Difference between revisions of "Elefsina Refinery Upgrade Project"
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| − | Summary Information | + | === Summary Information === |
* Ownership: Hellenic Petroleum | * Ownership: Hellenic Petroleum | ||
| Line 11: | Line 11: | ||
* Budget: €1.2 Billion | * Budget: €1.2 Billion | ||
| − | + | === The Project === | |
* Project Type: Major Upgrade | * Project Type: Major Upgrade | ||
* Project Summary: The project is designed to improve the refinery's complexity, through the addition of a Flexicoker, Hydrocracker and other units. | * Project Summary: The project is designed to improve the refinery's complexity, through the addition of a Flexicoker, Hydrocracker and other units. | ||
* Main Contractors: | * Main Contractors: | ||
| − | + | ** Foster Wheeler, FEED | |
| − | + | ** Tecnicas Reunidas, EPCM | |
| − | + | === Refining Units === | |
* Vacuum Distillation Unit - 45,300 bbls/day | * Vacuum Distillation Unit - 45,300 bbls/day | ||
| Line 30: | Line 30: | ||
* Associated utilities and offsites. | * Associated utilities and offsites. | ||
| − | + | === Terminal Capacity === | |
* Crude Oil: | * Crude Oil: | ||
* Refined Products: | * Refined Products: | ||
| − | + | === Crude Supply === | |
* The share of heavy crudes processed will increase from 60% to 100% | * The share of heavy crudes processed will increase from 60% to 100% | ||
| − | + | === Products Produced === | |
* The project increases production of white products at the expense of fuel oil. | * The project increases production of white products at the expense of fuel oil. | ||
| Line 47: | Line 47: | ||
| − | + | === Other Information === | |
* Aims of the upgrade: | * Aims of the upgrade: | ||
| − | + | ** Increase processing of medium- to highsulfur crudes: 60% 100% | |
| − | + | ** Increase production of white products at the expense of fuel oil: | |
| − | + | *** Light Products: 52% - 100% | |
| − | + | *** Black products: 48% - 0% | |
| − | + | ** Reduce emissions: | |
| − | + | *** SO2: 642 kg/hr < 200 kg/hr | |
| − | + | *** NOx: 92 kg/hr < 90 kg/hr | |
| − | + | *** PM: 45 kg/hr < 20 kg/hr | |
| − | + | === History === | |
* 2006 - Foster Wheeler Awarded Front-End Engineering Design Contract | * 2006 - Foster Wheeler Awarded Front-End Engineering Design Contract | ||
* 2012 - Refinery upgrade completed | * 2012 - Refinery upgrade completed | ||
| − | + | === Links === | |
# [http://www.hellenic-petroleum.gr/online/generic.aspx?mid=163&pid=109 Hellenic Petroleum Refining Page] | # [http://www.hellenic-petroleum.gr/online/generic.aspx?mid=163&pid=109 Hellenic Petroleum Refining Page] | ||
Latest revision as of 16:30, 26 January 2021
Contents
Summary Information
- Ownership: Hellenic Petroleum
- Website: http://www.hellenic-petroleum.gr/online/index.aspx
- Wiki Page: Elefsina Refinery
- Location: South of Athens, Greece
- Capacity: million tons/annum & bbl/day
- Nelson Complexity: Current, 1.5, After Completion, 7.2
- Project Stage: [[[Completed Refinery Projects | Completed]]]
- Expected Completion: [[[Refinery Projects to be Completed in 2012 | 2012]]]
- Budget: €1.2 Billion
The Project
- Project Type: Major Upgrade
- Project Summary: The project is designed to improve the refinery's complexity, through the addition of a Flexicoker, Hydrocracker and other units.
- Main Contractors:
- Foster Wheeler, FEED
- Tecnicas Reunidas, EPCM
Refining Units
- Vacuum Distillation Unit - 45,300 bbls/day
- [[[Flexicoking]]] - Exxon Mobil - 20,050 bbls/day
- [[[Hydrocracker]]] - UOP - 40,000 bbls/day
- Hydrogen Plant - Haldor Topsøe- 120,000 m3/h
- Sulphur Recovery Unit 2 X 140 t/d
- Sour Water Stripper 120 m3/h
- Amine Recovery Unit 280 t/d
- Associated utilities and offsites.
Terminal Capacity
- Crude Oil:
- Refined Products:
Crude Supply
- The share of heavy crudes processed will increase from 60% to 100%
Products Produced
- The project increases production of white products at the expense of fuel oil.
- It will address the shortage of diesel locally and regionally
- Middle Distillate yield will increase to 75%
Other Information
- Aims of the upgrade:
- Increase processing of medium- to highsulfur crudes: 60% 100%
- Increase production of white products at the expense of fuel oil:
- Light Products: 52% - 100%
- Black products: 48% - 0%
- Reduce emissions:
- SO2: 642 kg/hr < 200 kg/hr
- NOx: 92 kg/hr < 90 kg/hr
- PM: 45 kg/hr < 20 kg/hr
History
- 2006 - Foster Wheeler Awarded Front-End Engineering Design Contract
- 2012 - Refinery upgrade completed
