Mixture of Tetrachloroethylene + Carbon Tetrachloride
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 (1) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0009 |
0.0946 |
0.0009 |
0.1904 |
0.0009 |
0.2873 |
0.0009 |
0.3853 |
0.0009 |
0.4845 |
0.0009 |
0.5859 |
0.0008 |
0.6876 |
0.0008 |
0.7904 |
0.0008 |
0.8946 |
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 (1) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0009 |
0.0946 |
0.0009 |
0.1904 |
0.0009 |
0.2873 |
0.0009 |
0.3853 |
0.0009 |
0.4845 |
0.0009 |
0.5859 |
0.0008 |
0.6876 |
0.0008 |
0.7904 |
0.0008 |
0.8946 |
0.0008 |
1.0000 |
0.0008 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrachloroethylene (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
283.15 |
0.0862 |
6.94 |
283.15 |
0.1638 |
6.45 |
283.15 |
0.2756 |
5.75 |
283.15 |
0.3520 |
5.25 |
283.15 |
0.4245 |
4.79 |
283.15 |
0.4890 |
4.36 |
283.15 |
0.5816 |
3.77 |
283.15 |
0.6494 |
3.32 |
283.15 |
0.7200 |
2.86 |
283.15 |
0.7935 |
2.38 |
283.15 |
0.8323 |
2.12 |
283.15 |
0.9226 |
1.53 |
288.15 |
0.0863 |
8.90 |
288.15 |
0.1639 |
8.27 |
288.15 |
0.2757 |
7.36 |
288.15 |
0.3521 |
6.74 |
288.15 |
0.4247 |
6.15 |
288.15 |
0.4890 |
5.62 |
288.15 |
0.5817 |
4.85 |
288.15 |
0.6495 |
4.29 |
288.15 |
0.7201 |
3.71 |
288.15 |
0.7935 |
3.09 |
288.15 |
0.8323 |
2.78 |
288.15 |
0.9227 |
2.04 |
293.15 |
0.0863 |
11.25 |
293.15 |
0.1640 |
10.46 |
293.15 |
0.2758 |
9.33 |
293.15 |
0.3523 |
8.55 |
293.15 |
0.4249 |
7.82 |
293.15 |
0.4891 |
7.13 |
293.15 |
0.5818 |
6.17 |
293.15 |
0.6496 |
5.49 |
293.15 |
0.7202 |
4.74 |
293.15 |
0.7936 |
3.98 |
293.15 |
0.8324 |
3.60 |
293.15 |
0.9227 |
2.66 |
298.15 |
0.0864 |
14.11 |
298.15 |
0.1641 |
13.14 |
298.15 |
0.2759 |
11.72 |
298.15 |
0.3525 |
10.74 |
298.15 |
0.4251 |
9.81 |
298.15 |
0.4892 |
8.99 |
298.15 |
0.5819 |
7.80 |
298.15 |
0.6497 |
6.94 |
298.15 |
0.7202 |
6.03 |
298.15 |
0.7937 |
5.08 |
298.15 |
0.8325 |
4.62 |
298.15 |
0.9227 |
3.43 |
303.15 |
0.0863 |
17.62 |
303.15 |
0.1639 |
16.42 |
303.15 |
0.2761 |
14.64 |
303.15 |
0.3527 |
13.43 |
303.15 |
0.4255 |
12.28 |
303.15 |
0.4894 |
11.26 |
303.15 |
0.5820 |
9.82 |
303.15 |
0.6499 |
8.72 |
303.15 |
0.7204 |
7.60 |
303.15 |
0.7939 |
6.44 |
303.15 |
0.8326 |
5.84 |
303.15 |
0.9228 |
4.43 |
308.15 |
0.0863 |
21.71 |
308.15 |
0.1640 |
20.22 |
308.15 |
0.2758 |
