| Name | Data Input (Amount/Value) | Operational Condition (Temperature) | Equipment/Stream |
| Crude JO: Base Total Flowrate | 5000 l/batch (or 4600 kg/batch) | 30 ±1˚C (Room Temp.) | Fed to PFF-101 |
| Crude JO: Composition | Ref. Table 2 | 30˚C ±1˚C | Fed to PFF-101 |
| Water | 5% by volume of oil | 30˚C ±1˚C | Added to V-101 |
| Pure oil | -- | 80˚C ±1˚C | In the V-102 |
| Phosphoric Acid | 0.2% by volume of oil | -- | Charged to V-102 |
| Sodium Hydroxide | 3.5 g/l of oil | -- | Charged to V-102 |
| Water2 | 40% by volume of oil | 50˚C ±1˚C | Leaving HX-101; Added to V-103 |
| Pure oil | -- | 140˚C ±1˚C | In the EV-101 |
| Pure oil | -- | 30˚C ±1˚C | In the V-105 |
| NGC | 10% by volume of oil | 30˚C ±1˚C | Added to V-105 |
| Efficiency: Water degumming | 30% gums removal | -- | Pure oil Leaving V-101 |
| Efficiency: Acid degumming | 98% gums removal | -- | Pure oil Leaving V-102 |
| Efficiency: Neutralisation | 98% FFAs removal | -- | Pure oil Leaving V-102 |
| Yield: pure oil (after acid degumming and neutralisation) | 97% | -- | Pure oil Leaving PFF-103 |
| Yield-final: pure oil (after drying) | 97% | -- | Pure oil Leaving EV-101 |
| Efficiency: Blending | 65% Viscosity Reduction | -- | MPO Leaving V-105 (Final Product) |