Mixture of Butanoic acid, ethyl ester + Nonane

Datasets

1. Mole fraction (2)
2. ρ_l - Mass density, kg/m3 (2)
3. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Butanoic acid, ethyl ester (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, ethyl ester (1) - Liquid	Mole fraction of Butanoic acid, ethyl ester (1) - Gas
0.0000	0.0000
0.0140	0.0390
0.0420	0.1120
0.0620	0.1630
0.0800	0.2040
0.0980	0.2440
0.1220	0.2890
0.1440	0.3300
0.1660	0.3640
0.2150	0.4300
0.2310	0.4510
0.2480	0.4700
0.2680	0.4910
0.2890	0.5130
0.3100	0.5390
0.3340	0.5620
0.3560	0.5820
0.3800	0.6050
0.4050	0.6250
0.4360	0.6470
0.4630	0.6650
0.4860	0.6840
0.5160	0.7060
0.5500	0.7240
0.5790	0.7440
0.6090	0.7630
0.6420	0.7800
0.6710	0.7970
0.7110	0.8210
0.7390	0.8410
0.7790	0.8600
0.8120	0.8790
0.8360	0.8960
0.8610	0.9080
0.8870	0.9250
0.9060	0.9380
0.9290	0.9510
0.9460	0.9630
0.9630	0.9740
0.9800	0.9850
0.9920	0.9940
1.0000	1.0000

Mole fraction of Butanoic acid, ethyl ester (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, ethyl ester (1) - Liquid	Mole fraction of Butanoic acid, ethyl ester (1) - Gas
0.0000	0.0000
0.0140	0.0390
0.0420	0.1120
0.0620	0.1630
0.0800	0.2040
0.0980	0.2440
0.1220	0.2890
0.1440	0.3300
0.1660	0.3640
0.2150	0.4300
0.2310	0.4510
0.2480	0.4700
0.2680	0.4910
0.2890	0.5130
0.3100	0.5390
0.3340	0.5620
0.3560	0.5820
0.3800	0.6050
0.4050	0.6250
0.4360	0.6470
0.4630	0.6650
0.4860	0.6840
0.5160	0.7060
0.5500	0.7240
0.5790	0.7440
0.6090	0.7630
0.6420	0.7800
0.6710	0.7970
0.7110	0.8210
0.7390	0.8410
0.7790	0.8600
0.8120	0.8790
0.8360	0.8960
0.8610	0.9080
0.8870	0.9250
0.9060	0.9380
0.9290	0.9510
0.9460	0.9630
0.9630	0.9740
0.9800	0.9850
0.9920	0.9940
1.0000	1.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Butanoic acid, ethyl ester (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	288.15	721.65
0.0000	298.15	713.85
0.0000	308.15	705.96
0.0000	318.15	698.06
0.0000	328.15	690.17
0.0379	288.15	725.8
0.0435	318.15	702.45
0.0481	328.15	695.05
0.0486	298.15	719.05
0.0505	308.15	711.25
0.0818	308.15	714.63
0.0906	298.15	723.69
0.1007	298.15	724.84
0.1009	318.15	708.56
0.1046	288.15	733.19
0.1134	328.15	701.93
0.1439	318.15	713.46
0.1495	298.15	730.49
0.1502	288.15	738.59
0.1528	308.15	722.65
0.1627	328.15	707.35
0.1872	308.15	726.67
0.2001	318.15	719.85
0.2013	288.15	744.84
0.2102	328.15	712.81
0.2112	308.15	729.53
0.2442	298.15	742.05
0.2489	318.15	725.77
0.2499	288.15	751.04
0.2589	328.15	718.53
0.2818	308.15	738.36
0.2861	318.15	730.43
0.2985	298.15	749.08
0.3047	288.15	758.28
0.3111	328.15	725.0
0.3131	298.15	750.97
0.3302	308.15	744.66
0.3427	288.15	763.5
0.3518	298.15	756.23
0.3550	318.15	739.26
0.3588	328.15	731.17
0.3685	308.15	749.81
0.3961	288.15	771.2
0.4020	318.15	745.62
0.4020	328.15	736.91
0.4260	308.15	757.85
0.4355	288.15	776.9
0.4357	298.15	768.18
0.4556	318.15	753.18
0.4562	328.15	744.36
0.4773	308.15	765.37
0.4957	288.15	786.1
0.4988	318.15	759.53
0.5028	298.15	778.32
0.5187	308.15	771.59
0.5455	288.15	794.1
0.5470	318.15	766.88
0.5511	298.15	785.92
0.5565	328.15	759.06
0.5712	308.15	779.88
0.5857	288.15	800.8
0.5974	298.15	793.57
0.5996	328.15	765.77
0.6011	318.15	775.45
0.6420	308.15	791.55
0.6498	288.15	811.8
0.6524	328.15	774.29
0.6560	318.15	784.53
0.6753	308.15	797.37
0.6951	318.15	791.27
0.7030	298.15	811.93
0.7062	328.15	783.42
0.7067	288.15	822.09
0.7260	308.15	806.38
0.7460	298.15	819.92
0.7520	288.15	830.65
0.7543	318.15	801.83
0.7544	328.15	791.91
0.7822	308.15	816.86
0.7879	298.15	827.92
0.7999	318.15	810.52
0.8019	288.15	840.45
0.8060	328.15	801.44
0.8330	308.15	826.88
0.8433	328.15	808.67
0.8485	318.15	819.97
0.8502	288.15	850.42
0.8532	298.15	841.01
0.8780	308.15	836.1
0.8917	328.15	818.28
0.8947	318.15	829.27
0.9040	288.15	861.91
0.9053	298.15	852.07
0.9384	308.15	848.96
0.9532	328.15	831.23
0.9545	318.15	842.03
0.9569	288.15	873.91
1.0000	288.15	884.01
1.0000	298.15	873.5
1.0000	308.15	862.85
1.0000	318.15	852.26
1.0000	328.15	841.55

