Difference between revisions of "Puerto Limon Refinery Project"
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Abarrelfull (talk | contribs) (Created page with "=== Summary Information === * Ownership: Recope * Website: http://www.recope.go.cr/ * Wiki Page: [[[Puerto Limon Refinery]]] * Location: Costa Rica * Capacity: * Before...") |
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* Ownership: Recope | * Ownership: Recope | ||
* Website: http://www.recope.go.cr/ | * Website: http://www.recope.go.cr/ | ||
| − | * Wiki Page: | + | * Wiki Page: [[Puerto Limon Refinery]] |
* Location: Costa Rica | * Location: Costa Rica | ||
* Capacity: | * Capacity: | ||
| − | + | ** Before: 1.25 million tons/annum & 25,000 bbl/day | |
| − | + | ** After: 3.0 million tons/annum & 60,000 bbl/day | |
* Nelson Complexity: | * Nelson Complexity: | ||
* Project Stage: FEED Awarded | * Project Stage: FEED Awarded | ||
| Line 55: | Line 55: | ||
* UOP has questioned the calculations of Huanqiu Contracting & Engineering Corp. (HQCEC) which did the initial design | * UOP has questioned the calculations of Huanqiu Contracting & Engineering Corp. (HQCEC) which did the initial design | ||
| − | * The China Development Bank will loan up to $900 million for the project | + | * The China Development Bank will loan up to $900 million for the project |
| − | |||
=== Links === | === Links === | ||
Latest revision as of 23:56, 24 October 2020
Summary Information
- Ownership: Recope
- Website: http://www.recope.go.cr/
- Wiki Page: Puerto Limon Refinery
- Location: Costa Rica
- Capacity:
- Before: 1.25 million tons/annum & 25,000 bbl/day
- After: 3.0 million tons/annum & 60,000 bbl/day
- Nelson Complexity:
- Project Stage: FEED Awarded
- Expected Completion: [[[Refinery Projects to be Completed in 2015 | 2015]]]
- Budget: between $ 800 and $ 1,000 million
+++ The Project
- Project Type: Expansion & Upgrading
- Project Summary: To expand existing refinery to process 60,000 BPSD
- Main Contractors:
* WorleyParsons: Project management team and front end engineering and design services
+++ Refining Units
- Atmospheric distillation unit - 40 000 BPSD
- Vacuum unit - 40 000 BPSD
- Hydrotreating units for gasoline from 10 000 to 12 000 BPSD
- Hydrotreating units for diesel from 15 000 to 20 000 BPSD
- Moderate cracking units - 16 000 BPSD
- Catalytic reforming unit 10 000 BPSD
- A possible solvent deasphalting drive.
- It is estimated that it will be necessary to make a revamping of the existing catalytic reformer to convert to a 1300 BPSD isomerizer
- Extension may also require revamping the current Kerosene Hydrotreater 2400 BPSD process.
+++ Terminal Capacity
- Crude Oil:
- Refined Products:
+++ Crude Supply
- -
+++ Products Produced
- LPG, Gasoline, Jet Fuel, Diesel, Coke
+++ History
- 2009 - CNPC and RECOPE sign a supplementary agreement for the project
- 2011 - UOP published feasibility study
- 2011 - Worleyparsons awarded PMC & FEED Contract
- 2011 - the China Development Bank agree to provide finance for the project
+++ Other Information
- UOP has questioned the calculations of Huanqiu Contracting & Engineering Corp. (HQCEC) which did the initial design
- The China Development Bank will loan up to $900 million for the project
