Mixture of Octane + Ethyl Acetate

Datasets

1. Mole fraction (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. ρ_l - Mass density, kg/m3 (2)
4. T_boil - Boiling temperature at pressure P, 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
0.0150	0.0940
0.0330	0.1980
0.0590	0.3150
0.0770	0.3760
0.1010	0.4450
0.1180	0.4900
0.1410	0.5370
0.1720	0.5940
0.2040	0.6410
0.2590	0.7020
0.2990	0.7310
0.3620	0.7700
0.4000	0.7850
0.4620	0.8080
0.5190	0.8110
0.6020	0.8370
0.6660	0.8540
0.7390	0.8760
0.7880	0.8980
0.8450	0.9210
0.8810	0.9360
0.9060	0.9490
0.9330	0.9640
0.9580	0.9760
0.9910	0.9950
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
0.0150	0.0940
0.0330	0.1980
0.0590	0.3150
0.0770	0.3760
0.1010	0.4450
0.1180	0.4900
0.1410	0.5370
0.1720	0.5940
0.2040	0.6410
0.2590	0.7020
0.2990	0.7310
0.3620	0.7700
0.4000	0.7850
0.4620	0.8080
0.5190	0.8110
0.6020	0.8370
0.6660	0.8540
0.7390	0.8760
0.7880	0.8980
0.8450	0.9210
0.8810	0.9360
0.9060	0.9490
0.9330	0.9640
0.9580	0.9760
0.9910	0.9950
1.0000	1.0000

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	0.0994	0.6110
291.15	0.1715	0.9630
291.15	0.2540	1.266
291.15	0.3369	1.486
291.15	0.4081	1.604
291.15	0.4740	1.669
291.15	0.5317	1.673
291.15	0.5698	1.641
291.15	0.5955	1.615
291.15	0.6441	1.553
291.15	0.6953	1.44
291.15	0.7435	1.308
291.15	0.7996	1.139
291.15	0.8530	0.9440
291.15	0.8967	0.7370
291.15	0.9435	0.4920
291.15	0.9810	0.2430
298.15	0.0774	0.4260
298.15	0.1517	0.7450
298.15	0.2198	1.017
298.15	0.2861	1.225
298.15	0.3374	1.366
298.15	0.3769	1.474
298.15	0.4335	1.576
298.15	0.4856	1.605
298.15	0.5281	1.604
298.15	0.5773	1.588
298.15	0.6255	1.551
298.15	0.6736	1.468
298.15	0.7261	1.359
298.15	0.7729	1.222
298.15	0.8276	1.028
298.15	0.8796	0.8010
298.15	0.9202	0.5400
298.15	0.9644	0.2710
318.15	0.0832	0.4630
318.15	0.1591	0.8140
318.15	0.2322	1.119
318.15	0.3009	1.335
318.15	0.3637	1.477
318.15	0.4184	1.564
318.15	0.4655	1.607
318.15	0.5112	1.625
318.15	0.5525	1.613
318.15	0.5886	1.598
318.15	0.6324	1.554
318.15	0.6807	1.485
318.15	0.7307	1.374
318.15	0.7788	1.225
318.15	0.8291	1.036
318.15	0.8801	0.8040
318.15	0.9259	0.5440
318.15	0.9646	0.2790

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	0.0994	0.6110
291.15	0.1715	0.9630
291.15	0.2540	1.266
291.15	0.3369	1.486
291.15	0.4081	1.604
291.15	0.4740	1.669
291.15	0.5317	1.673
291.15	0.5698	1.641
291.15	0.5955	1.615
291.15	0.6441	1.553
291.15	0.6953	1.44
291.15	0.7435	1.308
291.15	0.7996	1.139
291.15	0.8530	0.9440
291.15	0.8967	0.7370
291.15	0.9435	0.4920
291.15	0.9810	0.2430
298.15	0.0774	0.4260
298.15	0.1517	0.7450
298.15	0.2198	1.017
298.15	0.2861	1.225
298.15	0.3374	1.366
298.15	0.3769	1.474
298.15	0.4335	1.576
298.15	0.4856	1.605
298.15	0.5281	1.604
298.15	0.5773	1.588
298.15	0.6255	1.551
298.15	0.6736	1.468
298.15	0.7261	1.359
298.15	0.7729	1.222
298.15	0.8276	1.028
298.15	0.8796	0.8010
298.15	0.9202	0.5400
298.15	0.9644	0.2710
318.15	0.0832	0.4630
318.15	0.1591	0.8140
318.15	0.2322	1.119
318.15	0.3009	1.335
318.15	0.3637	1.477
318.15	0.4184	1.564
318.15	0.4655	1.607
318.15	0.5112	1.625
318.15	0.5525	1.613
318.15	0.5886	1.598
318.15	0.6324	1.554
318.15	0.6807	1.485
318.15	0.7307	1.374
318.15	0.7788	1.225
318.15	0.8291	1.036
318.15	0.8801	0.8040
318.15	0.9259	0.5440
318.15	0.9646	0.2790

