Difference between revisions of "Tuapse Refinery Project"
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Abarrelfull (talk | contribs) (Created page with "Summary Information * Ownership: Rosneft * Website: http://www.rosneft.com/ * Wiki Page: [[[Tuapse Refinery]]] * Location: Tuapse, Black Sea * Capacity: * Before: 5 milli...") |
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* Ownership: Rosneft | * Ownership: Rosneft | ||
* Website: http://www.rosneft.com/ | * Website: http://www.rosneft.com/ | ||
− | * Wiki Page: | + | * Wiki Page: [[Tuapse Refinery]] |
* Location: Tuapse, Black Sea | * Location: Tuapse, Black Sea | ||
* Capacity: | * Capacity: | ||
− | + | ** Before: 5 million tons/annum & 100,000 bbl/day | |
− | + | ** After:12 million tons/annum & 240,000 bbl/day | |
* Nelson Complexity: 1,5 - 9,0 | * Nelson Complexity: 1,5 - 9,0 | ||
* Project Stage: | * Project Stage: | ||
Line 18: | Line 18: | ||
* Project Summary: | * Project Summary: | ||
* The project is being realised in three stages: | * The project is being realised in three stages: | ||
− | + | ** **Stage 1:** Atmospheric and vacuum distillation units and a naphtha hydrotreatment unit. This will increase the capacity but not the complexity | |
− | + | ** **Stage 2:** Conversion and specification units, enabling the refinery to produce Euro V fuels | |
− | + | ** **Stage 3:** Addition of the Flexicoking unit designed for deeper conversion of oil residues | |
* Main Contractors: | * Main Contractors: | ||
− | + | ** **Siemens:** gas turbine-generators | |
* Licences: | * Licences: | ||
− | + | ** **Chevron Lummus Global:** Hydrocracker and diesel hydrotreater license | |
− | + | ** **UOP:** isomerization and catalytic reforming of gasoline fractions | |
− | + | ** **Technip:** Hydrogen production unit | |
+++ Refining Units | +++ Refining Units |
Latest revision as of 09:25, 25 January 2024
Summary Information
- Ownership: Rosneft
- Website: http://www.rosneft.com/
- Wiki Page: Tuapse Refinery
- Location: Tuapse, Black Sea
- Capacity:
- Before: 5 million tons/annum & 100,000 bbl/day
- After:12 million tons/annum & 240,000 bbl/day
- Nelson Complexity: 1,5 - 9,0
- Project Stage:
- Expected Completion: [[[Refinery Projects to be Completed in 2013 | 2013]]]
- Budget:
+++ The Project
- Project Type: Upgrade & Expansion
- Project Summary:
- The project is being realised in three stages:
- **Stage 1:** Atmospheric and vacuum distillation units and a naphtha hydrotreatment unit. This will increase the capacity but not the complexity
- **Stage 2:** Conversion and specification units, enabling the refinery to produce Euro V fuels
- **Stage 3:** Addition of the Flexicoking unit designed for deeper conversion of oil residues
- Main Contractors:
- **Siemens:** gas turbine-generators
- Licences:
- **Chevron Lummus Global:** Hydrocracker and diesel hydrotreater license
- **UOP:** isomerization and catalytic reforming of gasoline fractions
- **Technip:** Hydrogen production unit
+++ Refining Units
- atmospheric distillation
- vacuum distillation units
- diesel fuel hydrotreatment,
- hydrocracking
- hydrogen production,
- naphtha isomerization,
- catalytic reforming,
- delayed coking,
- sulphur production
+++ Terminal Capacity
- Crude Oil:
- Refined Products:
+++ Crude Supply
- -
+++ Products Produced
- The products will be Euro V compliant
- Majority of the products will be exported
+++ History
- 2007 - Technip awarded contract for Hydrogen Unit
- 2008 - Rosneft and Vnesheconombank Sign Memorandum on Cooperation to finance the project
- 2009 - Siemens awarded contract to supply gas turbine-generators
- 2013 - Stage 1 of the project is completed
+++ Other Information
- -
+++ Relevant Links