	344.82
0.4930	344.73
0.5400	344.71
0.5840	344.73
0.6240	344.80
0.6660	344.91
0.6900	345.04
0.7170	345.18
0.7440	345.37
0.7670	345.57
0.7900	345.80
0.8180	346.05
0.8350	346.27
0.8510	346.51
0.8750	346.88
0.9000	347.36
0.9370	348.13
0.9750	349.10
1.0000	349.89

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	351.46
0.0490	350.13
0.1070	348.85
0.1950	347.04
0.3230	346.13
0.4180	345.46
0.5170	345.06
0.6100	345.00
0.7090	345.36
0.8050	345.94
0.9130	347.55
0.9620	348.86
1.0000	350.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0239	350.77
0.0437	350.08
0.0651	349.52
0.1005	348.76
0.1633	347.53
0.1886	347.16
0.2220	346.74
0.2905	346.07
0.3406	345.70
0.3697	345.61
0.3916	345.51
0.4150	345.41
0.4342	345.35
0.4643	345.27
0.4990	345.22
0.5369	345.19
0.5792	345.21
0.6241	345.29
0.6594	345.43
0.7002	345.61
0.7447	345.89
0.7919	346.33
0.8420	346.99
0.8992	347.91

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1870	338.85
0.2580	337.75
0.3610	337.25
0.6050	337.45
0.8040	338.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Gas)

Mole fraction of Ethanol (1) - Gas	Boiling temperature at pressure P, K - Liquid
0.2850	338.85
0.3340	337.75
0.4210	337.25
0.5240	337.45
0.6770	338.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Gas)

Mole fraction of Ethyl Acetate (2) - Gas	Boiling temperature at pressure P, K - Gas
0.0000	351.55
0.0077	351.35
0.0491	350.85
0.0727	350.35
0.1203	349.75
0.1639	349.25
0.2059	348.65
0.2601	348.05
0.3979	346.25
0.4596	345.55
0.6294	345.35
0.6563	345.35
0.7307	345.85
0.7964	346.75
0.7995	346.65
0.8357	347.45
0.8791	348.25
0.8830	348.25
0.9588	349.35

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.55
0.0011	351.35
0.0158	350.85
0.0237	350.35
0.0445	349.75
0.0609	349.25
0.0820	348.65
0.1368	348.05
0.2660	346.25
0.3566	345.55
0.6308	345.35
0.6902	345.35
0.7772	345.85
0.8494	346.65
0.8679	346.75
0.8789	347.45
0.9224	348.25
0.9374	348.25
0.9784	349.35
0.9909	350.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	350.26
0.9690	349.17
0.9390	348.36
0.8830	347.23
0.8260	346.26
0.7350	345.45
0.6200	344.95
0.5180	345.00
0.4010	345.35
0.3080	345.83
0.2260	346.69
0.1590	347.42
0.1070	348.45
0.0670	349.40
0.0370	350.15
0.0000	351.50

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	352.75
0.0502	350.25
0.0968	349.35
0.1990	347.45
0.2923	347.25
0.3913	346.65
0.4962	346.35
0.6000	346.45
0.7038	346.75
0.8192	348.05
1.0000	350.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.21
0.0210	350.45
0.0430	349.74
0.0740	348.85
0.1210	347.82
0.1680	347.02
0.2170	346.39
0.2600	345.89
0.3030	345.53
0.3550	345.18
0.4020	344.98
0.4480	344.82
0.4930	344.73
0.5400	344.71
0.5840	344.73
0.6240	344.80
0.6660	344.91
0.6900	345.04
0.7170	345.18
0.7440	345.37
0.7670	345.57
0.7900	345.80
0.8180	346.05
0.8350	346.27
0.8510	346.51
0.8750	346.88
0.9000	347.36
0.9370	348.13
0.9750	349.10
1.0000	349.89

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	351.46
0.0490	350.13
0.1070	348.85
0.1950	347.04
0.3230	346.13
0.4180	345.46
0.5170	345.06
0.6100	345.00
0.7090	345.36
0.8050	345.94
0.9130	347.55
0.9620	348.86
1.0000	350.25

Critical temperature, K [ref]

Mole fraction of Ethanol (1) - Liquid	Critical temperature, K - Liquid
0.2000	521.60
0.4000	519.20
0.5900	516.80
0.6800	515.90
0.7500	515.30
0.8500	515.40

Critical temperature, K [ref]

Mole fraction of Ethanol (1) - Liquid	Critical temperature, K - Liquid
0.2000	521.60
0.4000	519.20
0.5900	516.80
0.6800	515.90
0.7500	515.30
0.8500	515.40

