Mixture of Butanoic acid, methyl 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, methyl ester (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (1) - Liquid	Mole fraction of Butanoic acid, methyl ester (1) - Gas
0.0000	0.0000
0.0420	0.1630
0.0650	0.2400
0.0810	0.2950
0.1410	0.4410
0.1660	0.4870
0.1870	0.5320
0.2270	0.5950
0.2720	0.6470
0.2980	0.6720
0.3240	0.6940
0.3440	0.7150
0.3880	0.7420
0.4320	0.7700
0.4690	0.7880
0.5060	0.8050
0.5360	0.8210
0.5690	0.8340
0.6060	0.8490
0.6400	0.8620
0.6730	0.8740
0.7110	0.8870
0.7440	0.8990
0.7750	0.9090
0.8060	0.9220
0.8330	0.9320
0.8590	0.9410
0.8810	0.9480
0.8970	0.9550
0.9160	0.9630
0.9360	0.9710
0.9540	0.9780
0.9660	0.9840
0.9690	0.9860
1.0000	1.0000

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

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (1) - Liquid	Mole fraction of Butanoic acid, methyl ester (1) - Gas
0.0000	0.0000
0.0420	0.1630
0.0650	0.2400
0.0810	0.2950
0.1410	0.4410
0.1660	0.4870
0.1870	0.5320
0.2270	0.5950
0.2720	0.6470
0.2980	0.6720
0.3240	0.6940
0.3440	0.7150
0.3880	0.7420
0.4320	0.7700
0.4690	0.7880
0.5060	0.8050
0.5360	0.8210
0.5690	0.8340
0.6060	0.8490
0.6400	0.8620
0.6730	0.8740
0.7110	0.8870
0.7440	0.8990
0.7750	0.9090
0.8060	0.9220
0.8330	0.9320
0.8590	0.9410
0.8810	0.9480
0.8970	0.9550
0.9160	0.9630
0.9360	0.9710
0.9540	0.9780
0.9660	0.9840
0.9690	0.9860
1.0000	1.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Butanoic acid, methyl 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
0.0234	318.15	700.32
0.0272	328.15	692.57
0.0495	298.15	718.76
0.0544	288.15	727.14
0.0554	308.15	711.45
0.0562	328.15	695.34
0.0731	318.15	705.17
0.0780	328.15	697.49
0.0804	288.15	729.99
0.0998	298.15	724.04
0.1002	308.15	716.1
0.1033	318.15	708.28
0.1041	328.15	700.12
0.1502	328.15	704.97
0.1552	318.15	713.83
0.1647	288.15	739.66
0.1653	308.15	723.29
0.1729	298.15	732.49
0.1935	298.15	734.88
0.1993	318.15	718.91
0.2023	328.15	710.73
0.2108	308.15	728.63
0.2172	288.15	746.06
0.2378	288.15	748.63
0.2473	298.15	741.54
0.2545	308.15	734.04
0.2571	318.15	725.77
0.2654	328.15	718.16
0.2963	288.15	756.43
0.3035	298.15	748.92
0.3073	328.15	723.36
0.3082	308.15	740.93
0.3123	318.15	732.79
0.3419	288.15	762.85
0.3558	298.15	756.23
0.3568	318.15	738.79
0.3598	308.15	748.08
0.3624	328.15	730.61
0.3986	288.15	771.19
0.4090	308.15	755.11
0.4120	328.15	737.45
0.4135	318.15	746.74
0.4425	288.15	778.04
0.4462	298.15	769.69
0.4555	318.15	753.07
0.4567	328.15	744.0
0.4594	308.15	762.76
0.4993	308.15	769.14
0.5007	288.15	787.63
0.5083	328.15	751.95
0.5093	318.15	761.51
0.5488	288.15	796.09
0.5497	298.15	786.99
0.5504	308.15	777.76
0.5549	328.15	759.51
0.5565	318.15	769.3
0.6001	308.15	786.6
0.6040	288.15	806.21
0.6043	318.15	777.7
0.6157	328.15	770.1
0.6465	298.15	805.02
0.6482	308.15	795.68
0.6544	318.15	787.04
0.6553	288.15	816.39
0.6554	328.15	777.42
0.6945	308.15	804.91
0.6959	288.15	824.67
0.7027	328.15	786.49
0.7067	318.15	797.4
0.7463	308.15	815.78
0.7490	328.15	795.99
0.7507	288.15	836.81
0.7509	298.15	826.86
0.7541	318.15	807.31
0.7772	298.15	832.78
0.7964	308.15	827.07
0.8037	318.15	818.4
0.8038	298.15	839.14
0.8114	288.15	850.96
0.8451	308.15	838.68
0.8511	328.15	819.04
0.8553	288.15	862.13
0.8594	318.15	831.69
0.8948	308.15	851.33
0.8988	288.15	873.46
0.9051	328.15	832.64
0.9052	298.15	864.6
0.9068	318.15	843.76
0.9497	308.15	866.34
0.9506	328.15	844.76
0.9507	288.15	888.13
0.9511	318.15	855.91
0.9530	298.15	878.19
1.0000	288.15	903.31
1.0000	298.15	892.31
1.0000	308.15	881.19
1.0000	318.15	870.06
1.0000	328.15	858.8

