Mixture of Ethyl Acetate + Methyl Alcohol

Datasets

1. Mole fraction (6)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (2)
4. ρ_l - Mass density, kg/m3 (6)
5. c_sound,fluid - Speed of Sound, m/s (2)
6. T_boil - Boiling temperature at pressure P, K (6)
7. Vapor Liquid Equilibrium at Constant Pressure
8. Vapor Liquid Equilibrium at Constant Temperature (2)

Mole fraction of Ethyl Acetate (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Mole fraction of Ethyl Acetate (1) - Gas
0.0000	0.0000
0.0300	0.0580
0.0720	0.1140
0.1450	0.1950
0.2110	0.2460
0.2440	0.2650
0.3030	0.3110
0.3650	0.3320
0.4190	0.3610
0.4870	0.3910
0.5310	0.4100
0.6100	0.4470
0.6720	0.4830
0.7340	0.5220
0.8010	0.5800
0.8650	0.6530
0.9130	0.7340
0.9520	0.8260
0.9830	0.9320
1.0000	1.0000

Mole fraction of Ethyl Acetate (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Mole fraction of Ethyl Acetate (1) - Gas
0.0000	0.0000
0.0230	0.0390
0.0490	0.0800
0.0770	0.1160
0.1130	0.1590
0.1580	0.1990
0.1980	0.2330
0.2660	0.2750
0.3220	0.3140
0.4280	0.3540
0.5400	0.4130
0.6730	0.4850
0.8090	0.5890
0.8980	0.7150
0.9610	0.8570
1.0000	1.0000

Mole fraction of Ethyl Acetate (1) [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethyl Acetate (1) - Gas
0.0000	100.00	0.0000
0.0000	500.00	0.0000
0.0000	700.00	0.0000
0.0130	100.00	0.0260
0.0220	500.00	0.0340
0.0260	100.00	0.0490
0.0290	500.00	0.0440
0.0350	700.00	0.0470
0.0390	500.00	0.0550
0.0450	500.00	0.0630
0.0460	700.00	0.0600
0.0580	500.00	0.0770
0.0580	700.00	0.0720
0.0670	100.00	0.1010
0.0720	500.00	0.0920
0.0770	700.00	0.0920
0.0810	100.00	0.1170
0.0920	500.00	0.1120
0.0990	700.00	0.1120
0.1110	100.00	0.1490
0.1120	700.00	0.1220
0.1130	500.00	0.1300
0.1280	700.00	0.1330
0.1440	500.00	0.1550
0.1440	700.00	0.1440
0.1610	500.00	0.1660
0.1610	700.00	0.1550
0.1660	100.00	0.2010
0.1780	700.00	0.1660
0.1890	100.00	0.2200
0.1900	500.00	0.1780
0.2070	500.00	0.1880
0.2210	500.00	0.1970
0.2270	700.00	0.1900
0.2400	500.00	0.2080
0.2460	100.00	0.2600
0.2540	700.00	0.2080
0.2600	100.00	0.2670
0.2880	100.00	0.2810
0.2890	500.00	0.2340
0.2890	700.00	0.2270
0.3120	700.00	0.2340
0.3270	100.00	0.3040
0.3440	500.00	0.2610
0.3700	500.00	0.2750
0.3700	700.00	0.2610
0.3880	500.00	0.2890
0.3970	100.00	0.3360
0.4160	700.00	0.2820
0.4460	100.00	0.3610
0.4460	700.00	0.2970
0.4670	500.00	0.3280
0.4780	100.00	0.3790
0.5010	500.00	0.3440
0.5130	100.00	0.3970
0.5130	700.00	0.3360
0.5500	100.00	0.4160
0.5910	100.00	0.4360
0.5910	500.00	0.3880
0.5910	700.00	0.3780
0.6200	500.00	0.4060
0.6670	100.00	0.4780
0.6670	700.00	0.4360
0.7010	100.00	0.5010
0.7180	700.00	0.4780
0.7540	700.00	0.5130
0.7730	100.00	0.5640
0.7730	500.00	0.5380
0.8120	700.00	0.5770
0.8720	100.00	0.6840
0.8720	500.00	0.6670
0.9120	100.00	0.7550
0.9320	100.00	0.7930
0.9320	500.00	0.7730
0.9520	100.00	0.8320
0.9520	700.00	0.8320
0.9720	100.00	0.8920
0.9720	700.00	0.8920
0.9910	500.00	0.9520
1.0000	100.00	1.0000
1.0000	500.00	1.0000
1.0000	700.00	1.0000

