Mixture of n-Hexane + Ethane, 1,2-dimethoxy-

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 n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
1.0000	1.0000
0.9218	0.9311
0.8922	0.9060
0.7831	0.8186
0.7505	0.7981
0.6710	0.7474
0.6269	0.7102
0.5813	0.6814
0.5248	0.6350
0.4636	0.5912
0.4423	0.6004
0.3824	0.5563
0.3379	0.5097
0.3060	0.4757
0.2679	0.4296
0.2349	0.3883
0.1981	0.3410
0.1186	0.2193
0.1001	0.1916
0.0697	0.1398
0.0682	0.1375
0.0614	0.1256
0.0573	0.1186
0.0474	0.0995
0.0404	0.0859
0.0315	0.0686
0.0155	0.0345
0.0114	0.0255
0.0096	0.0218
0.0000	0.0000

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
1.0000	1.0000
0.9218	0.9311
0.8922	0.9060
0.7831	0.8186
0.7505	0.7981
0.6710	0.7474
0.6269	0.7102
0.5813	0.6814
0.5248	0.6350
0.4636	0.5912
0.4423	0.6004
0.3824	0.5563
0.3379	0.5097
0.3060	0.4757
0.2679	0.4296
0.2349	0.3883
0.1981	0.3410
0.1186	0.2193
0.1001	0.1916
0.0697	0.1398
0.0682	0.1375
0.0614	0.1256
0.0573	0.1186
0.0474	0.0995
0.0404	0.0859
0.0315	0.0686
0.0155	0.0345
0.0114	0.0255
0.0096	0.0218
0.0000	0.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0501	857.87
288.15	0.1049	842.87
288.15	0.2999	794.19
288.15	0.4059	770.33
288.15	0.4961	751.31
288.15	0.6054	729.6
288.15	0.6940	713.16
288.15	0.7916	696.41
288.15	0.9035	678.43
288.15	0.9533	670.87
298.15	0.0495	846.99
298.15	0.1011	833.13
298.15	0.2009	807.1
298.15	0.3031	782.87
298.15	0.4027	760.92
298.15	0.4977	740.86
298.15	0.5959	721.71
298.15	0.6972	703.06
298.15	0.8051	684.57
298.15	0.8985	670.0
308.15	0.0457	837.34
308.15	0.0927	824.63
308.15	0.2001	797.09
308.15	0.2984	773.76
308.15	0.3939	752.46
308.15	0.5082	728.75
308.15	0.5955	711.88
308.15	0.6927	694.24
308.15	0.8036	675.37
308.15	0.9023	660.16
308.15	0.9509	653.01
288.15	0.0000	872.06
298.15	0.0000	861.17
308.15	0.0000	850.13
288.15	1.0000	664.13
298.15	1.0000	655.14
308.15	1.0000	646.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0501	857.87
288.15	0.1049	842.87
288.15	0.2999	794.19
288.15	0.4059	770.33
288.15	0.4961	751.31
288.15	0.6054	729.6
288.15	0.6940	713.16
288.15	0.7916	696.41
288.15	0.9035	678.43
288.15	0.9533	670.87
298.15	0.0495	846.99
298.15	0.1011	833.13
298.15	0.2009	807.1
298.15	0.3031	782.87
298.15	0.4027	760.92
298.15	0.4977	740.86
298.15	0.5959	721.71
298.15	0.6972	703.06
298.15	0.8051	684.57
298.15	0.8985	670.0
308.15	0.0457	837.34
308.15	0.0927	824.63
308.15	0.2001	797.09
308.15	0.2984	773.76
308.15	0.3939	752.46
308.15	0.5082	728.75
308.15	0.5955	711.88
308.15	0.6927	694.24
308.15	0.8036	675.37
308.15	0.9023	660.16
308.15	0.9509	653.01
288.15	0.0000	872.06
298.15	0.0000	861.17
308.15	0.0000	850.13
288.15	1.0000	664.13
298.15	1.0000	655.14
308.15	1.0000	646.1

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	341.88
0.9218	342.15
0.8922	342.25
0.7831	342.61
0.7505	342.86
0.6710	343.46
0.6269	344.02
0.5813	344.53
0.5248	345.21
0.4636	345.94
0.4423	346.28
0.3824	346.72
0.3379	347.79
0.3060	348.51
0.2679	349.43
0.2349	350.23
0.1981	351.49
0.1186	353.49
0.1001	354.13
0.0697	354.81
0.0682	354.94
0.0614	355.34
0.0573	355.76
0.0474	355.92
0.0404	356.16
0.0315	356.44
0.0155	357.01
0.0114	357.14
0.0096	357.22
0.0000	357.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	341.88
0.9218	342.15
0.8922	342.25
0.7831	342.61
0.7505	342.86
0.6710	343.46
0.6269	344.02
0.5813	344.53
0.5248	345.21
0.4636	345.94
0.4423	346.28
0.3824	346.72
0.3379	347.79
0.3060	348.51
0.2679	349.43
0.2349	350.23
0.1981	351.49
0.1186	353.49
0.1001	354.13
0.0697	354.81
0.0682	354.94
0.0614	355.34
0.0573	355.76
0.0474	355.92
0.0404	356.16
0.0315	356.44
0.0155	357.01
0.0114	357.14
0.0096	357.22
0.0000	357.75

Sources

• Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
• Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa

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