REFERENCES FOR TECHNOLOGY/LICENSOR SELECTION
The Owner of The Company was either team leader or team member for all steps (Investment Planning and Technology Selection) on the implementation of the following units.
| Unıt | Capacity, M3/Day | Licensor | Date |
| Refinery X | |||
| PENEX UNIT | 2600 | UOP | 1996 |
| CCR REFORMER | 4.700 | UOP | 2000 |
| DIESEL/KEROSENE HYDROPROCESSING | 8.500 | UOP | 1998 |
| BENZENE SATURATION | 3.800 | AXENS | 2005 |
| FCC GASOLINE DESULFURIZATION | 1.600 | AXENS | 2005 |
| KEROSEN TREATING UNIT | 5.500 | MERICHEM | 2009 |
| SELECTIVE HYDROGENATION UNIT | 450 | UOP | 2010 |
| COOKER UNIT | 8.200 | FOSTER WHEELER | 2008 |
| VACUUM DISTILLATION UNIT | 7.500 | SHELL GLOBAL SOLUTIONS | 2008 |
| HYDROCRACKER UNIT- TWO STAGE | 8.000 | UOP | 2009 |
| DIESEL DESULPHURIZATION UNIT | 4.000 | ||
| NAPHTHA HYDROTREATING UNIT | 1.200 | ||
| HYDROGEN UNIT | 160000 NM^3/hr | TECHNIP | 2009 |
| Refinery Y | |||
| HEAVY NAPHTHA HYDROTREATING | 3200 | UOP | 1996 |
| CCR REFORMER | 3200 | UOP | 1996 |
| NAPHTHA SPLITTING | 4500 | UOP | |
| LIGHT NAPHTHA HYDROTREATING | 2000 | UOP | |
| Isomerization | 2000 | UOP | 1996 |
| DIESEL/KEROSENE HYDROPROCESSING | 9600 | UOP | 1998 |
| FCC GASOLINE DESULPHURIZATION | 1600 | AXENS | 2005 |
| KEROSENE TREATING UNIT | 3600 | MERICHEM | 2009 |
| Refinery Z | |||
| CCR REFORMER | 3600 | AXENS | 2002 |
| BENZENE SATURATION | 3600 | AXENS | 2002 |
| DIESEL/KEROSENE HYDROPROCESSING | 4500 | ABB LUMMUS | 2001 |