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Butanoic acid, methyl 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
0.0234	318.15	700.32
0.0272	328.15	692.57
0.0495	298.15	718.76
0.0544	288.15	727.14
0.0554	308.15	711.45
0.0562	328.15	695.34
0.0731	318.15	705.17
0.0780	328.15	697.49
0.0804	288.15	729.99
0.0998	298.15	724.04
0.1002	308.15	716.1
0.1033	318.15	708.28
0.1041	328.15	700.12
0.1502	328.15	704.97
0.1552	318.15	713.83
0.1647	288.15	739.66
0.1653	308.15	723.29
0.1729	298.15	732.49
0.1935	298.15	734.88
0.1993	318.15	718.91
0.2023	328.15	710.73
0.2108	308.15	728.63
0.2172	288.15	746.06
0.2378	288.15	748.63
0.2473	298.15	741.54
0.2545	308.15	734.04
0.2571	318.15	725.77
0.2654	328.15	718.16
0.2963	288.15	756.43
0.3035	298.15	748.92
0.3073	328.15	723.36
0.3082	308.15	740.93
0.3123	318.15	732.79
0.3419	288.15	762.85
0.3558	298.15	756.23
0.3568	318.15	738.79
0.3598	308.15	748.08
0.3624	328.15	730.61
0.3986	288.15	771.19
0.4090	308.15	755.11
0.4120	328.15	737.45
0.4135	318.15	746.74
0.4425	288.15	778.04
0.4462	298.15	769.69
0.4555	318.15	753.07
0.4567	328.15	744.0
0.4594	308.15	762.76
0.4993	308.15	769.14
0.5007	288.15	787.63
0.5083	328.15	751.95
0.5093	318.15	761.51
0.5488	288.15	796.09
0.5497	298.15	786.99
0.5504	308.15	777.76
0.5549	328.15	759.51
0.5565	318.15	769.3
0.6001	308.15	786.6
0.6040	288.15	806.21
0.6043	318.15	777.7
0.6157	328.15	770.1
0.6465	298.15	805.02
0.6482	308.15	795.68
0.6544	318.15	787.04
0.6553	288.15	816.39
0.6554	328.15	777.42
0.6945	308.15	804.91
0.6959	288.15	824.67
0.7027	328.15	786.49
0.7067	318.15	797.4
0.7463	308.15	815.78
0.7490	328.15	795.99
0.7507	288.15	836.81
0.7509	298.15	826.86
0.7541	318.15	807.31
0.7772	298.15	832.78
0.7964	308.15	827.07
0.8037	318.15	818.4
0.8038	298.15	839.14
0.8114	288.15	850.96
0.8451	308.15	838.68
0.8511	328.15	819.04
0.8553	288.15	862.13
0.8594	318.15	831.69
0.8948	308.15	851.33
0.8988	288.15	873.46
0.9051	328.15	832.64
0.9052	298.15	864.6
0.9068	318.15	843.76
0.9497	308.15	866.34
0.9506	328.15	844.76
0.9507	288.15	888.13
0.9511	318.15	855.91
0.9530	298.15	878.19
1.0000	288.15	903.31
1.0000	298.15	892.31
1.0000	308.15	881.19
1.0000	318.15	870.06
1.0000	328.15	858.8

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	423.90
0.0420	418.67
0.0650	415.89
0.0810	413.88
0.1410	407.75
0.1660	405.58
0.1870	403.43
0.2270	400.20
0.2720	397.25
0.2980	395.74
0.3240	394.41
0.3440	393.01
0.3880	391.37
0.4320	389.52
0.4690	388.15
0.5060	386.99
0.5360	385.96
0.5690	385.02
0.6060	384.04
0.6400	383.16
0.6730	382.34
0.7110	381.48
0.7440	380.71
0.7750	380.09
0.8060	379.39
0.8330	378.82
0.8590	378.37
0.8810	377.95
0.8970	377.62
0.9160	377.25
0.9360	376.91
0.9540	376.58
0.9660	376.36
0.9690	376.30
1.0000	375.74

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	423.90
0.0420	418.67
0.0650	415.89
0.0810	413.88
0.1410	407.75
0.1660	405.58
0.1870	403.43
0.2270	400.20
0.2720	397.25
0.2980	395.74
0.3240	394.41
0.3440	393.01
0.3880	391.37
0.4320	389.52
0.4690	388.15
0.5060	386.99
0.5360	385.96
0.5690	385.02
0.6060	384.04
0.6400	383.16
0.6730	382.34
0.7110	381.48
0.7440	380.71
0.7750	380.09
0.8060	379.39
0.8330	378.82
0.8590	378.37
0.8810	377.95
0.8970	377.62
0.9160	377.25
0.9360	376.91
0.9540	376.58
0.9660	376.36
0.9690	376.30
1.0000	375.74

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