Table 2.
The exergy flow of the proposed integrated and optimal PPE processing system and the exergy efficiency is 80%.
| Exergy Input |
Exergy Output |
||
|---|---|---|---|
| Input | Exergy Flows (J/s) | Output | Exergy Flows (J/s) |
| N2 | 1,548 | C2H4 | 57,319 |
| O2 | 1,925 | C3H6 | 39,891 |
| PPE | 503,390 | C3H8 | 10,065 |
| H2O | 1,423 | C4H10 | 13,383 |
| LP Steam | 842,702 | Light Naphtha | 12,401 |
| MP Steam | 732,229 | Aromatic Mix | 34,466 |
| HP Steam | 641,043 | Gasoline | 4,044 |
| Cooling Water | 740,546 | Diesel | 37,195 |
| Electricity | 66,086 | Sulfur | 18 |
| Bauxite | 89,757 | ||
| Offgas | 2,542,131 | ||