Mixture of Ethane, 1,2-dimethoxy- + Nonane

Datasets

1. ε_r - Relative permittivity at zero frequency (2)
2. ρ_l - Mass density, kg/m3 (2)

Relative permittivity at zero frequency [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Nonane (2) - Liquid	Temperature, K - Liquid	Relative permittivity at zero frequency - Liquid
0.0506	288.15	6.732
0.0507	298.15	6.433
0.0509	318.15	5.899
0.0510	308.15	6.157
0.0527	338.15	5.421
0.0542	328.15	5.626
0.1026	288.15	6.133
0.1028	338.15	5.0
0.1036	308.15	5.62
0.1036	328.15	5.188
0.1043	298.15	5.853
0.1044	318.15	5.387
0.2023	308.15	4.791
0.2031	298.15	4.968
0.2038	318.15	4.607
0.2039	338.15	4.295
0.2041	328.15	4.44
0.2058	288.15	5.147
0.2997	338.15	3.766
0.3029	288.15	4.417
0.3038	308.15	4.118
0.3045	298.15	4.254
0.3051	318.15	3.98
0.3072	328.15	3.845
0.3947	288.15	3.865
0.4037	338.15	3.31
0.4039	308.15	3.59
0.4040	298.15	3.697
0.4052	328.15	3.391
0.4097	318.15	3.463
0.4995	288.15	3.351
0.5013	318.15	3.101
0.5021	308.15	3.173
0.5031	298.15	3.249
0.5036	338.15	2.954
0.5039	328.15	3.019
0.6002	338.15	2.672
0.6014	298.15	2.885
0.6037	318.15	2.767
0.6043	328.15	2.71
0.6048	288.15	2.94
0.6070	308.15	2.812
0.7019	328.15	2.462
0.7020	288.15	2.633
0.7022	318.15	2.503
0.7023	338.15	2.426
0.7039	298.15	2.582
0.7042	308.15	2.538
0.8038	288.15	2.369
0.8041	318.15	2.279
0.8042	338.15	2.224
0.8044	298.15	2.336
0.8050	328.15	2.249
0.8090	308.15	2.298
0.9000	298.15	2.145
0.9032	338.15	2.06
0.9033	308.15	2.119
0.9036	288.15	2.158
0.9040	318.15	2.098
0.9041	328.15	2.079
0.9508	288.15	2.074
0.9510	338.15	1.991
0.9511	298.15	2.057
0.9511	328.15	2.003
0.9515	318.15	2.023
0.9595	308.15	2.027

Relative permittivity at zero frequency [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Nonane (2) - Liquid	Temperature, K - Liquid	Relative permittivity at zero frequency - Liquid
0.0506	288.15	6.732
0.0507	298.15	6.433
0.0509	318.15	5.899
0.0510	308.15	6.157
0.0527	338.15	5.421
0.0542	328.15	5.626
0.1026	288.15	6.133
0.1028	338.15	5.0
0.1036	308.15	5.62
0.1036	328.15	5.188
0.1043	298.15	5.853
0.1044	318.15	5.387
0.2023	308.15	4.791
0.2031	298.15	4.968
0.2038	318.15	4.607
0.2039	338.15	4.295
0.2041	328.15	4.44
0.2058	288.15	5.147
0.2997	338.15	3.766
0.3029	288.15	4.417
0.3038	308.15	4.118
0.3045	298.15	4.254
0.3051	318.15	3.98
0.3072	328.15	3.845
0.3947	288.15	3.865
0.4037	338.15	3.31
0.4039	308.15	3.59
0.4040	298.15	3.697
0.4052	328.15	3.391
0.4097	318.15	3.463
0.4995	288.15	3.351
0.5013	318.15	3.101
0.5021	308.15	3.173
0.5031	298.15	3.249
0.5036	338.15	2.954
0.5039	328.15	3.019
0.6002	338.15	2.672
0.6014	298.15	2.885
0.6037	318.15	2.767
0.6043	328.15	2.71
0.6048	288.15	2.94
0.6070	308.15	2.812
0.7019	328.15	2.462
0.7020	288.15	2.633
0.7022	318.15	2.503
0.7023	338.15	2.426
0.7039	298.15	2.582
0.7042	308.15	2.538
0.8038	288.15	2.369
0.8041	318.15	2.279
0.8042	338.15	2.224
0.8044	298.15	2.336
0.8050	328.15	2.249
0.8090	308.15	2.298
0.9000	298.15	2.145
0.9032	338.15	2.06
0.9033	308.15	2.119
0.9036	288.15	2.158
0.9040	318.15	2.098
0.9041	328.15	2.079
0.9508	288.15	2.074
0.9510	338.15	1.991
0.9511	298.15	2.057
0.9511	328.15	2.003
0.9515	318.15	2.023
0.9595	308.15	2.027

