Mixture of Ethane, 1,2-dichloro- + 1,4-Dioxane

Datasets

1. η - Viscosity, Pa*s
2. P_vap - Vapor or sublimation pressure, kPa
3. ρ_l - Mass density, kg/m3 (2)
4. c_sound,fluid - Speed of Sound, m/s

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0008
298.15	0.0934	0.0008
298.15	0.1881	0.0008
298.15	0.2843	0.0009
298.15	0.3819	0.0009
298.15	0.4258	0.0009
298.15	0.5816	0.0010
298.15	0.6838	0.0010
298.15	0.7875	0.0011
298.15	0.8929	0.0011
298.15	1.0000	0.0012
308.15	0.0000	0.0007
308.15	0.0934	0.0007
308.15	0.1881	0.0007
308.15	0.2843	0.0007
308.15	0.3819	0.0008
308.15	0.4258	0.0008
308.15	0.5816	0.0008
308.15	0.6838	0.0009
308.15	0.7875	0.0009
308.15	0.8929	0.0009
308.15	1.0000	0.0010
318.15	0.0000	0.0006
318.15	0.0934	0.0006
318.15	0.1881	0.0006
318.15	0.2843	0.0006
318.15	0.3819	0.0006
318.15	0.4258	0.0007
318.15	0.5816	0.0007
318.15	0.6838	0.0007
318.15	0.7875	0.0008
318.15	0.8929	0.0008
318.15	1.0000	0.0009

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dichloro- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
275.23	0.1437	1.41
284.92	0.1437	2.52
294.82	0.1437	4.36
304.81	0.1437	7.25
314.76	0.1437	11.54
324.90	0.1437	18.09
334.92	0.1437	27.58
344.91	0.1437	40.53
354.90	0.1437	57.77
274.94	0.3347	1.63
284.89	0.3347	2.93
294.80	0.3347	5.03
304.76	0.3347	8.33
314.74	0.3347	13.20
324.90	0.3347	20.66
334.89	0.3347	30.76
344.91	0.3347	44.69
354.85	0.3347	63.52
274.94	0.4800	1.87
284.84	0.4800	3.34
294.80	0.4800	5.68
304.76	0.4800	9.27
314.72	0.4800	14.63
324.90	0.4800	22.66
334.89	0.4800	33.73
344.89	0.4800	48.86
354.81	0.4800	68.94
274.89	0.6316	2.20
284.84	0.6316	3.88
294.77	0.6316	6.54
304.76	0.6316	10.58
314.72	0.6316	16.63
324.90	0.6316	25.46
334.85	0.6316	37.39
344.85	0.6316	53.97
354.81	0.6316	75.54
274.94	0.8892	2.77
284.89	0.8892	4.83
294.85	0.8892	8.06
304.74	0.8892	13.01
314.74	0.8892	20.16
324.76	0.8892	30.64
334.76	0.8892	44.86
344.78	0.8892	64.02
354.69	0.8892	89.47

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	1246.37
298.15	0.0934	1221.34
298.15	0.1881	1197.17
298.15	0.2843	1173.99
298.15	0.3819	1151.77
298.15	0.4258	1142.09
298.15	0.5816	1109.56
298.15	0.6838	1089.25
298.15	0.7875	1069.16
298.15	0.8929	1048.86
298.15	1.0000	1027.79
308.15	0.0000	1231.21
308.15	0.0934	1206.17
308.15	0.1881	1182.34
308.15	0.2843	1159.5
308.15	0.3819	1137.63
308.15	0.4258	1128.16
308.15	0.5816	1096.17
308.15	0.6838	1076.38
308.15	0.7875	1056.58
308.15	0.8929	1036.88
308.15	1.0000	1016.78
318.15	0.0000	1214.55
318.15	0.0934	1189.14
318.15	0.1881	1164.97
318.15	0.2843	1141.96
318.15	0.3819	1120.0
318.15	0.4258	1110.67
318.15	0.5816	1079.43
318.15	0.6838	1060.46
318.15	0.7875	1042.21
318.15	0.8929	1024.08
318.15	1.0000	1005.24

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1260.35
288.15	0.0500	1247.73
288.15	0.1500	1223.15
288.15	0.2500	1199.18
288.15	0.3500	1175.98
288.15	0.4500	1153.2
288.15	0.5000	1142.13
288.15	0.5500	1131.22
288.15	0.6500	1109.63
288.15	0.7500	1088.81
288.15	0.8500	1068.59
288.15	0.9500	1048.8
288.15	1.0000	1039.12
298.15	0.0000	1245.75
298.15	0.0500	1233.53
298.15	0.1500	1209.44
298.15	0.2500	1185.91
298.15	0.3500	1163.09
298.15	0.4500	1140.69
298.15	0.5000	1129.79
298.15	0.5500	1119.02
298.15	0.6500	1097.72
298.15	0.7500	1077.13
298.15	0.8500	1057.12
298.15	0.9500	1037.49
298.15	1.0000	1027.84
308.15	0.0000	1231.16
308.15	0.0500	1219.2
308.15	0.1500	1195.6
308.15	0.2500	1172.52
308.15	0.3500	1150.11
308.15	0.4500	1128.08
308.15	0.5000	1117.34
308.15	0.5500	1106.74
308.15	0.6500	1085.72
308.15	0.7500	1065.38
308.15	0.8500	1045.59
308.15	0.9500	1026.13
308.15	1.0000	1016.57
318.15	0.0000	1216.56
318.15	0.0500	1204.74
318.15	0.1500	1181.63
318.15	0.2500	1159.01
318.15	0.3500	1137.01
318.15	0.4500	1115.36
318.15	0.5000	1104.79
318.15	0.5500	1094.34
318.15	0.6500	1073.62
318.15	0.7500	1053.55
318.15	0.8500	1033.98
318.15	0.9500	1014.72
318.15	1.0000	1005.29

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)
• Frequency, MHz = 2 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1193.6
0.0934	1198.9
0.1881	1204.7
0.2843	1211.7
0.3819	1218.7
0.4258	1222.7
0.5816	1240.4
0.6838	1256.1
0.7875	1277.4
0.8929	1306.8
1.0000	1343.4

Sources

• Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
• Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
• Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling

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