Operational conditions:
| Mole fraction of Trichloroethylene (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0897 | 0.0006 |
| 0.1540 | 0.0006 |
| 0.2402 | 0.0006 |
| 0.3180 | 0.0006 |
| 0.3990 | 0.0006 |
| 0.4801 | 0.0006 |
| 0.5624 | 0.0006 |
| 0.6400 | 0.0006 |
| 0.7180 | 0.0006 |
| 0.8000 | 0.0006 |
| 0.8834 | 0.0006 |
| 0.9632 | 0.0006 |
Operational conditions:
| Mole fraction of Trichloroethylene (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0897 | 0.0006 |
| 0.1540 | 0.0006 |
| 0.2402 | 0.0006 |
| 0.3180 | 0.0006 |
| 0.3990 | 0.0006 |
| 0.4801 | 0.0006 |
| 0.5624 | 0.0006 |
| 0.6400 | 0.0006 |
| 0.7180 | 0.0006 |
| 0.8000 | 0.0006 |
| 0.8834 | 0.0006 |
| 0.9632 | 0.0006 |
Operational conditions:
| Mole fraction of Trichloroethylene (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0897 | 1.4921 |
| 0.1540 | 1.4911 |
| 0.2402 | 1.4897 |
| 0.3180 | 1.4885 |
| 0.3990 | 1.4873 |
| 0.4801 | 1.486 |
| 0.5624 | 1.4844 |
| 0.6400 | 1.4829 |
| 0.7210 | 1.4811 |
| 0.7988 | 1.4794 |
| 0.8834 | 1.4775 |
| 0.9610 | 1.4753 |
Operational conditions:
| Mole fraction of Trichloroethylene (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0897 | 1.4921 |
| 0.1540 | 1.4911 |
| 0.2402 | 1.4897 |
| 0.3180 | 1.4885 |
| 0.3990 | 1.4873 |
| 0.4801 | 1.486 |
| 0.5624 | 1.4844 |
| 0.6400 | 1.4829 |
| 0.7210 | 1.4811 |
| 0.7988 | 1.4794 |
| 0.8834 | 1.4775 |
| 0.9610 | 1.4753 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloroethylene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0843 | 899.17 |
| 293.15 | 0.1806 | 944.97 |
| 293.15 | 0.2528 | 980.96 |
| 293.15 | 0.3239 | 1017.91 |
| 293.15 | 0.4030 | 1060.83 |
| 293.15 | 0.4900 | 1110.44 |
| 293.15 | 0.5689 | 1157.79 |
| 293.15 | 0.6381 | 1201.31 |
| 293.15 | 0.7202 | 1255.5 |
| 293.15 | 0.7975 | 1309.15 |
| 293.15 | 0.8925 | 1379.16 |
| 293.15 | 0.9582 | 1430.28 |
| 298.15 | 0.0843 | 894.6 |
| 298.15 | 0.1806 | 940.12 |
| 298.15 | 0.2528 | 975.88 |
| 298.15 | 0.3239 | 1012.59 |
| 298.15 | 0.4030 | 1055.25 |
| 298.15 | 0.4900 | 1104.53 |
| 298.15 | 0.5689 | 1151.57 |
| 298.15 | 0.6381 | 1194.8 |
| 298.15 | 0.7202 | 1248.62 |
| 298.15 | 0.7975 | 1301.88 |
| 298.15 | 0.8925 | 1371.4 |
| 298.15 | 0.9582 | 1422.14 |
| 303.15 | 0.0843 | 890.02 |
| 303.15 | 0.1806 | 935.27 |
| 303.15 | 0.2528 | 970.8 |
| 303.15 | 0.3239 | 1007.28 |
| 303.15 | 0.4030 | 1049.65 |
| 303.15 | 0.4900 | 1098.61 |
| 303.15 | 0.5689 | 1145.35 |
| 303.15 | 0.6381 | 1188.25 |
| 303.15 | 0.7202 | 1241.69 |
| 303.15 | 0.7975 | 1294.56 |
| 303.15 | 0.8925 | 1363.59 |
| 303.15 | 0.9582 | 1413.95 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Trichloroethylene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0843 | 899.17 |
| 293.15 | 0.1806 | 944.97 |
| 293.15 | 0.2528 | 980.96 |
| 293.15 | 0.3239 | 1017.91 |
| 293.15 | 0.4030 | 1060.83 |
| 293.15 | 0.4900 | 1110.44 |
| 293.15 | 0.5689 | 1157.79 |
| 293.15 | 0.6381 | 1201.31 |
| 293.15 | 0.7202 | 1255.5 |
| 293.15 | 0.7975 | 1309.15 |
| 293.15 | 0.8925 | 1379.16 |
| 293.15 | 0.9582 | 1430.28 |
| 298.15 | 0.0843 | 894.6 |
| 298.15 | 0.1806 | 940.12 |
| 298.15 | 0.2528 | 975.88 |
| 298.15 | 0.3239 | 1012.59 |
| 298.15 | 0.4030 | 1055.25 |
| 298.15 | 0.4900 | 1104.53 |
| 298.15 | 0.5689 | 1151.57 |
| 298.15 | 0.6381 | 1194.8 |
| 298.15 | 0.7202 | 1248.62 |
| 298.15 | 0.7975 | 1301.88 |
| 298.15 | 0.8925 | 1371.4 |
| 298.15 | 0.9582 | 1422.14 |
| 303.15 | 0.0843 | 890.02 |
| 303.15 | 0.1806 | 935.27 |
| 303.15 | 0.2528 | 970.8 |
| 303.15 | 0.3239 | 1007.28 |
| 303.15 | 0.4030 | 1049.65 |
| 303.15 | 0.4900 | 1098.61 |
| 303.15 | 0.5689 | 1145.35 |
| 303.15 | 0.6381 | 1188.25 |
| 303.15 | 0.7202 | 1241.69 |
| 303.15 | 0.7975 | 1294.56 |
| 303.15 | 0.8925 | 1363.59 |
| 303.15 | 0.9582 | 1413.95 |