Mixture of Butanoic acid, ethyl ester + Heptane

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
0.0080	0.0070
0.0290	0.0230
0.0490	0.0390
0.0660	0.0520
0.0840	0.0650
0.1010	0.0780
0.1200	0.0910
0.1390	0.1040
0.1600	0.1180
0.1800	0.1310
0.2070	0.1490
0.2310	0.1640
0.2580	0.1810
0.2830	0.1960
0.3080	0.2110
0.3360	0.2290
0.3630	0.2490
0.3820	0.2610
0.4040	0.2750
0.4260	0.2900
0.4490	0.3050
0.4590	0.3120
0.4820	0.3280
0.5030	0.3430
0.5300	0.3630
0.5500	0.3800
0.5980	0.4150
0.6230	0.4360
0.7080	0.5190
0.7380	0.5540
0.8070	0.6330
0.8370	0.6770
0.8790	0.7420
0.8990	0.7800
0.9160	0.8110
0.9320	0.8410
0.9440	0.8700
0.9600	0.9010
0.9710	0.9270
0.9820	0.9540
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
0.0080	0.0070
0.0290	0.0230
0.0490	0.0390
0.0660	0.0520
0.0840	0.0650
0.1010	0.0780
0.1200	0.0910
0.1390	0.1040
0.1600	0.1180
0.1800	0.1310
0.2070	0.1490
0.2310	0.1640
0.2580	0.1810
0.2830	0.1960
0.3080	0.2110
0.3360	0.2290
0.3630	0.2490
0.3820	0.2610
0.4040	0.2750
0.4260	0.2900
0.4490	0.3050
0.4590	0.3120
0.4820	0.3280
0.5030	0.3430
0.5300	0.3630
0.5500	0.3800
0.5980	0.4150
0.6230	0.4360
0.7080	0.5190
0.7380	0.5540
0.8070	0.6330
0.8370	0.6770
0.8790	0.7420
0.8990	0.7800
0.9160	0.8110
0.9320	0.8410
0.9440	0.8700
0.9600	0.9010
0.9710	0.9270
0.9820	0.9540
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	688.16
0.0000	298.15	679.62
0.0000	308.15	670.96
0.0000	318.15	662.33
0.0000	328.15	653.61
0.0461	308.15	678.42
0.0502	288.15	696.39
0.0522	298.15	688.18
0.0532	318.15	670.78
0.0535	328.15	662.06
0.0904	298.15	694.54
0.0918	288.15	703.35
0.0950	318.15	677.56
0.0952	308.15	686.44
0.0975	328.15	669.12
0.1397	318.15	684.91
0.1404	298.15	703.05
0.1445	308.15	694.69
0.1473	288.15	712.8
0.1485	328.15	677.41
0.1785	328.15	682.4
0.1901	298.15	711.58
0.2022	288.15	722.42
0.2034	308.15	704.7
0.2087	318.15	696.59
0.2367	328.15	692.21
0.2465	288.15	730.35
0.2497	308.15	712.78
0.2539	298.15	722.68
0.2565	318.15	704.87
0.2880	288.15	737.84
0.2962	298.15	730.22
0.3034	328.15	703.69
0.3048	318.15	713.3
0.3081	308.15	723.17
0.3441	308.15	729.57
0.3543	298.15	740.87
0.3590	328.15	713.56
0.3608	318.15	723.3
0.3987	288.15	758.41
0.4000	298.15	749.31
0.4046	318.15	731.26
0.4060	308.15	741.01
0.4430	298.15	757.44
0.4488	288.15	767.94
0.4532	318.15	740.3
0.4538	328.15	730.76
0.4563	308.15	750.35
0.5008	288.15	778.03
0.5053	308.15	759.76
0.5065	318.15	750.34
0.5087	328.15	741.0
0.5456	288.15	786.84
0.5505	308.15	768.46
0.5511	328.15	749.04
0.5517	298.15	778.51
0.5517	318.15	759.04
0.6007	318.15	768.46
0.6018	298.15	788.45
0.6023	288.15	798.22
0.6038	308.15	778.99
0.6093	328.15	760.27
0.6471	328.15	767.65
0.6480	298.15	797.84
0.6492	318.15	778.12
0.6498	308.15	788.17
0.6584	288.15	809.63
0.6934	318.15	787.02
0.6967	328.15	777.52
0.6976	298.15	808.02
0.6999	288.15	818.26
0.7026	308.15	798.87
0.7390	318.15	796.28
0.7390	328.15	786.07
0.7463	298.15	818.17
0.7486	288.15	828.54
0.7544	308.15	809.6
0.7880	308.15	816.69
0.7884	298.15	827.06
0.7947	318.15	807.72
0.7999	328.15	798.54
0.8042	288.15	840.42
0.8397	328.15	806.83
0.8424	308.15	828.13
0.8473	298.15	839.64
0.8481	288.15	850.01
0.8554	318.15	820.65
0.8861	318.15	827.23
0.9009	308.15	840.82
0.9010	288.15	861.58
0.9054	298.15	852.26
0.9086	328.15	821.54
0.9347	288.15	869.11
0.9512	308.15	851.86
0.9515	318.15	841.48
0.9524	298.15	862.74
0.9527	288.15	873.2
0.9533	328.15	831.27
