Table 4.
[Recycle amount (kg/s), Bottom operating pressure of deethanizer (MPaa), Bottom operating pressure of debutanizer (MPaa)] |
|||||
---|---|---|---|---|---|
First Interval [12–45, 0.45–0.85, 0.5–0.7] |
|||||
Execution number |
|||||
1 | 2 | 3 | 4 | 5 | |
Optimum recycled flowrate (kg/s) | 12 | 12 | 12 | 12 | 12 |
Optimum bottom operating pressure for deethanizer(MPaa) | 0.85 | 0.85 | 0.85 | 0.85 | 0.85 |
Optimum bottom operating pressure for debutanizer (MPaa) | 0.50 | 0.50 | 0.50 | 0.50 | 0.50 |
TAC (1000 USD/year) | 1132.90 | 1132.92 | 1132.95 | 1132.90 | 1132.98 |
CPU time (s) | 973 | 978 | 1026 | 950 | 1000 |
Function evaluations | 690 | 690 | 690 | 690 | 690 |
Second Interval [3.2–12, 0.8–0.85, 0.5–0.7] |
|||||
---|---|---|---|---|---|
Execution number |
|||||
1 | 2 | 3 | 4 | 5 | |
Optimum recycled flowrate (kg/s) | 3.2 | 3.2 | 3.2 | 3.2 | 3.2 |
Optimum bottom operating pressure for deethanizer (MPaa) | 0.85 | 0.85 | 0.85 | 0.85 | 0.85 |
Optimum bottom operating pressure for debutanizer (MPaa) | 0.50 | 0.50 | 0.50 | 0.50 | 0.50 |
TAC (1000 USD/year) | 821.420 | 821.465 | 821.452 | 821.420 | 821.420 |
CPU time (s) | 493 | 480 | 490 | 490 | 490 |
Function evaluations | 660 | 660 | 660 | 660 | 660 |