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

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Ethane, 1,2-dichloro-

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

1,4-Dioxane

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

  1. η - Viscosity, Pa*s (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. ρl - Mass density, kg/m3 (4)
  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:

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:

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