Mole fraction of Ethyl Acetate (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Mole fraction of Ethyl Acetate (1) - Gas
0.0000	0.0000
0.0300	0.0580
0.0720	0.1140
0.1450	0.1950
0.2110	0.2460
0.2440	0.2650
0.3030	0.3110
0.3650	0.3320
0.4190	0.3610
0.4870	0.3910
0.5310	0.4100
0.6100	0.4470
0.6720	0.4830
0.7340	0.5220
0.8010	0.5800
0.8650	0.6530
0.9130	0.7340
0.9520	0.8260
0.9830	0.9320
1.0000	1.0000

Mole fraction of Ethyl Acetate (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Mole fraction of Ethyl Acetate (1) - Gas
0.0000	0.0000
0.0230	0.0390
0.0490	0.0800
0.0770	0.1160
0.1130	0.1590
0.1580	0.1990
0.1980	0.2330
0.2660	0.2750
0.3220	0.3140
0.4280	0.3540
0.5400	0.4130
0.6730	0.4850
0.8090	0.5890
0.8980	0.7150
0.9610	0.8570
1.0000	1.0000

Mole fraction of Ethyl Acetate (1) [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethyl Acetate (1) - Gas
0.0000	100.00	0.0000
0.0000	500.00	0.0000
0.0000	700.00	0.0000
0.0130	100.00	0.0260
0.0220	500.00	0.0340
0.0260	100.00	0.0490
0.0290	500.00	0.0440
0.0350	700.00	0.0470
0.0390	500.00	0.0550
0.0450	500.00	0.0630
0.0460	700.00	0.0600
0.0580	500.00	0.0770
0.0580	700.00	0.0720
0.0670	100.00	0.1010
0.0720	500.00	0.0920
0.0770	700.00	0.0920
0.0810	100.00	0.1170
0.0920	500.00	0.1120
0.0990	700.00	0.1120
0.1110	100.00	0.1490
0.1120	700.00	0.1220
0.1130	500.00	0.1300
0.1280	700.00	0.1330
0.1440	500.00	0.1550
0.1440	700.00	0.1440
0.1610	500.00	0.1660
0.1610	700.00	0.1550
0.1660	100.00	0.2010
0.1780	700.00	0.1660
0.1890	100.00	0.2200
0.1900	500.00	0.1780
0.2070	500.00	0.1880
0.2210	500.00	0.1970
0.2270	700.00	0.1900
0.2400	500.00	0.2080
0.2460	100.00	0.2600
0.2540	700.00	0.2080
0.2600	100.00	0.2670
0.2880	100.00	0.2810
0.2890	500.00	0.2340
0.2890	700.00	0.2270
0.3120	700.00	0.2340
0.3270	100.00	0.3040
0.3440	500.00	0.2610
0.3700	500.00	0.2750
0.3700	700.00	0.2610
0.3880	500.00	0.2890
0.3970	100.00	0.3360
0.4160	700.00	0.2820
0.4460	100.00	0.3610
0.4460	700.00	0.2970
0.4670	500.00	0.3280
0.4780	100.00	0.3790
0.5010	500.00	0.3440
0.5130	100.00	0.3970
0.5130	700.00	0.3360
0.5500	100.00	0.4160
0.5910	100.00	0.4360
0.5910	500.00	0.3880
0.5910	700.00	0.3780
0.6200	500.00	0.4060
0.6670	100.00	0.4780
0.6670	700.00	0.4360
0.7010	100.00	0.5010
0.7180	700.00	0.4780
0.7540	700.00	0.5130
0.7730	100.00	0.5640
0.7730	500.00	0.5380
0.8120	700.00	0.5770
0.8720	100.00	0.6840
