Mixture of Benzene + Tetrachloroethylene
Datasets
-
η - Viscosity, Pa*s (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Tetrachloroethylene (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0006 |
0.0883 |
0.0006 |
0.1788 |
0.0006 |
0.2720 |
0.0006 |
0.3674 |
0.0007 |
0.4655 |
0.0007 |
0.5671 |
0.0007 |
0.6706 |
0.0007 |
0.7770 |
0.0008 |
0.8873 |
0.0008 |
1.0000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Tetrachloroethylene (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0006 |
0.0883 |
0.0006 |
0.1788 |
0.0006 |
0.2720 |
0.0006 |
0.3674 |
0.0007 |
0.4655 |
0.0007 |
0.5671 |
0.0007 |
0.6706 |
0.0007 |
0.7770 |
0.0008 |
0.8873 |
0.0008 |
1.0000 |
0.0008 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrachloroethylene (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
283.15 |
0.0798 |
5.76 |
283.15 |
0.1262 |
5.54 |
283.15 |
0.2205 |
5.14 |
283.15 |
0.3153 |
4.72 |
283.15 |
0.3909 |
4.39 |
283.15 |
0.4419 |
4.16 |
283.15 |
0.4981 |
3.91 |
283.15 |
0.6046 |
3.41 |
283.15 |
0.6779 |
3.03 |
283.15 |
0.7759 |
2.48 |
283.15 |
0.8844 |
1.80 |
288.15 |
0.0798 |
7.42 |
288.15 |
0.1262 |
7.14 |
288.15 |
0.2206 |
6.63 |
288.15 |
0.3154 |
6.10 |
288.15 |
0.3909 |
5.68 |
288.15 |
0.4420 |
5.41 |
288.15 |
0.4982 |
5.06 |
288.15 |
0.6047 |
4.42 |
288.15 |
0.6780 |
3.92 |
288.15 |
0.7760 |
3.23 |
288.15 |
0.8844 |
2.40 |
293.15 |
0.0799 |
9.45 |
293.15 |
0.1262 |
9.12 |
293.15 |
0.2207 |
8.48 |
293.15 |
0.3154 |
7.81 |
293.15 |
0.3911 |
7.27 |
293.15 |
0.4422 |
6.91 |
293.15 |
0.4984 |
6.49 |
293.15 |
0.6047 |
5.64 |
293.15 |
0.6780 |
5.04 |
293.15 |
0.7761 |
4.16 |
293.15 |
0.8845 |
3.12 |
298.15 |
0.0799 |
11.98 |
298.15 |
0.1262 |
11.59 |
298.15 |
0.2207 |
10.75 |
298.15 |
0.3155 |
9.89 |
298.15 |
0.3912 |
9.22 |
298.15 |
0.4426 |
8.75 |
298.15 |
0.4986 |
8.22 |
298.15 |
0.6049 |
7.20 |
298.15 |
0.6781 |
6.44 |
298.15 |
0.7762 |
5.31 |
298.15 |
0.8845 |
4.00 |
303.15 |
0.0799 |
15.07 |
303.15 |
0.1262 |
14.55 |
303.15 |
0.2206 |
13.52 |
303.15 |
0.3154 |
12.47 |
303.15 |
0.3915 |
11.60 |
303.15 |
0.4431 |
11.00 |
303.15 |
0.4989 |
10.34 |
303.15 |
0.6050 |
9.04 |
303.15 |
0.6782 |
8.11 |
303.15 |
0.7765 |
6.73 |
303.15 |
0.8846 |
5.12 |
308.15 |
0.0799 |
18.72 |
308.15 |
0.1262 |
18.10 |
308.15 |
0.2207 |
16.82 |
308.15 |
0.3155 |
15.51 |
308.15 |
0.3912 |
14.47 |
308.15 |
0.4426 |
13.75 |
308.15 |
0.4994 |
12.87 |
308.15 |
0.6052 |
11.29 |
308.15 |
0.6784 |
10.13 |
308.15 |
0.7767 |
8.46 |
308.15 |
0.8848 |
6.47 |
313.15 |
0.0799 |
23.06 |
313.15 |
0.1262 |
22.31 |
313.15 |
0.2208 |
20.75 |
313.15 |
0.3155 |
19.14 |
313.15 |
0.3914 |
17.89 |
313.15 |
0.4431 |
16.96 |
313.15 |
0.4988 |
15.97 |
313.15 |
0.6050 |
13.98 |
313.15 |
0.6786 |
12.54 |
313.15 |
0.7771 |
10.48 |
313.15 |
0.8849 |
8.10 |
318.15 |
0.0799 |
28.22 |
318.15 |
0.1263 |
27.27 |
318.15 |
0.2208 |
25.36 |
318.15 |
0.3157 |
23.42 |
318.15 |
0.3916 |
21.84 |
318.15 |
0.4432 |
20.76 |
318.15 |
0.4990 |
19.59 |
318.15 |
0.6051 |
17.16 |
318.15 |
0.6783 |
15.47 |
318.15 |
0.7776 |
12.91 |
318.15 |
0.8851 |
10.04 |
323.15 |
0.0800 |
34.23 |
323.15 |
0.1264 |
33.07 |
323.15 |
0.2210 |
30.84 |
323.15 |
0.3157 |
28.57 |
323.15 |
0.3917 |
26.65 |
323.15 |
0.4438 |
25.20 |
323.15 |
0.4994 |
23.84 |
323.15 |
0.6052 |
20.90 |
323.15 |
0.6784 |
18.86 |
323.15 |
0.7769 |
15.88 |