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	688.16
0.0000	298.15	679.62
0.0000	308.15	670.96
0.0000	318.15	662.33
0.0000	328.15	653.61
0.0461	308.15	678.42
0.0502	288.15	696.39
0.0522	298.15	688.18
0.0532	318.15	670.78
0.0535	328.15	662.06
0.0904	298.15	694.54
0.0918	288.15	703.35
0.0950	318.15	677.56
0.0952	308.15	686.44
0.0975	328.15	669.12
0.1397	318.15	684.91
0.1404	298.15	703.05
0.1445	308.15	694.69
0.1473	288.15	712.8
0.1485	328.15	677.41
0.1785	328.15	682.4
0.1901	298.15	711.58
0.2022	288.15	722.42
0.2034	308.15	704.7
0.2087	318.15	696.59
0.2367	328.15	692.21
0.2465	288.15	730.35
0.2497	308.15	712.78
0.2539	298.15	722.68
0.2565	318.15	704.87
0.2880	288.15	737.84
0.2962	298.15	730.22
0.3034	328.15	703.69
0.3048	318.15	713.3
0.3081	308.15	723.17
0.3441	308.15	729.57
0.3543	298.15	740.87
0.3590	328.15	713.56
0.3608	318.15	723.3
0.3987	288.15	758.41
0.4000	298.15	749.31
0.4046	318.15	731.26
0.4060	308.15	741.01
0.4430	298.15	757.44
0.4488	288.15	767.94
0.4532	318.15	740.3
0.4538	328.15	730.76
0.4563	308.15	750.35
0.5008	288.15	778.03
0.5053	308.15	759.76
0.5065	318.15	750.34
0.5087	328.15	741.0
0.5456	288.15	786.84
0.5505	308.15	768.46
0.5511	328.15	749.04
0.5517	298.15	778.51
0.5517	318.15	759.04
0.6007	318.15	768.46
0.6018	298.15	788.45
0.6023	288.15	798.22
0.6038	308.15	778.99
0.6093	328.15	760.27
0.6471	328.15	767.65
0.6480	298.15	797.84
0.6492	318.15	778.12
0.6498	308.15	788.17
0.6584	288.15	809.63
0.6934	318.15	787.02
0.6967	328.15	777.52
0.6976	298.15	808.02
0.6999	288.15	818.26
0.7026	308.15	798.87
0.7390	318.15	796.28
0.7390	328.15	786.07
0.7463	298.15	818.17
0.7486	288.15	828.54
0.7544	308.15	809.6
0.7880	308.15	816.69
0.7884	298.15	827.06
0.7947	318.15	807.72
0.7999	328.15	798.54
0.8042	288.15	840.42
0.8397	328.15	806.83
0.8424	308.15	828.13
0.8473	298.15	839.64
0.8481	288.15	850.01
0.8554	318.15	820.65
0.8861	318.15	827.23
0.9009	308.15	840.82
0.9010	288.15	861.58
0.9054	298.15	852.26
0.9086	328.15	821.54
0.9347	288.15	869.11
0.9512	308.15	851.86
0.9515	318.15	841.48
0.9524	298.15	862.74
0.9527	288.15	873.2
0.9533	328.15	831.27
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	371.38
0.0080	371.40
0.0290	371.62
0.0490	371.75
0.0660	371.85
0.0840	371.99
0.1010	372.12
0.1200	372.27
0.1390	372.42
0.1600	372.61
0.1800	372.80
0.2070	373.05
0.2310	373.30
0.2580	373.60
0.2830	373.88
0.3080	374.17
0.3360	374.55
0.3630	374.96
0.3820	375.23
0.4040	375.54
0.4260	375.90
0.4490	376.24
0.4590	376.42
0.4820	376.79
0.5030	377.18
0.5300	377.70
0.5500	378.10
0.5980	379.04
0.6230	379.62
0.7080	381.90
0.7380	382.86
0.8070	385.01
0.8370	386.16
0.8790	387.93
0.8990	388.85
0.9160	389.66
0.9320	390.45
0.9440	391.15
0.9600	391.90
0.9710	392.52
0.9820	393.20
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	371.38
0.0080	371.40
0.0290	371.62
0.0490	371.75
0.0660	371.85
0.0840	371.99
0.1010	372.12
0.1200	372.27
0.1390	372.42
0.1600	372.61
0.1800	372.80
0.2070	373.05
0.2310	373.30
0.2580	373.60
0.2830	373.88
0.3080	374.17
0.3360	374.55
0.3630	374.96
0.3820	375.23
0.4040	375.54
0.4260	375.90
0.4490	376.24
0.4590	376.42
0.4820	376.79
0.5030	377.18
0.5300	377.70
0.5500	378.10
0.5980	379.04
0.6230	379.62
0.7080	381.90
0.7380	382.86
0.8070	385.01
0.8370	386.16
0.8790	387.93
0.8990	388.85
0.9160	389.66
0.9320	390.45
0.9440	391.15
0.9600	391.90
0.9710	392.52
0.9820	393.20
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