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Nonane (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0505	288.15	857.26
0.0505	298.15	846.61
0.0505	308.15	835.84
0.0507	318.15	824.84
0.0507	328.15	813.72
0.0507	338.15	802.32
0.1008	318.15	812.22
0.1008	328.15	801.43
0.1008	338.15	790.18
0.1014	288.15	843.78
0.1014	298.15	833.36
0.1014	308.15	822.81
0.2017	288.15	820.73
0.2017	298.15	810.7
0.2017	308.15	800.56
0.2062	318.15	789.34
0.2062	328.15	778.96
0.2062	338.15	768.28
0.2962	318.15	772.92
0.2962	328.15	762.85
0.2962	338.15	752.61
0.3027	288.15	801.14
0.3027	298.15	791.51
0.3027	308.15	781.72
0.4033	318.15	756.06
0.4033	328.15	746.4
0.4033	338.15	736.58
0.4071	288.15	783.82
0.4071	298.15	774.52
0.4071	308.15	765.13
0.5043	288.15	769.97
0.5043	298.15	760.99
0.5043	308.15	751.89
0.5051	318.15	742.56
0.5051	328.15	733.25
0.5051	338.15	723.8
0.6014	288.15	757.85
0.6014	298.15	749.16
0.6014	308.15	740.38
0.6024	318.15	731.39
0.6024	328.15	722.33
0.6024	338.15	713.21
0.7041	318.15	721.07
0.7041	328.15	712.38
0.7041	338.15	703.57
0.7048	288.15	746.6
0.7048	298.15	738.23
0.7048	308.15	729.68
0.8042	318.15	712.36
0.8042	328.15	703.93
0.8042	338.15	695.4
0.8051	288.15	737.05
0.8051	298.15	728.9
0.8051	308.15	720.64
0.9039	318.15	704.77
0.9039	328.15	696.59
0.9039	338.15	688.32
0.9043	288.15	728.79
0.9043	298.15	720.86
0.9043	308.15	712.83
0.9520	318.15	701.43
0.9520	328.15	693.36
0.9520	338.15	685.2
0.9528	288.15	725.12
0.9528	298.15	717.29
0.9528	308.15	709.43

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Nonane (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0505	288.15	857.26
0.0505	298.15	846.61
0.0505	308.15	835.84
0.0507	318.15	824.84
0.0507	328.15	813.72
0.0507	338.15	802.32
0.1008	318.15	812.22
0.1008	328.15	801.43
0.1008	338.15	790.18
0.1014	288.15	843.78
0.1014	298.15	833.36
0.1014	308.15	822.81
0.2017	288.15	820.73
0.2017	298.15	810.7
0.2017	308.15	800.56
0.2062	318.15	789.34
0.2062	328.15	778.96
0.2062	338.15	768.28
0.2962	318.15	772.92
0.2962	328.15	762.85
0.2962	338.15	752.61
0.3027	288.15	801.14
0.3027	298.15	791.51
0.3027	308.15	781.72
0.4033	318.15	756.06
0.4033	328.15	746.4
0.4033	338.15	736.58
0.4071	288.15	783.82
0.4071	298.15	774.52
0.4071	308.15	765.13
0.5043	288.15	769.97
0.5043	298.15	760.99
0.5043	308.15	751.89
0.5051	318.15	742.56
0.5051	328.15	733.25
0.5051	338.15	723.8
0.6014	288.15	757.85
0.6014	298.15	749.16
0.6014	308.15	740.38
0.6024	318.15	731.39
0.6024	328.15	722.33
0.6024	338.15	713.21
0.7041	318.15	721.07
0.7041	328.15	712.38
0.7041	338.15	703.57
0.7048	288.15	746.6
0.7048	298.15	738.23
0.7048	308.15	729.68
0.8042	318.15	712.36
0.8042	328.15	703.93
0.8042	338.15	695.4
0.8051	288.15	737.05
0.8051	298.15	728.9
0.8051	308.15	720.64
0.9039	318.15	704.77
0.9039	328.15	696.59
0.9039	338.15	688.32
0.9043	288.15	728.79
0.9043	298.15	720.86
0.9043	308.15	712.83
0.9520	318.15	701.43
0.9520	328.15	693.36
0.9520	338.15	685.2
0.9528	288.15	725.12
0.9528	298.15	717.29
0.9528	308.15	709.43

Sources

• Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures

Note: These property values are available through the Cheméo API. A free account gives you an access key.