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Butanoic acid, ethyl ester (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	288.15	721.65
0.0000	298.15	713.85
0.0000	308.15	705.96
0.0000	318.15	698.06
0.0000	328.15	690.17
0.0379	288.15	725.8
0.0435	318.15	702.45
0.0481	328.15	695.05
0.0486	298.15	719.05
0.0505	308.15	711.25
0.0818	308.15	714.63
0.0906	298.15	723.69
0.1007	298.15	724.84
0.1009	318.15	708.56
0.1046	288.15	733.19
0.1134	328.15	701.93
0.1439	318.15	713.46
0.1495	298.15	730.49
0.1502	288.15	738.59
0.1528	308.15	722.65
0.1627	328.15	707.35
0.1872	308.15	726.67
0.2001	318.15	719.85
0.2013	288.15	744.84
0.2102	328.15	712.81
0.2112	308.15	729.53
0.2442	298.15	742.05
0.2489	318.15	725.77
0.2499	288.15	751.04
0.2589	328.15	718.53
0.2818	308.15	738.36
0.2861	318.15	730.43
0.2985	298.15	749.08
0.3047	288.15	758.28
0.3111	328.15	725.0
0.3131	298.15	750.97
0.3302	308.15	744.66
0.3427	288.15	763.5
0.3518	298.15	756.23
0.3550	318.15	739.26
0.3588	328.15	731.17
0.3685	308.15	749.81
0.3961	288.15	771.2
0.4020	318.15	745.62
0.4020	328.15	736.91
0.4260	308.15	757.85
0.4355	288.15	776.9
0.4357	298.15	768.18
0.4556	318.15	753.18
0.4562	328.15	744.36
0.4773	308.15	765.37
0.4957	288.15	786.1
0.4988	318.15	759.53
0.5028	298.15	778.32
0.5187	308.15	771.59
0.5455	288.15	794.1
0.5470	318.15	766.88
0.5511	298.15	785.92
0.5565	328.15	759.06
0.5712	308.15	779.88
0.5857	288.15	800.8
0.5974	298.15	793.57
0.5996	328.15	765.77
0.6011	318.15	775.45
0.6420	308.15	791.55
0.6498	288.15	811.8
0.6524	328.15	774.29
0.6560	318.15	784.53
0.6753	308.15	797.37
0.6951	318.15	791.27
0.7030	298.15	811.93
0.7062	328.15	783.42
0.7067	288.15	822.09
0.7260	308.15	806.38
0.7460	298.15	819.92
0.7520	288.15	830.65
0.7543	318.15	801.83
0.7544	328.15	791.91
0.7822	308.15	816.86
0.7879	298.15	827.92
0.7999	318.15	810.52
0.8019	288.15	840.45
0.8060	328.15	801.44
0.8330	308.15	826.88
0.8433	328.15	808.67
0.8485	318.15	819.97
0.8502	288.15	850.42
0.8532	298.15	841.01
0.8780	308.15	836.1
0.8917	328.15	818.28
0.8947	318.15	829.27
0.9040	288.15	861.91
0.9053	298.15	852.07
0.9384	308.15	848.96
0.9532	328.15	831.23
0.9545	318.15	842.03
0.9569	288.15	873.91
1.0000	288.15	884.01
1.0000	298.15	873.5
1.0000	308.15	862.85
1.0000	318.15	852.26
1.0000	328.15	841.55

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, ethyl ester (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	423.90
0.0140	422.86
0.0420	420.81
0.0620	419.42
0.0800	418.32
0.0980	417.15
0.1220	415.85
0.1440	414.64
0.1660	413.58
0.2150	411.47
0.2310	410.77
0.2480	410.15
0.2680	409.47
0.2890	408.66
0.3100	407.83
0.3340	407.06
0.3560	406.31
0.3800	405.49
0.4050	404.76
0.4360	404.04
0.4630	403.32
0.4860	402.62
0.5160	401.92
0.5500	401.28
0.5790	400.59
0.6090	399.95
0.6420	399.36
0.6710	398.89
0.7110	398.13
0.7390	397.59
0.7790	397.05
0.8120	396.55
0.8360	396.20
0.8610	395.90
0.8870	395.59
0.9060	395.33
0.9290	395.08
0.9460	394.89
0.9630	394.70
0.9800	394.53
0.9920	394.41
1.0000	394.31

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, ethyl ester (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	423.90
0.0140	422.86
0.0420	420.81
0.0620	419.42
0.0800	418.32
0.0980	417.15
0.1220	415.85
0.1440	414.64
0.1660	413.58
0.2150	411.47
0.2310	410.77
0.2480	410.15
0.2680	409.47
0.2890	408.66
0.3100	407.83
0.3340	407.06
0.3560	406.31
0.3800	405.49
0.4050	404.76
0.4360	404.04
0.4630	403.32
0.4860	402.62
0.5160	401.92
0.5500	401.28
0.5790	400.59
0.6090	399.95
0.6420	399.36
0.6710	398.89
0.7110	398.13
0.7390	397.59
0.7790	397.05
0.8120	396.55
0.8360	396.20
0.8610	395.90
0.8870	395.59
0.9060	395.33
0.9290	395.08
0.9460	394.89
0.9630	394.70
0.9800	394.53
0.9920	394.41
1.0000	394.31

Sources

• Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa