Table 2
Operating and design conditions of the existing NGL plant and added LNG part.
| Stream | T (°C) | P (bar) | Flow (kmol hr−1) | Stream | T (°C) | P (bar) | Flow (kmol hr−1) |
|---|---|---|---|---|---|---|---|
| 31 | 22.0 | 64.4 | 25 649 | 142 | 19.0 | 8.2 | 3403 |
| 32 | 22.0 | 64.4 | 25 612 | 144 | 2.4 | 5.1 | 865 |
| 35 | 23.0 | 63.7 | 25 607 | 145 | −1.6 | 4.5 | 423 |
| 36 | 22.7 | 63.1 | 23 814 | 146 | −0.1 | 4.5 | 423 |
| 38 | 300.0 | 61.0 | 1792 | 147 | 1.6 | 4.5 | 1288 |
| 39 | 60.0 | 59.4 | 1880 | 148 | 19 | 8.0 | 2712 |
| 41 | 60.0 | 59.3 | 1800 | 149 | 77.3 | 22.6 | 4000 |
| 42 | 71.5 | 65.2 | 1800 | 247 | −84.5 | 60.8 | 6697 |
| 51 | 27.7 | 62 | 23 814 | 248 | −87.2 | 30.0 | 22 085 |
| 52 | −35 | 61 | 23 814 | 249 | 9.3 | 30.1 | 2714 |
| 53 | −35 | 61 | 803 | 250 | −38.9 | 30.1 | 3143 |
| 54 | −66.8 | 30.4 | 16 315 | 256 | 14.3 | 29.8 | 2714 |
| 55 | −48.8 | 30.4 | 803 | 261 | −15.4 | 29.8 | 3143 |
| 56 | 16.2 | 28.8 | 22 085 | NG-3 | −38.3 | 75.0 | 22 085 |
| 57 | 33.4 | 28.3 | 22 085 | MR-1 | 35.0 | 48.0 | 29 765 |
| 58 | 36.3 | 30.2 | 1729 | MR-4 | −38.3 | 48.0 | 29 765 |
| 59 | 36.6 | 33.2 | 1729 | MR-5V | −130.0 | 48.0 | 8874 |
| 63 | 8.7 | 30 | 954 | MR-5L | −130.0 | 48.0 | 20 891 |
| 64 | 104.6 | 30.8 | 776 | MR-7V | −166.4 | 2.9 | 8874 |
| 81 | 89.3 | 22.8 | 1551 | MR-8V | −136.3 | 2.9 | 8874 |
| 85 | 134.2 | 22.6 | 631 | MR-10 | −135.1 | 2.9 | 29 765 |
| 86 | 89.5 | 8.7 | 631 | MR-14 | 102.9 | 48.0 | 29 765 |
| 89 | 60.7 | 7.5 | 413 | C3-1 | 35.0 | 12.2 | 30 746 |
| 90 | 127.5 | 8.5 | 218 | C3-2 | 35.0 | 12.2 | 6964 |
| 91 | 61.8 | 21.6 | 920 | C3-8 | −14.9 | 2.45 | 17 186 |
| 141 | 60.0 | 21.6 | 4000 | C3-10 | 14.1 | 5.47 | 30 746 |