A final environmental and social impact assessment (ESIA) report for the project issued in November 2015 and based on its original nameplate capacity outlined original process design capacities as follows: • Crude distillation; 477,273 b/sd. • Saturate gas concentration; 1,839 tonnes/day. • Saturate LPG Merox; 18,700 b/sd. • Kerosine merox; 119,200 b/sd. • Mild hydrocracking (unicracking); 148,000 b/sd. • Naphtha hydrodesulfurization; 115,000 b/sd. • CCR platforming; 118,300 b/sd. • Isomerization (penex); 52,000 b/sd. • RFCC gasoline hydrodesulfurization; 71,300 b/sd. • RFCC; 171,800 b/sd. • Unsaturated LPG merox; 68,700 b/sd. • C5-extraction merox; 20,800 b/sd. • Propylene recovery; 68,700 b/sd. • UOP huels selective hydrogenation; 25,900 b/sd. • Sulfuric acid alkylation, regeneration; 26,300 b/sd. • C4 isomerization (butamer); 8,400 b/sd. • Hydrogen generation; 436 tonnes/day. • Sulfur recovery; 230 tonnes/day. • Amine regeneration (unsaturated); 108.4 tonnes/hr. • Amine regeneration (saturated); 90 tonnes/hr. • Nonphenolic sour water stripping; 100 tonnes/hr. • Phenolic sour water stripping; 283 tonnes/hr.

Link