Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Propane, 2-ethoxy-2-methyl- (1) - Liquid |
|---|---|
| 288.15 | 325.0 |
| 298.15 | 514.0 |
| 308.15 | 659.0 |
| 318.15 | 873.0 |
Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Propane, 2-ethoxy-2-methyl- (1) - Liquid |
|---|---|
| 288.15 | 325.0 |
| 298.15 | 514.0 |
| 308.15 | 659.0 |
| 318.15 | 873.0 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
|---|---|
| 278.15 | 0.0140 |
| 288.15 | 0.0155 |
| 298.15 | 0.0166 |
| 308.15 | 0.0178 |
| 318.15 | 0.0187 |
| 328.15 | 0.0193 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
|---|---|
| 278.15 | 0.0140 |
| 288.15 | 0.0155 |
| 298.15 | 0.0166 |
| 308.15 | 0.0178 |
| 318.15 | 0.0187 |
| 328.15 | 0.0193 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
|---|---|
| 278.15 | 996.11 |
| 288.15 | 996.17 |
| 298.15 | 994.97 |
| 308.15 | 992.35 |
| 318.15 | 989.07 |
| 328.15 | 984.73 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
|---|---|
| 278.15 | 759.85 |
| 288.15 | 747.67 |
| 298.15 | 737.63 |
| 308.15 | 727.42 |
| 318.15 | 717.17 |
| 328.15 | 706.84 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
|---|---|
| 278.15 | 996.11 |
| 288.15 | 996.17 |
| 298.15 | 994.97 |
| 308.15 | 992.35 |
| 318.15 | 989.07 |
| 328.15 | 984.73 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
|---|---|
| 278.15 | 759.85 |
| 288.15 | 747.67 |
| 298.15 | 737.63 |
| 308.15 | 727.42 |
| 318.15 | 717.17 |
| 328.15 | 706.84 |