0.8720	500.00	0.6670
0.9120	100.00	0.7550
0.9320	100.00	0.7930
0.9320	500.00	0.7730
0.9520	100.00	0.8320
0.9520	700.00	0.8320
0.9720	100.00	0.8920
0.9720	700.00	0.8920
0.9910	500.00	0.9520
1.0000	100.00	1.0000
1.0000	500.00	1.0000
1.0000	700.00	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0005
293.15	0.0474	0.0004
293.15	0.0970	0.0004
293.15	0.1956	0.0004
293.15	0.2999	0.0004
293.15	0.3963	0.0004
293.15	0.4962	0.0005
293.15	0.5963	0.0005
293.15	0.6998	0.0005
293.15	0.7992	0.0005
293.15	0.9005	0.0005
293.15	1.0000	0.0006
298.15	0.0000	0.0004
298.15	0.0474	0.0004
298.15	0.0970	0.0004
298.15	0.1956	0.0004
298.15	0.2999	0.0004
298.15	0.3963	0.0004
298.15	0.4962	0.0004
298.15	0.5963	0.0004
298.15	0.6998	0.0005
298.15	0.7992	0.0005
298.15	0.9005	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0004
303.15	0.0474	0.0004
303.15	0.0970	0.0004
303.15	0.1956	0.0004
303.15	0.2999	0.0004
303.15	0.3963	0.0004
303.15	0.4962	0.0004
303.15	0.5963	0.0004
303.15	0.6998	0.0004
303.15	0.7992	0.0004
303.15	0.9005	0.0005
303.15	1.0000	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0005
293.15	0.0474	0.0004
293.15	0.0970	0.0004
293.15	0.1956	0.0004
293.15	0.2999	0.0004
293.15	0.3963	0.0004
293.15	0.4962	0.0005
293.15	0.5963	0.0005
293.15	0.6998	0.0005
293.15	0.7992	0.0005
293.15	0.9005	0.0005
293.15	1.0000	0.0006
298.15	0.0000	0.0004
298.15	0.0474	0.0004
298.15	0.0970	0.0004
298.15	0.1956	0.0004
298.15	0.2999	0.0004
298.15	0.3963	0.0004
298.15	0.4962	0.0004
298.15	0.5963	0.0004
298.15	0.6998	0.0005
298.15	0.7992	0.0005
298.15	0.9005	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0004
303.15	0.0474	0.0004
303.15	0.0970	0.0004
303.15	0.1956	0.0004
303.15	0.2999	0.0004
303.15	0.3963	0.0004
303.15	0.4962	0.0004
303.15	0.5963	0.0004
303.15	0.6998	0.0004
303.15	0.7992	0.0004
303.15	0.9005	0.0005
303.15	1.0000	0.0005

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 (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0570	0.1826
0.0860	0.2725
0.1130	0.3338
0.1880	0.5232
0.2570	0.6803
0.3190	0.8094
0.3770	0.8971
0.4300	0.9683
0.4780	0.9958
0.5240	1.0133
0.5660	1.0091
0.6050	0.9870
0.6410	0.9774
0.6750	0.9453
0.7070	0.9102
0.7380	0.8696
0.7660	0.8218
0.7930	0.7676
0.8180	0.7113
0.8420	0.6513
0.8640	0.5854
0.8860	0.5181
0.9060	0.4465
0.9260	0.3677
0.9440	0.2846
0.9620	0.2001
0.9790	0.1059

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 (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0570	0.1826
0.0860	0.2725
0.1130	0.3338
0.1880	0.5232
0.2570	0.6803
0.3190	0.8094
0.3770	0.8971
0.4300	0.9683
0.4780	0.9958
0.5240	1.0133
0.5660	1.0091
0.6050	0.9870
0.6410	0.9774
0.6750	0.9453
0.7070	0.9102
0.7380	0.8696
0.7660	0.8218
0.7930	0.7676
0.8180	0.7113
0.8420	0.6513
0.8640	0.5854
0.8860	0.5181
0.9060	0.4465
0.9260	0.3677
0.9440	0.2846
0.9620	0.2001
0.9790	0.1059

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	900.52
293.15	0.0474	898.51
293.15	0.0970	896.18
293.15	0.1956	891.18
293.15	0.2999	884.93
293.15	0.3963	878.26
293.15	0.4962	870.14
293.15	0.5963	860.45
293.15	0.6998	848.26
293.15	0.7992	833.88
293.15	0.9005	815.52
293.15	1.0000	791.9
298.15	0.0000	894.43
298.15	0.0474	892.43
298.15	0.0970	890.12
298.15	0.1956	885.16
298.15	0.2999	878.99
298.15	0.3963	872.38
298.15	0.4962	864.36
298.15	0.5963	854.82
298.15	0.6998	842.81
298.15	0.7992	828.62
298.15	0.9005	810.5
298.15	1.0000	787.2
303.15	0.0000	888.3
303.15	0.0474	886.3
303.15	0.0970	884.01
303.15	0.1956	879.09
303.15	0.2999	872.98
303.15	0.3963	866.46
303.15	0.4962	858.55
303.15	0.5963	849.15
303.15	0.6998	837.3
303.15	0.7992	823.31
303.15	0.9005	805.45
303.15	1.0000	782.48

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0111	894.5
298.15	0.0223	894.6
298.15	0.0495	894.7
298.15	0.1474	894.9
298.15	0.2878	894.7
298.15	0.3556	894.4
298.15	0.4905	893.6
298.15	0.7268	892.2
298.15	0.9740	890.5
298.15	1.4085	888.2
298.15	2.4454	886.1
298.15	3.0005	886.0
303.15	0.0111	888.9
303.15	0.0223	888.8
303.15	0.0495	888.7
303.15	0.1474	888.6
303.15	0.2878	888.5
303.15	0.3556	888.3
303.15	0.4905	887.7
303.15	0.7268	886.4
303.15	0.9740	884.9
303.15	1.4085	882.6
303.15	2.4454	879.8
303.15	3.0005	879.1
308.15	0.0111	883.0
308.15	0.0223	882.9
308.15	0.0495	882.8
308.15	0.1474	882.7
308.15	0.2878	882.4
308.15	0.3556	882.1
308.15	0.4905	881.6
308.15	0.7268	880.6
308.15	0.9740	879.1
308.15	1.4085	877.0
308.15	2.4454	873.8
308.15	3.0005	873.1
313.15	0.0111	877.1
313.15	0.0223	877.0
313.15	0.0495	876.9
313.15	0.1474	876.8
313.15	0.2878	876.4
313.15	0.3556	876.2
313.15	0.4905	875.8
313.15	0.7268	874.8
313.15	0.9740	873.8
313.15	1.4085	871.6
313.15	2.4454	868.4
313.15	3.0005	867.9

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	786.8
0.0513	799.6
0.1009	810.4
0.1537	820.5
0.2028	828.9
0.2535	836.5
0.3517	849.2
0.4527	859.9
0.4983	864.1
0.6042	872.7
0.7012	879.3
0.7500	882.3
0.8036	885.3
0.8500	887.7
0.8964	890.0
0.9391	892.0
1.0000	894.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	900.52
293.15	0.0474	898.51
293.15	0.0970	896.18
293.15	0.1956	891.18
293.15	0.2999	884.93
293.15	0.3963	878.26
293.15	0.4962	870.14
293.15	0.5963	860.45
293.15	0.6998	848.26
293.15	0.7992	833.88
293.15	0.9005	815.52
293.15	1.0000	791.9
298.15	0.0000	894.43
298.15	0.0474	892.43
298.15	0.0970	890.12
298.15	0.1956	885.16
298.15	0.2999	878.99
298.15	0.3963	872.38
298.15	0.4962	864.36
298.15	0.5963	854.82
298.15	0.6998	842.81
298.15	0.7992	828.62
298.15	0.9005	810.5
298.15	1.0000	787.2
303.15	0.0000	888.3
303.15	0.0474	886.3
303.15	0.0970	884.01
303.15	0.1956	879.09
303.15	0.2999	872.98
303.15	0.3963	866.46
303.15	0.4962	858.55
303.15	0.5963	849.15
303.15	0.6998	837.3
303.15	0.7992	823.31
303.15	0.9005	805.45
303.15	1.0000	782.48

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0111	894.5
298.15	0.0223	894.6
298.15	0.0495	894.7
298.15	0.1474	894.9
298.15	0.2878	894.7
298.15	0.3556	894.4
298.15	0.4905	893.6
298.15	0.7268	892.2
298.15	0.9740	890.5
298.15	1.4085	888.2
298.15	2.4454	886.1
298.15	3.0005	886.0
303.15	0.0111	888.9
303.15	0.0223	888.8
303.15	0.0495	888.7
303.15	0.1474	888.6
303.15	0.2878	888.5
303.15	0.3556	888.3
303.15	0.4905	887.7
303.15	0.7268	886.4
303.15	0.9740	884.9
303.15	1.4085	882.6
303.15	2.4454	879.8
303.15	3.0005	879.1
308.15	0.0111	883.0
308.15	0.0223	882.9
308.15	0.0495	882.8
308.15	0.1474	882.7
308.15	0.2878	882.4
308.15	0.3556	882.1
308.15	0.4905	881.6
308.15	0.7268	880.6
308.15	0.9740	879.1
308.15	1.4085	877.0
308.15	2.4454	873.8
308.15	3.0005	873.1
313.15	0.0111	877.1
313.15	0.0223	877.0
313.15	0.0495	876.9
313.15	0.1474	876.8
313.15	0.2878	876.4
313.15	0.3556	876.2
313.15	0.4905	875.8
313.15	0.7268	874.8
313.15	0.9740	873.8
313.15	1.4085	871.6
313.15	2.4454	868.4
313.15	3.0005	867.9

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	786.8
0.0513	799.6
0.1009	810.4
0.1537	820.5
0.2028	828.9
0.2535	836.5
0.3517	849.2
0.4527	859.9
0.4983	864.1
0.6042	872.7
0.7012	879.3
0.7500	882.3
0.8036	885.3
0.8500	887.7
0.8964	890.0
0.9391	892.0
1.0000	894.6

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Methyl Alcohol (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0111	1110.0
298.15	0.0223	1113.0
298.15	0.0495	1116.0
298.15	0.1474	1119.0
298.15	0.2878	1122.0
298.15	0.3556	1125.0
298.15	0.4905	1128.0
298.15	0.7268	1131.0
298.15	0.9740	1134.0
298.15	1.4085	1137.0
298.15	2.4454	1140.0
298.15	3.0005	1143.0
303.15	0.0111	1086.0
303.15	0.0223	1089.0
303.15	0.0495	1092.0
303.15	0.1474	1095.0
303.15	0.2878	1098.0
303.15	0.3556	1101.0
303.15	0.4905	1104.0
303.15	0.7268	1107.0
303.15	0.9740	1110.0
303.15	1.4085	1113.0
303.15	2.4454	1116.0
303.15	3.0005	1122.0
308.15	0.0111	1059.0
308.15	0.0223	1062.0
308.15	0.0495	1065.0
308.15	0.1474	1068.0
308.15	0.2878	1071.0
308.15	0.3556	1074.0
308.15	0.4905	1077.0
308.15	0.7268	1080.0
308.15	0.9740	1089.0
308.15	1.4085	1092.0
308.15	2.4454	1095.0
308.15	3.0005	1098.0
313.15	0.0111	1038.0
313.15	0.0223	1041.0
313.15	0.0495	1044.0
313.15	0.1474	1047.0
313.15	0.2878	1050.0
313.15	0.3556	1053.0
313.15	0.4905	1056.0
313.15	0.7268	1059.0
313.15	0.9740	1062.0
313.15	1.4085	1065.0
313.15	2.4454	1068.0
313.15	3.0005	1071.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Methyl Alcohol (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0111	1110.0
298.15	0.0223	1113.0
298.15	0.0495	1116.0
298.15	0.1474	1119.0
298.15	0.2878	1122.0
298.15	0.3556	1125.0
298.15	0.4905	1128.0
298.15	0.7268	1131.0
298.15	0.9740	1134.0
298.15	1.4085	1137.0
298.15	2.4454	1140.0
298.15	3.0005	1143.0
303.15	0.0111	1086.0
303.15	0.0223	1089.0
303.15	0.0495	1092.0
303.15	0.1474	1095.0
303.15	0.2878	1098.0
303.15	0.3556	1101.0
303.15	0.4905	1104.0
303.15	0.7268	1107.0
303.15	0.9740	1110.0
303.15	1.4085	1113.0
303.15	2.4454	1116.0
303.15	3.0005	1122.0
308.15	0.0111	1059.0
308.15	0.0223	1062.0
308.15	0.0495	1065.0
308.15	0.1474	1068.0
308.15	0.2878	1071.0
308.15	0.3556	1074.0
308.15	0.4905	1077.0
308.15	0.7268	1080.0
308.15	0.9740	1089.0
308.15	1.4085	1092.0
308.15	2.4454	1095.0
308.15	3.0005	1098.0
313.15	0.0111	1038.0
313.15	0.0223	1041.0
313.15	0.0495	1044.0
313.15	0.1474	1047.0
313.15	0.2878	1050.0
313.15	0.3556	1053.0
313.15	0.4905	1056.0
313.15	0.7268	1059.0
313.15	0.9740	1062.0
313.15	1.4085	1065.0
313.15	2.4454	1068.0
313.15	3.0005	1071.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	337.68
0.0300	337.12
0.0720	336.49
0.1450	335.87
0.2110	335.59
0.2440	335.64
0.3030	335.77
0.3650	335.94
0.4190	336.17
0.4870	336.39
0.5310	336.61
0.6100	337.05
0.6720	337.53
0.7340	338.29
0.8010	339.65
0.8650	341.59
0.9130	343.71
0.9520	346.22
0.9830	348.74
1.0000	350.35

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	337.45
0.0230	337.29
0.0490	336.85
0.0770	336.49
0.1130	336.12
0.1580	335.80
0.1980	335.62
0.2660	335.45
0.3220	335.50
0.4280	335.70
0.5400	336.26
0.6730	337.48
0.8090	339.95
0.8980	343.06
0.9610	346.80
1.0000	349.95

