Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Propenenitrile (1) - Liquid mixture 2 |
---|---|
288.15 | 0.9720 |
298.15 | 0.9710 |
313.15 | 0.9650 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Propenenitrile (1) - Liquid mixture 1 |
---|---|
288.15 | 0.0680 |
298.15 | 0.0820 |
313.15 | 0.0890 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of 2-Propenenitrile (1) - Liquid |
---|---|
274.15 | 1.2429 |
294.65 | 5.2308 |
294.65 | 8.0734 |
296.15 | 9.1868 |
310.15 | 25.299 |
320.15 | 40.028 |
331.15 | 73.904 |
333.15 | 97.824 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Propenenitrile (1) - Liquid mixture 2 |
---|---|
288.15 | 0.9720 |
298.15 | 0.9710 |
313.15 | 0.9650 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Propenenitrile (1) - Liquid mixture 1 |
---|---|
288.15 | 0.0680 |
298.15 | 0.0820 |
313.15 | 0.0890 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of 2-Propenenitrile (1) - Liquid |
---|---|
274.15 | 1.2429 |
294.65 | 5.2308 |
294.65 | 8.0734 |
296.15 | 9.1868 |
310.15 | 25.299 |
320.15 | 40.028 |
331.15 | 73.904 |
333.15 | 97.824 |