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Ethyl Acetate (2) - Liquid	y1[mol/mol] of Ethyl Acetate (2) - Vapour
349.25	0.0790	0.1550
347.75	0.1640	0.2670
346.45	0.2640	0.3720
345.45	0.3720	0.4380
345.15	0.4420	0.4830
345.05	0.4730	0.4990
345.55	0.6910	0.6400
345.85	0.7280	0.6680
347.05	0.8450	0.7720

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 313.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Ethyl Acetate (2) - Liquid	y1[mol/mol] of Ethyl Acetate (2) - Vapour
19.465	0.0224	0.0808
20.198	0.0364	0.1132
21.065	0.0688	0.1836
21.998	0.0991	0.2456
23.465	0.1362	0.3079
24.531	0.1740	0.3558
25.531	0.2285	0.4170
25.531	0.2424	0.4240
26.731	0.2834	0.4685
27.264	0.3641	0.5090
28.131	0.4590	0.5683
28.798	0.5611	0.5978
28.731	0.6446	0.6693
28.798	0.6559	0.6586
28.798	0.7684	0.7386
28.464	0.7744	0.7255
28.264	0.8715	0.8126
27.464	0.9243	0.8774

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 333.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Ethyl Acetate (2) - Liquid	y1[mol/mol] of Ethyl Acetate (2) - Vapour
49.996	0.0435	0.1151
48.196	0.0240	0.0607
51.862	0.0753	0.1509
54.795	0.1060	0.2270
56.195	0.1441	0.2740
59.262	0.1936	0.3200
60.528	0.2459	0.3715
62.128	0.3130	0.4120
63.061	0.3800	0.4706
63.195	0.4140	0.5135
63.928	0.4771	0.5375
64.128	0.4989	0.5422
64.661	0.5563	0.5756
64.595	0.6721	0.6743
63.795	0.7714	0.7111
63.728	0.7714	0.7199
61.862	0.8681	0.7977
59.262	0.9405	0.8900
59.195	0.9495	0.8893

Azeotropic pressure, kPa [ref]

Mole fraction of Ethyl Acetate (2) - Liquid	Azeotropic pressure, kPa - Liquid
0.5272	113.42
0.6205	43.60

Azeotropic temperature, K [ref]

Mole fraction of Ethyl Acetate (2) - Liquid	Azeotropic temperature, K - Liquid
0.5272	348.15
0.6205	323.15

Azeotropic pressure, kPa [ref]

Mole fraction of Ethyl Acetate (2) - Liquid	Azeotropic pressure, kPa - Liquid
0.5272	113.42
0.6205	43.60

Azeotropic temperature, K [ref]

Mole fraction of Ethyl Acetate (2) - Liquid	Azeotropic temperature, K - Liquid
0.5272	348.15
0.6205	323.15

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Vapor liquid equilibria for the quaternary reactive system ethyl acetate + ethanol +water + acetic acid and some of the constituent binary systems at 101.3 kPa
• Experimental measurements of vapor liquid equilibria at low pressure: Systems containing alcohols, esters and organic acids
• Phase equilibria for reactive distillation of diethyl succinate. Part II: Systems diethyl succinate + ethyl acetate + water and diethyl succinate + acetic acid + water
• Vapour-liquid and chemical equilibria in the ethyl ethanoate + ethanol + propyl ethanoate + propanol system accompanied with transesterification reaction
• Phase equilibria and excess properties for binary systems in reactive distillation processes Part II. Ethyl acetate synthesis
• Separation of ethyl acetate and ethanol azeotrope mixture using dialkylphosphates-based ionic liquids as entrainers
• Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
• Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
• Effects of temperature and concentration on interactions in (methanol + ethyl acetate) and (ethanol + methyl acetate or ethyl acetate) systems: insights from apparent molar volume and apparent molar isentropic compressibility study
• Measurement of the Effect of Salt on Vapor-Liquid Equilibria by Using Headspace Gas Chromatography
• Critical Properties of the Reacting Mixture in the Esterification of Acetic Acid with Ethanol
• Evaluation of Excess Molar Enthalpies for a Quaternary Mixture System of Acetic Anhydride, Ethanol, Acetic Acid, and Ethyl Acetate
• Effect of Inorganic Salts on the Isobaric Vapor Liquid Equilibrium of the Ethyl Acetate Ethanol System
• Viscosity and Density of Water + Ethyl Acetate + Ethanol Mixtures at 298.15 and 318.15 K and Atmospheric Pressure
• Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Isobaric Vapor-Liquid Equilibrium for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate
• Physical Properties of Binary and Ternary Mixtures of Ethyl Acetate, Ethanol, and 1-Octyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)imide at 298.15 K