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	100.00	337.85
0.0000	500.00	385.35
0.0000	700.00	397.55
0.0130	100.00	337.65
0.0220	500.00	384.85
0.0260	100.00	337.35
0.0290	500.00	384.75
0.0350	700.00	396.75
0.0390	500.00	384.65
0.0450	500.00	384.55
0.0460	700.00	396.65
0.0580	500.00	384.45
0.0580	700.00	396.55
0.0670	100.00	336.85
0.0720	500.00	384.35
0.0770	700.00	396.35
0.0810	100.00	336.65
0.0920	500.00	384.25
0.0990	700.00	396.25
0.1110	100.00	336.35
0.1120	700.00	396.25
0.1130	500.00	384.15
0.1280	700.00	396.25
0.1440	500.00	384.05
0.1440	700.00	396.25
0.1610	500.00	384.05
0.1610	700.00	396.25
0.1660	100.00	335.95
0.1780	700.00	396.25
0.1890	100.00	335.85
0.1900	500.00	384.05
0.2070	500.00	384.05
0.2210	500.00	384.05
0.2270	700.00	396.45
0.2400	500.00	384.15
0.2460	100.00	335.65
0.2540	700.00	396.65
0.2600	100.00	335.65
0.2880	100.00	335.65
0.2890	500.00	384.35
0.2890	700.00	396.85
0.3120	700.00	397.05
0.3270	100.00	335.75
0.3440	500.00	384.65
0.3700	500.00	384.85
0.3700	700.00	397.65
0.3880	500.00	385.05
0.3970	100.00	335.95
0.4160	700.00	398.25
0.4460	100.00	336.15
0.4460	700.00	398.55
0.4670	500.00	385.85
0.4780	100.00	336.25
0.5010	500.00	386.35
0.5130	100.00	336.45
0.5130	700.00	399.65
0.5500	100.00	336.75
0.5910	100.00	337.05
0.5910	500.00	387.75
0.5910	700.00	401.25
0.6200	500.00	388.35
0.6670	100.00	337.95
0.6670	700.00	403.35
0.7010	100.00	338.45
0.7180	700.00	405.15
0.7540	700.00	406.35
0.7730	100.00	339.65
0.7730	500.00	392.35
0.8120	700.00	408.85
0.8720	100.00	342.75
0.8720	500.00	396.65
0.9120	100.00	343.95
0.9320	100.00	344.85
0.9320	500.00	400.65
0.9520	100.00	345.95
0.9520	700.00	418.45
0.9720	100.00	347.05
0.9720	700.00	420.85
0.9910	500.00	407.45
1.0000	100.00	350.15
1.0000	500.00	408.75
1.0000	700.00	423.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	337.68
0.0300	337.12
0.0720	336.49
0.1450	335.87
0.2110	335.59
0.2440	335.64
0.3030	335.77
0.3650	335.94
0.4190	336.17
0.4870	336.39
0.5310	336.61
0.6100	337.05
0.6720	337.53
0.7340	338.29
0.8010	339.65
0.8650	341.59
0.9130	343.71
0.9520	346.22
0.9830	348.74
1.0000	350.35

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	337.45
0.0230	337.29
0.0490	336.85
0.0770	336.49
0.1130	336.12
0.1580	335.80
0.1980	335.62
0.2660	335.45
0.3220	335.50
0.4280	335.70
0.5400	336.26
0.6730	337.48
0.8090	339.95
0.8980	343.06
0.9610	346.80
1.0000	349.95