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	704.13
291.15	0.0296	707.15
291.15	0.0628	710.48
291.15	0.1163	716.36
291.15	0.1605	721.46
291.15	0.2056	727.01
291.15	0.2901	738.23
291.15	0.3723	750.35
291.15	0.4427	761.76
291.15	0.5131	774.24
291.15	0.5744	785.94
291.15	0.6332	798.14
291.15	0.6886	810.54
291.15	0.7414	823.25
291.15	0.7945	836.98
291.15	0.8400	849.83
291.15	0.8950	866.53
291.15	0.9304	878.05
291.15	0.9523	885.46
291.15	1.0000	902.88
298.15	0.0000	698.6
298.15	0.0485	703.3
298.15	0.0998	708.8
298.15	0.1711	716.9
298.15	0.2518	727.02
298.15	0.3198	736.29
298.15	0.3814	745.42
298.15	0.4622	758.48
298.15	0.4977	764.69
298.15	0.5598	776.23
298.15	0.6548	795.8
298.15	0.6729	799.8
298.15	0.6865	802.9
298.15	0.7550	819.2
298.15	0.7913	828.6
298.15	0.8335	840.2
298.15	0.8686	850.5
298.15	0.9039	861.4
298.15	0.9578	879.3
298.15	1.0000	894.4
318.15	0.0000	682.16
318.15	0.0340	685.37
318.15	0.1080	692.6
318.15	0.1961	702.19
318.15	0.2859	713.24
318.15	0.3635	723.8
318.15	0.4203	732.23
318.15	0.4875	743.04
318.15	0.5678	757.24
318.15	0.6088	765.1
318.15	0.6633	776.23
318.15	0.7123	786.92
318.15	0.7640	799.14
318.15	0.8086	810.54
318.15	0.8487	821.51
318.15	0.8943	834.53
318.15	0.9320	846.34
318.15	0.9762	860.93
318.15	1.0000	869.6
328.15	0.0000	674.15
328.15	0.0441	678.0
328.15	0.1138	684.7
328.15	0.2084	694.85
328.15	0.2915	704.8
328.15	0.3741	715.9
328.15	0.4415	725.91
328.15	0.5234	739.31
328.15	0.5735	748.22
328.15	0.6354	760.07
328.15	0.6861	770.65
328.15	0.7435	783.45
328.15	0.7958	796.07
328.15	0.8407	807.86
328.15	0.8822	819.28
328.15	0.9270	832.83
328.15	0.9737	848.01
328.15	1.0000	857.17

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	704.13
291.15	0.0296	707.15
291.15	0.0628	710.48
291.15	0.1163	716.36
291.15	0.1605	721.46
291.15	0.2056	727.01
291.15	0.2901	738.23
291.15	0.3723	750.35
291.15	0.4427	761.76
291.15	0.5131	774.24
291.15	0.5744	785.94
291.15	0.6332	798.14
291.15	0.6886	810.54
291.15	0.7414	823.25
291.15	0.7945	836.98
291.15	0.8400	849.83
291.15	0.8950	866.53
291.15	0.9304	878.05
291.15	0.9523	885.46
291.15	1.0000	902.88
298.15	0.0000	698.6
298.15	0.0485	703.3
298.15	0.0998	708.8
298.15	0.1711	716.9
298.15	0.2518	727.02
298.15	0.3198	736.29
298.15	0.3814	745.42
298.15	0.4622	758.48
298.15	0.4977	764.69
298.15	0.5598	776.23
298.15	0.6548	795.8
298.15	0.6729	799.8
298.15	0.6865	802.9
298.15	0.7550	819.2
298.15	0.7913	828.6
298.15	0.8335	840.2
298.15	0.8686	850.5
298.15	0.9039	861.4
298.15	0.9578	879.3
298.15	1.0000	894.4
318.15	0.0000	682.16
318.15	0.0340	685.37
318.15	0.1080	692.6
318.15	0.1961	702.19
318.15	0.2859	713.24
318.15	0.3635	723.8
318.15	0.4203	732.23
318.15	0.4875	743.04
318.15	0.5678	757.24
318.15	0.6088	765.1
318.15	0.6633	776.23
318.15	0.7123	786.92
318.15	0.7640	799.14
318.15	0.8086	810.54
318.15	0.8487	821.51
318.15	0.8943	834.53
318.15	0.9320	846.34
318.15	0.9762	860.93
318.15	1.0000	869.6
328.15	0.0000	674.15
328.15	0.0441	678.0
328.15	0.1138	684.7
328.15	0.2084	694.85
328.15	0.2915	704.8
328.15	0.3741	715.9
328.15	0.4415	725.91
328.15	0.5234	739.31
328.15	0.5735	748.22
328.15	0.6354	760.07
328.15	0.6861	770.65
328.15	0.7435	783.45
328.15	0.7958	796.07
328.15	0.8407	807.86
328.15	0.8822	819.28
328.15	0.9270	832.83
328.15	0.9737	848.01
328.15	1.0000	857.17

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	398.83
0.0150	395.85
0.0330	392.41
0.0590	387.83
0.0770	385.17
0.1010	382.11
0.1180	380.00
0.1410	377.52
0.1720	374.42
0.2040	371.76
0.2590	367.92
0.2990	365.92
0.3620	363.34
0.4000	362.37
0.4620	360.68
0.5190	359.34
0.6020	357.54
0.6660	356.38
0.7390	354.98
0.7880	353.68
0.8450	352.80
0.8810	352.08
0.9060	351.55
0.9330	351.06
0.9580	350.69
0.9910	350.23
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	398.83
0.0150	395.85
0.0330	392.41
0.0590	387.83
0.0770	385.17
0.1010	382.11
0.1180	380.00
0.1410	377.52
0.1720	374.42
0.2040	371.76
0.2590	367.92
0.2990	365.92
0.3620	363.34
0.4000	362.37
0.4620	360.68
0.5190	359.34
0.6020	357.54
0.6660	356.38
0.7390	354.98
0.7880	353.68
0.8450	352.80
0.8810	352.08
0.9060	351.55
0.9330	351.06
0.9580	350.69
0.9910	350.23
1.0000	350.15

Sources

• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)