323.15 |
0.8855 |
12.30 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrachloroethylene (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
283.15 |
0.0798 |
5.76 |
283.15 |
0.1262 |
5.54 |
283.15 |
0.2205 |
5.14 |
283.15 |
0.3153 |
4.72 |
283.15 |
0.3909 |
4.39 |
283.15 |
0.4419 |
4.16 |
283.15 |
0.4981 |
3.91 |
283.15 |
0.6046 |
3.41 |
283.15 |
0.6779 |
3.03 |
283.15 |
0.7759 |
2.48 |
283.15 |
0.8844 |
1.80 |
288.15 |
0.0798 |
7.42 |
288.15 |
0.1262 |
7.14 |
288.15 |
0.2206 |
6.63 |
288.15 |
0.3154 |
6.10 |
288.15 |
0.3909 |
5.68 |
288.15 |
0.4420 |
5.41 |
288.15 |
0.4982 |
5.06 |
288.15 |
0.6047 |
4.42 |
288.15 |
0.6780 |
3.92 |
288.15 |
0.7760 |
3.23 |
288.15 |
0.8844 |
2.40 |
293.15 |
0.0799 |
9.45 |
293.15 |
0.1262 |
9.12 |
293.15 |
0.2207 |
8.48 |
293.15 |
0.3154 |
7.81 |
293.15 |
0.3911 |
7.27 |
293.15 |
0.4422 |
6.91 |
293.15 |
0.4984 |
6.49 |
293.15 |
0.6047 |
5.64 |
293.15 |
0.6780 |
5.04 |
293.15 |
0.7761 |
4.16 |
293.15 |
0.8845 |
3.12 |
298.15 |
0.0799 |
11.98 |
298.15 |
0.1262 |
11.59 |
298.15 |
0.2207 |
10.75 |
298.15 |
0.3155 |
9.89 |
298.15 |
0.3912 |
9.22 |
298.15 |
0.4426 |
8.75 |
298.15 |
0.4986 |
8.22 |
298.15 |
0.6049 |
7.20 |
298.15 |
0.6781 |
6.44 |
298.15 |
0.7762 |
5.31 |
298.15 |
0.8845 |
4.00 |
303.15 |
0.0799 |
15.07 |
303.15 |
0.1262 |
14.55 |
303.15 |
0.2206 |
13.52 |
303.15 |
0.3154 |
12.47 |
303.15 |
0.3915 |
11.60 |
303.15 |
0.4431 |
11.00 |
303.15 |
0.4989 |
10.34 |
303.15 |
0.6050 |
9.04 |
303.15 |
0.6782 |
8.11 |
303.15 |
0.7765 |
6.73 |
303.15 |
0.8846 |
5.12 |
308.15 |
0.0799 |
18.72 |
308.15 |
0.1262 |
18.10 |
308.15 |
0.2207 |
16.82 |
308.15 |
0.3155 |
15.51 |
308.15 |
0.3912 |
14.47 |
308.15 |
0.4426 |
13.75 |
308.15 |
0.4994 |
12.87 |
308.15 |
0.6052 |
11.29 |
308.15 |
0.6784 |
10.13 |
308.15 |
0.7767 |
8.46 |
308.15 |
0.8848 |
6.47 |
313.15 |
0.0799 |
23.06 |
313.15 |
0.1262 |
22.31 |
313.15 |
0.2208 |
20.75 |
313.15 |
0.3155 |
19.14 |
313.15 |
0.3914 |
17.89 |
313.15 |
0.4431 |
16.96 |
313.15 |
0.4988 |
15.97 |
313.15 |
0.6050 |
13.98 |
313.15 |
0.6786 |
12.54 |
313.15 |
0.7771 |
10.48 |
313.15 |
0.8849 |
8.10 |
318.15 |
0.0799 |
28.22 |
318.15 |
0.1263 |
27.27 |
318.15 |
0.2208 |
25.36 |
318.15 |
0.3157 |
23.42 |
318.15 |
0.3916 |
21.84 |
318.15 |
0.4432 |
20.76 |
318.15 |
0.4990 |
19.59 |
318.15 |
0.6051 |
17.16 |
318.15 |
0.6783 |
15.47 |
318.15 |
0.7776 |
12.91 |
318.15 |
0.8851 |
10.04 |
323.15 |
0.0800 |
34.23 |
323.15 |
0.1264 |
33.07 |
323.15 |
0.2210 |
30.84 |
323.15 |
0.3157 |
28.57 |
323.15 |
0.3917 |
26.65 |
323.15 |
0.4438 |
25.20 |
323.15 |
0.4994 |
23.84 |
323.15 |
0.6052 |
20.90 |
323.15 |
0.6784 |
18.86 |
323.15 |
0.7769 |
15.88 |
323.15 |
0.8855 |
12.30 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Tetrachloroethylene (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
869.7 |
0.0883 |
939.8 |
0.1788 |
1011.5 |
0.2720 |
1084.6 |
0.3674 |
1156.7 |
0.4655 |
1228.8 |
0.5671 |
1302.3 |
0.6706 |
1377.4 |
0.7770 |
1453.2 |
0.8873 |
1531.7 |
1.0000 |
1610.2 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Tetrachloroethylene (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
869.7 |
0.0883 |
939.8 |
0.1788 |
1011.5 |
0.2720 |
1084.6 |
0.3674 |
1156.7 |
0.4655 |
1228.8 |
0.5671 |
1302.3 |
0.6706 |
1377.4 |
0.7770 |
1453.2 |
0.8873 |
1531.7 |
1.0000 |
1610.2 |
Sources