Mixture of p-Xylene + Ethane, 1,2-dimethoxy-

Datasets

1. ρ_l - Mass density, kg/m3
2. γ - Surface tension liquid-gas, N/m
3. Excess molar volume, m3/mol

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	856.95
298.15	0.1002	857.45
298.15	0.2004	857.95
298.15	0.2996	858.44
298.15	0.4001	858.93
298.15	0.5009	859.41
298.15	0.5997	859.85
298.15	0.7018	860.28
298.15	0.8005	860.66
298.15	0.8998	861.02
298.15	1.0000	861.36
303.15	0.0000	852.61
303.15	0.0999	853.1
303.15	0.2007	853.58
303.15	0.3002	854.06
303.15	0.3999	854.52
303.15	0.4999	854.97
303.15	0.6001	855.4
303.15	0.7011	855.81
303.15	0.8003	856.19
303.15	0.9003	856.52
303.15	1.0000	856.79
308.15	0.0000	848.27
308.15	0.0996	848.66
308.15	0.1998	849.05
308.15	0.2997	849.41
308.15	0.4001	849.76
308.15	0.4995	850.09
308.15	0.6004	850.4
308.15	0.6993	850.67
308.15	0.7993	850.93
308.15	0.8998	851.14
308.15	1.0000	851.24

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0281
298.15	0.1002	0.0276
298.15	0.2004	0.0272
298.15	0.2996	0.0267
298.15	0.4001	0.0263
298.15	0.5009	0.0259
298.15	0.5997	0.0255
298.15	0.7018	0.0252
298.15	0.8005	0.0249
298.15	0.8998	0.0246
298.15	1.0000	0.0243
303.15	0.0000	0.0276
303.15	0.0999	0.0271
303.15	0.2007	0.0267
303.15	0.3002	0.0262
303.15	0.3999	0.0258
303.15	0.4999	0.0254
303.15	0.6001	0.0250
303.15	0.7011	0.0247
303.15	0.8003	0.0244
303.15	0.9003	0.0240
303.15	1.0000	0.0237
308.15	0.0000	0.0271
308.15	0.0996	0.0266
308.15	0.1998	0.0262
308.15	0.2997	0.0257
308.15	0.4001	0.0253
308.15	0.4995	0.0249
308.15	0.6004	0.0245
308.15	0.6993	0.0242
308.15	0.7993	0.0238
308.15	0.8998	0.0235
308.15	1.0000	0.0232

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid	Excess molar volume, m3/mol - Liquid
298.15	0.0000	0.0000
298.15	0.1002	-1.7200e-08
298.15	0.2004	-3.2100e-08
298.15	0.2996	-4.4000e-08
298.15	0.4001	-5.2900e-08
298.15	0.5009	-5.7900e-08
298.15	0.5997	-5.7100e-08
298.15	0.7018	-5.0600e-08
298.15	0.8005	-3.8400e-08
298.15	0.8998	-2.1500e-08
298.15	1.0000	0.0000
303.15	0.0000	0.0000
303.15	0.0999	-1.8500e-08
303.15	0.2007	-3.3900e-08
303.15	0.3002	-4.6900e-08
303.15	0.3999	-5.4800e-08
303.15	0.4999	-6.0400e-08
303.15	0.6001	-6.0000e-08
303.15	0.7011	-5.4500e-08
303.15	0.8003	-4.4400e-08
303.15	0.9003	-2.7200e-08
303.15	1.0000	0.0000
308.15	0.0000	0.0000
308.15	0.0996	-1.9700e-08
308.15	0.1998	-3.7400e-08
308.15	0.2997	-4.9300e-08
308.15	0.4001	-5.7900e-08
308.15	0.4995	-6.2600e-08
308.15	0.6004	-6.2500e-08
308.15	0.6993	-5.6600e-08
308.15	0.7993	-4.7700e-08
308.15	0.8998	-3.1100e-08
308.15	1.0000	0.0000

Sources

• Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K

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