Operational condition: Mole fraction = 0 (Gas)
Temperature, K - Gas | Activity coefficient of 1,3-Butadiene (1) - Gas |
---|---|
374.00 | 5.0 |
393.30 | 4.7 |
412.50 | 4.2 |
Operational condition: Mole fraction = 0 (Gas)
Temperature, K - Gas | Activity coefficient of 1,3-Butadiene (1) - Gas |
---|---|
374.00 | 5.0 |
393.30 | 4.7 |
412.50 | 4.2 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of 1,3-Butadiene (1) - Liquid |
---|---|
374.00 | 7000.0 |
393.30 | 8900.0 |
412.50 | 10500.0 |
431.60 | 11200.0 |
451.00 | 11700.0 |
470.10 | 12100.0 |
489.50 | 12000.0 |
513.38 | 8700.0 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of 1,3-Butadiene (1) - Liquid |
---|---|
374.00 | 7000.0 |
393.30 | 8900.0 |
412.50 | 10500.0 |
431.60 | 11200.0 |
451.00 | 11700.0 |
470.10 | 12100.0 |
489.50 | 12000.0 |
513.38 | 8700.0 |
Operational condition: Temperature, K = 323.15 (VLE)
Fixed | Measured | |
---|---|---|
P [kPa] - VLE | x1[mol/mol] of 1,3-Butadiene (1) - Liquid | y1[mol/mol] of 1,3-Butadiene (1) - Vapour |
55.329 | 0.0000 | 0.0000 |
286.91 | 0.1000 | 0.8230 |
418.766 | 0.2000 | 0.8880 |
487.293 | 0.3000 | 0.9090 |
528.89 | 0.4000 | 0.9200 |
552.221 | 0.5000 | 0.9270 |
561.154 | 0.6000 | 0.9300 |
567.287 | 0.7000 | 0.9330 |
573.686 | 0.8000 | 0.9370 |
582.219 | 0.9000 | 0.9450 |
571.686 | 1.0000 | 1.0000 |