- Name
- Ethane, 1,2-dichloro-
- InChI
- InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2
- InChI Key
- WSLDOOZREJYCGB-UHFFFAOYSA-N
- Formula
- C2H4Cl2
- SMILES
- ClCCCl
- Mol. Weight (g/mol)
- 98.96
- CAS
- 107-06-2
- Name
- 1,4-Dioxane
- InChI
- InChI=1S/C4H8O2/c1-2-6-4-3-5-1/h1-4H2
- InChI Key
- RYHBNJHYFVUHQT-UHFFFAOYSA-N
- Formula
- C4H8O2
- SMILES
- C1COCCO1
- Mol. Weight (g/mol)
- 88.11
- CAS
- 123-91-1
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Datasets
- η - Viscosity, Pa*s (2)
- Pvap - Vapor or sublimation pressure, kPa (2)
- ρl - Mass density, kg/m3 (4)
- csound,fluid - Speed of Sound, m/s (2)
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 |
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 |
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 |
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 |
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