Difference between revisions of "Thai Oil Sriracha Refinery"

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* Ownership: Thai Oil
 
* Ownership: Thai Oil
 
* Website: http://www.thaioilgroup.com/th/
 
* Website: http://www.thaioilgroup.com/th/
Location: Sriracha, Thailand
+
* Location: Sriracha, Thailand
Capacity: 13.35 million tons/annum & 275,000 bbl/day
+
* Capacity: 13.35 million tons/annum & 275,000 bbl/day
Nelson Complexity: 9.8
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* Nelson Complexity: 9.8
Refining Depth:
+
* Refining Depth:
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
Fluidised Catalytic Cracker
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* Fluidised Catalytic Cracker
Hydrocracker
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* Hydrocracker
CCR Reformer
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* CCR Reformer
Isomerisation Unit
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* Isomerisation Unit
Desulphurisation
+
* Desulphurisation
Naphtha
+
** Naphtha
Kerosene
+
** Kerosene
Diesel
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** Diesel
Visbreaker
+
* Visbreaker
Terminal Capacity
+
 
Crude Oil:
+
=== Terminal Capacity ===
Refined Products:
+
* Crude Oil:
Crude Supply
+
* Refined Products:
Crude is unloaded from VLCC size tankers using an SPM Buoy system installed in a water depth of approximately 30 metres.
+
=== Crude Supply ===
Products Produced
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* Crude is unloaded from VLCC size tankers using an SPM Buoy system installed in a water depth of approximately 30 metres.
Gasoline, Diesel, Jet Fuel, LPG
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=== Products Produced ===
Ongoing Projects
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* Gasoline, Diesel, Jet Fuel, LPG
The refinery is being expanded and upgraded, in the [[Sriracha Refinery Expansion Project]]
+
=== Projects ===
The project will increase daily crude throughput from 275,000 barrels to 400,000 barrels
+
* The refinery is being expanded and upgraded, in the [[Sriracha Refinery Expansion Project]]
A previous upgrade was the Thai Oil Sriracha Refinery Project
+
* The project will increase daily crude throughput from 275,000 barrels to 400,000 barrels
Other Information
+
* A previous upgrade was the [[Thai Oil Sriracha Refinery Project]]
 +
=== Other Information ===
 
-
 
-
History
+
=== History ===
1961 - Refinery commissioned with 35,000 bpd capacity
+
* 1961 - Refinery commissioned with 35,000 bpd capacity
1989 - Column revamped from 30,000 to 43,000 bpd and hydrocracker commssioned
+
* 1989 - Column revamped from 30,000 to 43,000 bpd and hydrocracker commssioned
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
 +
 
 
=== Links ===
 
=== Links ===
 
# [[Chiyoda Crude Distillation Units]]
 
# [[Chiyoda Crude Distillation Units]]

Latest revision as of 18:18, 8 April 2020

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

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

  1. Chiyoda Crude Distillation Units
  2. Chiyoda Thermal Cracking Units
  3. Chiyoda Sweetening Units
  4. Chiyoda Vacuum Flasher Vacuum Distillation Units
  5. Chiyoda Catalytic Reforming Units
  6. Chiyoda Sour Water Stripping Units
  7. Chiyoda Hydrogen Manufacturing Units
  8. Chiyoda Naphtha And Middle Distillate Hydrodesulfurization U
  9. Chiyoda H2S Removal Units With Amine
  10. Bluewater Calm Buoy Mooring References
  11. Refinery Web Page
  12. ABB wins major contract for Thai Oil refinery
  13. Saipem wins four new contracts worth $550 million in Angola, Mexico, Thailand and Saudi Arabia
  14. Saipem awards SPM contract to Bluewater