18.08 |
308.15 |
0.3524 |
16.61 |
308.15 |
0.4251 |
15.22 |
308.15 |
0.4896 |
13.94 |
308.15 |
0.5822 |
12.16 |
308.15 |
0.6501 |
10.84 |
308.15 |
0.7205 |
9.48 |
308.15 |
0.7941 |
8.05 |
308.15 |
0.8327 |
7.32 |
308.15 |
0.9228 |
5.60 |
313.15 |
0.0864 |
26.52 |
313.15 |
0.1641 |
24.72 |
313.15 |
0.2760 |
22.12 |
313.15 |
0.3527 |
20.32 |
313.15 |
0.4254 |
18.65 |
313.15 |
0.4893 |
17.16 |
313.15 |
0.5825 |
14.98 |
313.15 |
0.6504 |
13.38 |
313.15 |
0.7207 |
11.73 |
313.15 |
0.7944 |
10.01 |
313.15 |
0.8329 |
9.12 |
313.15 |
0.9229 |
7.04 |
318.15 |
0.0864 |
32.18 |
318.15 |
0.1642 |
30.01 |
318.15 |
0.2761 |
26.89 |
318.15 |
0.3529 |
24.75 |
318.15 |
0.4257 |
22.70 |
318.15 |
0.4894 |
20.91 |
318.15 |
0.5829 |
18.26 |
318.15 |
0.6508 |
16.34 |
318.15 |
0.7210 |
14.40 |
318.15 |
0.7947 |
12.32 |
318.15 |
0.8331 |
11.25 |
318.15 |
0.9230 |
8.77 |
323.15 |
0.0865 |
38.78 |
323.15 |
0.1643 |
36.18 |
323.15 |
0.2762 |
32.43 |
323.15 |
0.3529 |
29.88 |
323.15 |
0.4259 |
27.44 |
323.15 |
0.4896 |
25.30 |
323.15 |
0.5824 |
22.18 |
323.15 |
0.6513 |
19.85 |
323.15 |
0.7215 |
17.53 |
323.15 |
0.7952 |
15.08 |
323.15 |
0.8335 |
13.79 |
323.15 |
0.9231 |
10.83 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrachloroethylene (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
283.15 |
0.0862 |
6.94 |
283.15 |
0.1638 |
6.45 |
283.15 |
0.2756 |
5.75 |
283.15 |
0.3520 |
5.25 |
283.15 |
0.4245 |
4.79 |
283.15 |
0.4890 |
4.36 |
283.15 |
0.5816 |
3.77 |
283.15 |
0.6494 |
3.32 |
283.15 |
0.7200 |
2.86 |
283.15 |
0.7935 |
2.38 |
283.15 |
0.8323 |
2.12 |
283.15 |
0.9226 |
1.53 |
288.15 |
0.0863 |
8.90 |
288.15 |
0.1639 |
8.27 |
288.15 |
0.2757 |
7.36 |
288.15 |
0.3521 |
6.74 |
288.15 |
0.4247 |
6.15 |
288.15 |
0.4890 |
5.62 |
288.15 |
0.5817 |
4.85 |
288.15 |
0.6495 |
4.29 |
288.15 |
0.7201 |
3.71 |
288.15 |
0.7935 |
3.09 |
288.15 |
0.8323 |
2.78 |
288.15 |
0.9227 |
2.04 |
293.15 |
0.0863 |
11.25 |
293.15 |
0.1640 |
10.46 |
293.15 |
0.2758 |
9.33 |
293.15 |
0.3523 |
8.55 |
293.15 |
0.4249 |
7.82 |
293.15 |
0.4891 |
7.13 |
293.15 |
0.5818 |
6.17 |
293.15 |
0.6496 |
5.49 |
293.15 |
0.7202 |
4.74 |
293.15 |
0.7936 |
3.98 |
293.15 |
0.8324 |
3.60 |
293.15 |
0.9227 |
2.66 |
298.15 |
0.0864 |
14.11 |
298.15 |
0.1641 |
13.14 |
298.15 |
0.2759 |
11.72 |
298.15 |
0.3525 |
10.74 |
298.15 |
0.4251 |
9.81 |
