Two, parallel LNG trains are provided to produce a total of more than 10.8 MMTPA of LNG. In addition to LNG, the process units will produce LPG, condensate and sulphur.
H/C Condensate shall be sent to Up-Steam for export.
Allowance is made in the layout of the LNG Plant for future expansion up to 4 LNG trains.
The design of the LNG trains shall be such that the shutdown of one LNG train does not require the shutdown of the other LNG train. Where practical, cross connections between units shall be provided to ensure minimal loss of capacity during shutdown of parallel units or equipment. The feedstock to the facilities is delivered via pipeline from the offshore facilities to the inlet of the slug catcher.
The process unitsare listed below and shown in the simplified block flow diagram, Figure 2:
| Description | No of Trains |
11 | Feed Gas Metering | 1 |
12 | Acid Gas Removal | 2 |
13 | Dehydration & Mercaptan Removal | 2 |
14 | Mercury Removal | 2 |
15 | Liquefaction | 2 |
16 | Refrigeration | 2 |
17 | Fractionation | 2 |
18 | Nitrogen Rejection | 2 |
19 | Sulfur Recovery | 2 |
20 | LPG Sweetening | 2 |
Utility Units Summary
Utility units which are common to both process trains are listed bellow and shown in the simplified block flow diagram, Figure 2:
Unit No. | Description |
61 | Power Generation |
62 | Steam and Condensate System |
63 | Fuel System |
64 | Fresh Water System |
65 | Compressed Air System |
66 | Nitrogen System |
67 | Sea Water System |
Off-site Units Summary
Off-site units which are common to both process trains are listed bellow and shown in the simplified block flow diagram, Figure 2:
Unit No. | Description |
71 | LNG Rundown, Storage and Loading |
72 | Refrigerant Storage |
73 | Condensate Rundown |
74 | Flare System |
75 | Fire Protection System |
76 | Sulfur Solidification, Storage and Loading |
77 | Effluent Treatment System |
78 | Irrigation Water System |
79 | LPG Rundown, Storage and Loading |