Difference between revisions of "Thessaloniki Refinery Project"

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(Created page with "Summary Information * Ownership: Hellenic Petroleum * Website: http://www.hellenic-petroleum.gr/online/index.aspx * Wiki Page: [[[Thessaloniki Refinery]]] * Location: Thessa...")
 
 
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* Ownership:  Hellenic Petroleum
 
* Ownership:  Hellenic Petroleum
 
* Website: http://www.hellenic-petroleum.gr/online/index.aspx
 
* Website: http://www.hellenic-petroleum.gr/online/index.aspx
* Wiki Page: [[[Thessaloniki Refinery]]]
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* Wiki Page: [[Thessaloniki Refinery]]
 
* Location: Thessaloniki, North East Greece  
 
* Location: Thessaloniki, North East Greece  
 
* Capacity:  million tons/annum & bbl/day  
 
* Capacity:  million tons/annum & bbl/day  
 
* Nelson Complexity: Increase from  6.7 to 7.3
 
* Nelson Complexity: Increase from  6.7 to 7.3
 
* Project Stage: Construction  
 
* Project Stage: Construction  
* Expected Completion: Commissioning completed in [[[Refinery Projects to be Completed in 2011 | 2011]]]
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* Expected Completion: Commissioning completed in [[Refinery Projects to be Completed in 2011 | 2011]]
 
* Budget: €200 million
 
* Budget: €200 million
  
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* Project Type: Upgrade
 
* Project Type: Upgrade
 
* Project Summary:  
 
* Project Summary:  
* Upgrading of existing Thessaloniki Refinery to increase production of low-sulphur gasoline and diesel for supporting regional consumption growth.
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** Upgrading of existing Thessaloniki Refinery to increase production of low-sulphur gasoline and diesel for supporting regional consumption growth.
* The project comprises:
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** The project comprises:
  * New 15.000 bpsd (barrels per stream day) continuous catalytic reformer  
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*** New 15.000 bpsd (barrels per stream day) continuous catalytic reformer  
  * Modification to existing atmospheric distillation Unit to allow switching  operations from high to low-sulphur crudes and increase distillation capacity
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*** Modification to existing atmospheric distillation Unit to allow switching  operations from high to low-sulphur crudes and increase distillation capacity
  * Revamp of existing naphtha hydrofiner and crude light ends processing to increase light ends processing capacity to 26.000 bpsd
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*** Revamp of existing naphtha hydrofiner and crude light ends processing to increase light ends processing capacity to 26.000 bpsd
 
* Main Contractors:  
 
* Main Contractors:  
* Foster Wheeler: EPCm services for the overall Refinery Upgrading, till Ready for Start-up (RFSU) LS Services contract for Offshore activities; RR contract (with ceiling) for Onshore activities
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** Foster Wheeler: EPCm services for the overall Refinery Upgrading, till Ready for Start-up (RFSU) LS Services contract for Offshore activities; RR contract (with ceiling) for Onshore activities
 
* Three Licensors involved, as follows:
 
* Three Licensors involved, as follows:
* Axens (CCR)
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** Axens (CCR)
* Exxonmobil (APS)
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** Exxonmobil (APS)
* MW Kellogg (LVN and Crude Light Ends)
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** MW Kellogg (LVN and Crude Light Ends)
  
 
+++ Refining Units
 
+++ Refining Units

Latest revision as of 17:19, 14 July 2024

Summary Information

+++ The Project

  • Project Type: Upgrade
  • Project Summary:
    • Upgrading of existing Thessaloniki Refinery to increase production of low-sulphur gasoline and diesel for supporting regional consumption growth.
    • The project comprises:
      • New 15.000 bpsd (barrels per stream day) continuous catalytic reformer
      • Modification to existing atmospheric distillation Unit to allow switching operations from high to low-sulphur crudes and increase distillation capacity
      • Revamp of existing naphtha hydrofiner and crude light ends processing to increase light ends processing capacity to 26.000 bpsd
  • Main Contractors:
    • Foster Wheeler: EPCm services for the overall Refinery Upgrading, till Ready for Start-up (RFSU) LS Services contract for Offshore activities; RR contract (with ceiling) for Onshore activities
  • Three Licensors involved, as follows:
    • Axens (CCR)
    • Exxonmobil (APS)
    • MW Kellogg (LVN and Crude Light Ends)

+++ Refining Units

  • Continuous catalytic reformer - 15,000 bpd
  • Naphtha hydrofiner - Revamp
  • Atmospheric distillation Unit - Modification

+++ Terminal Capacity

  • Crude Oil:
  • Refined Products:

+++ Crude Supply

  • Flexibility of crude supply will be increased


+++ Products Produced

  • Gasoline production will increase

+++ History

  • 2008 - Foster Wheeler awarded contract
  • 2011 - Upgrading project completed

+++ Other Information

  • -


+++ Relevant Links

  1. Investments in Low-Sulphur fuel production in Thessaloniki
  2. THESSALONIKI REFINERY UPGRADING PROJECT, Foster Wheeler
  3. Foster Wheeler Awarded Refinery Upgrading Contracts in Greece