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	100.00	337.85
0.0000	500.00	385.35
0.0000	700.00	397.55
0.0130	100.00	337.65
0.0220	500.00	384.85
0.0260	100.00	337.35
0.0290	500.00	384.75
0.0350	700.00	396.75
0.0390	500.00	384.65
0.0450	500.00	384.55
0.0460	700.00	396.65
0.0580	500.00	384.45
0.0580	700.00	396.55
0.0670	100.00	336.85
0.0720	500.00	384.35
0.0770	700.00	396.35
0.0810	100.00	336.65
0.0920	500.00	384.25
0.0990	700.00	396.25
0.1110	100.00	336.35
0.1120	700.00	396.25
0.1130	500.00	384.15
0.1280	700.00	396.25
0.1440	500.00	384.05
0.1440	700.00	396.25
0.1610	500.00	384.05
0.1610	700.00	396.25
0.1660	100.00	335.95
0.1780	700.00	396.25
0.1890	100.00	335.85
0.1900	500.00	384.05
0.2070	500.00	384.05
0.2210	500.00	384.05
0.2270	700.00	396.45
0.2400	500.00	384.15
0.2460	100.00	335.65
0.2540	700.00	396.65
0.2600	100.00	335.65
0.2880	100.00	335.65
0.2890	500.00	384.35
0.2890	700.00	396.85
0.3120	700.00	397.05
0.3270	100.00	335.75
0.3440	500.00	384.65
0.3700	500.00	384.85
0.3700	700.00	397.65
0.3880	500.00	385.05
0.3970	100.00	335.95
0.4160	700.00	398.25
0.4460	100.00	336.15
0.4460	700.00	398.55
0.4670	500.00	385.85
0.4780	100.00	336.25
0.5010	500.00	386.35
0.5130	100.00	336.45
0.5130	700.00	399.65
0.5500	100.00	336.75
0.5910	100.00	337.05
0.5910	500.00	387.75
0.5910	700.00	401.25
0.6200	500.00	388.35
0.6670	100.00	337.95
0.6670	700.00	403.35
0.7010	100.00	338.45
0.7180	700.00	405.15
0.7540	700.00	406.35
0.7730	100.00	339.65
0.7730	500.00	392.35
0.8120	700.00	408.85
0.8720	100.00	342.75
0.8720	500.00	396.65
0.9120	100.00	343.95
0.9320	100.00	344.85
0.9320	500.00	400.65
0.9520	100.00	345.95
0.9520	700.00	418.45
0.9720	100.00	347.05
0.9720	700.00	420.85
0.9910	500.00	407.45
1.0000	100.00	350.15
1.0000	500.00	408.75
1.0000	700.00	423.95

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
347.95	0.0190	0.0790
347.15	0.0240	0.0930
345.45	0.0560	0.1810
340.25	0.1810	0.3840
337.85	0.3110	0.4920
337.35	0.3500	0.5200
336.75	0.4030	0.5570
335.75	0.5660	0.6400
335.55	0.6160	0.6750
335.55	0.6460	0.6780
335.45	0.7080	0.7110
335.25	0.7200	0.7160
335.45	0.7340	0.7170
335.65	0.7430	0.7320
335.75	0.7440	0.7330
335.65	0.8100	0.7790
335.55	0.8150	0.7840
335.95	0.8890	0.8460
336.45	0.9390	0.9030

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 312.91 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
32.797	0.1290	0.3440
36.037	0.2320	0.4400
37.664	0.3110	0.5020
38.663	0.3920	0.5540
39.863	0.5070	0.6320
39.997	0.5520	0.6400
39.863	0.6410	0.6590
39.997	0.6730	0.6750
39.997	0.7210	0.7090
40.13	0.7660	0.7290
39.09	0.8600	0.8080
38.33	0.9110	0.8510
37.197	0.9510	0.9060

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 313.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
30.864	0.0500	0.2115
30.864	0.0670	0.2130
31.997	0.0970	0.2620
34.53	0.1540	0.3718
35.797	0.2175	0.4242
37.864	0.2620	0.4695
38.597	0.3000	0.4912
39.53	0.3820	0.5356
39.73	0.4500	0.5360
40.53	0.5680	0.6150
40.663	0.6560	0.6600
40.263	0.7190	0.6940
40.463	0.7800	0.7300
40.197	0.8100	0.7495

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• 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
• Isobaric Vapor - Liquid Equilibrium for Ethyl acetate + Methanol + Ionic Liquids Ternary systems at 101.3 kPa
• Effect of Ionic Liquids on the Binary Vapor-Liquid Equilibrium of Ethyl Acetate + Methanol System at 101.3 kPa
• Vapor-Liquid Equilibria for Ethyl Acetate + Methanol at (0.1, 0.5, and 0.7) MPa. Measurements with a New Ebulliometer