298.15 |
0.4892 |
8.99 |
298.15 |
0.5819 |
7.80 |
298.15 |
0.6497 |
6.94 |
298.15 |
0.7202 |
6.03 |
298.15 |
0.7937 |
5.08 |
298.15 |
0.8325 |
4.62 |
298.15 |
0.9227 |
3.43 |
303.15 |
0.0863 |
17.62 |
303.15 |
0.1639 |
16.42 |
303.15 |
0.2761 |
14.64 |
303.15 |
0.3527 |
13.43 |
303.15 |
0.4255 |
12.28 |
303.15 |
0.4894 |
11.26 |
303.15 |
0.5820 |
9.82 |
303.15 |
0.6499 |
8.72 |
303.15 |
0.7204 |
7.60 |
303.15 |
0.7939 |
6.44 |
303.15 |
0.8326 |
5.84 |
303.15 |
0.9228 |
4.43 |
308.15 |
0.0863 |
21.71 |
308.15 |
0.1640 |
20.22 |
308.15 |
0.2758 |
18.08 |
308.15 |
0.3524 |
16.61 |
308.15 |
0.4251 |
15.22 |
308.15 |
0.4896 |
13.94 |
308.15 |
0.5822 |
12.16 |
308.15 |
0.6501 |
10.84 |
308.15 |
0.7205 |
9.48 |
308.15 |
0.7941 |
8.05 |
308.15 |
0.8327 |
7.32 |
308.15 |
0.9228 |
5.60 |
313.15 |
0.0864 |
26.52 |
313.15 |
0.1641 |
24.72 |
313.15 |
0.2760 |
22.12 |
313.15 |
0.3527 |
20.32 |
313.15 |
0.4254 |
18.65 |
313.15 |
0.4893 |
17.16 |
313.15 |
0.5825 |
14.98 |
313.15 |
0.6504 |
13.38 |
313.15 |
0.7207 |
11.73 |
313.15 |
0.7944 |
10.01 |
313.15 |
0.8329 |
9.12 |
313.15 |
0.9229 |
7.04 |
318.15 |
0.0864 |
32.18 |
318.15 |
0.1642 |
30.01 |
318.15 |
0.2761 |
26.89 |
318.15 |
0.3529 |
24.75 |
318.15 |
0.4257 |
22.70 |
318.15 |
0.4894 |
20.91 |
318.15 |
0.5829 |
18.26 |
318.15 |
0.6508 |
16.34 |
318.15 |
0.7210 |
14.40 |
318.15 |
0.7947 |
12.32 |
318.15 |
0.8331 |
11.25 |
318.15 |
0.9230 |
8.77 |
323.15 |
0.0865 |
38.78 |
323.15 |
0.1643 |
36.18 |
323.15 |
0.2762 |
32.43 |
323.15 |
0.3529 |
29.88 |
323.15 |
0.4259 |
27.44 |
323.15 |
0.4896 |
25.30 |
323.15 |
0.5824 |
22.18 |
323.15 |
0.6513 |
19.85 |
323.15 |
0.7215 |
17.53 |
323.15 |
0.7952 |
15.08 |
323.15 |
0.8335 |
13.79 |
323.15 |
0.9231 |
10.83 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Tetrachloroethylene (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
1586.1 |
0.0946 |
1583.5 |
0.1904 |
1582.4 |
0.2873 |
1582.0 |
0.3853 |
1582.5 |
0.4845 |
1583.8 |
0.5859 |
1587.2 |
0.6876 |
1590.1 |
0.7904 |
1596.8 |
0.8946 |
1603.2 |
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 (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
1586.1 |
0.0946 |
1583.5 |
0.1904 |
1582.4 |
0.2873 |
1582.0 |
0.3853 |
1582.5 |
0.4845 |
1583.8 |
0.5859 |
1587.2 |
0.6876 |
1590.1 |
0.7904 |
1596.8 |
0.8946 |
1603.2 |
1.0000 |
1610.2 |
Sources