Difference between revisions of "Thai Oil Sriracha Refinery"
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=== Brief Description === | === Brief Description === | ||
* A large high complexity refinery | * A large high complexity refinery | ||
− | Refining Units | + | === Refining Units == |
* Atmospheric Distillation | * Atmospheric Distillation | ||
* Vacuum Distillation Unit | * Vacuum Distillation Unit | ||
Line 20: | Line 20: | ||
** Diesel | ** Diesel | ||
* Visbreaker | * Visbreaker | ||
+ | |||
=== Terminal Capacity === | === Terminal Capacity === | ||
* Crude Oil: | * Crude Oil: | ||
Line 38: | Line 39: | ||
* 1993 - Capacity increased by 100,000 bpd | * 1993 - Capacity increased by 100,000 bpd | ||
* 1995 - Isomerisation unit commissioned | * 1995 - Isomerisation unit commissioned | ||
− | * Gasoil desulphurisation unit commissioned | + | * 1998 - Gasoil desulphurisation unit commissioned |
* 2005 - Saipem awarded contract for design, procurement, fabrication, installation and pre-commissioning of an unloading Single Point Mooring buoy and pipeline | * 2005 - Saipem awarded contract for design, procurement, fabrication, installation and pre-commissioning of an unloading Single Point Mooring buoy and pipeline | ||
* 2005 - ABB awarded contract to revamp CDU | * 2005 - ABB awarded contract to revamp CDU |
Latest revision as of 18:18, 8 April 2020
Contents
Summary Information
- Ownership: Thai Oil
- Website: http://www.thaioilgroup.com/th/
- Location: Sriracha, Thailand
- Capacity: 13.35 million tons/annum & 275,000 bbl/day
- Nelson Complexity: 9.8
- Refining Depth:
Brief Description
- A large high complexity refinery
= Refining Units
- Atmospheric Distillation
- Vacuum Distillation Unit
- Fluidised Catalytic Cracker
- Hydrocracker
- CCR Reformer
- Isomerisation Unit
- Desulphurisation
- Naphtha
- Kerosene
- Diesel
- Visbreaker
Terminal Capacity
- Crude Oil:
- Refined Products:
Crude Supply
- Crude is unloaded from VLCC size tankers using an SPM Buoy system installed in a water depth of approximately 30 metres.
Products Produced
- Gasoline, Diesel, Jet Fuel, LPG
Projects
- The refinery is being expanded and upgraded, in the Sriracha Refinery Expansion Project
- The project will increase daily crude throughput from 275,000 barrels to 400,000 barrels
- A previous upgrade was the Thai Oil Sriracha Refinery Project
Other Information
-
History
- 1961 - Refinery commissioned with 35,000 bpd capacity
- 1989 - Column revamped from 30,000 to 43,000 bpd and hydrocracker commssioned
- 1993 - Capacity increased by 100,000 bpd
- 1995 - Isomerisation unit commissioned
- 1998 - Gasoil desulphurisation unit commissioned
- 2005 - Saipem awarded contract for design, procurement, fabrication, installation and pre-commissioning of an unloading Single Point Mooring buoy and pipeline
- 2005 - ABB awarded contract to revamp CDU
Links
- Chiyoda Crude Distillation Units
- Chiyoda Thermal Cracking Units
- Chiyoda Sweetening Units
- Chiyoda Vacuum Flasher Vacuum Distillation Units
- Chiyoda Catalytic Reforming Units
- Chiyoda Sour Water Stripping Units
- Chiyoda Hydrogen Manufacturing Units
- Chiyoda Naphtha And Middle Distillate Hydrodesulfurization U
- Chiyoda H2S Removal Units With Amine
- Bluewater Calm Buoy Mooring References
- Refinery Web Page
- ABB wins major contract for Thai Oil refinery
- Saipem wins four new contracts worth $550 million in Angola, Mexico, Thailand and Saudi Arabia
- Saipem awards SPM contract to Bluewater