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Velkommen til Kalundborg Raffinaderiet

Velkommen til Kalundborg Raffinaderiet. Indhold. Formål med raffinering Principper i raffinering Råoliens vej igennem raffinaderiet Benzin blanding Gasolie blanding Om destillationsprocessen Proceskontrol af destillationskolonne Avanceret proceskontrol af destillationskolonne

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Velkommen til Kalundborg Raffinaderiet

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  1. Velkommen til Kalundborg Raffinaderiet

  2. Indhold • Formål med raffinering • Principper i raffinering • Råoliens vej igennem raffinaderiet • Benzin blanding • Gasolie blanding • Om destillationsprocessen • Proceskontrol af destillationskolonne • Avanceret proceskontrol af destillationskolonne • Raffinaderi udfordringer

  3. Formål med raffinering Propan Benzin Jetfuel Diesel Råolie/ Kondensat Fyringsgasolie Brændselsolie

  4. Principper i raffinering Råolie/ Kondensat Raffinaderi processer Raffinaderi processer Hjælpemidler -Adskillelse - Oprensning - Kemisk omdannelse - Varme - Tryk - Katalysator - Additiver Produkter

  5. Råoliens vej igennem raffinaderiet

  6. LPG

  7. Benzin

  8. Jet Fuel

  9. Diesel

  10. Fyringsgasolie

  11. Atmosfærisk residue

  12. Vacuum destillation

  13. Krakning

  14. Krakning

  15. Råoliens vej igennem raffinaderiet

  16. Kalundborg refinery process flow overview

  17. Benzinbland

  18. Benzinbland

  19. Gasolieblanding Fraktionering Afsvovlings- reaktorer Inline blending Kvalitets-kontrol Færdigprodukt tanke

  20. Gasolieblanding GORTO: Kalundborg Gas Oil RTO/MPC RTO: Real Tids Optimering MPC: Multivariabel Predictive Control

  21. Om destillationsprocessen

  22. Om destillationsprocessen

  23. Om destillationsprocessen

  24. Proceskontrol af destillationskolonne

  25. Avanceret proceskontrol af destillationskolonne

  26. Notation: Running Application Implementation ongoing Future Application Sec. 700 Gas Plant 10-15 m3/hr Sec. 200/250 Light Ends Fractionation 80-120 m3/hr Overhead LVN Sec. 300/400 HT/ Reforming 45-60 m3/hr HVN Gas & LPG Naphtha to Light Ends HT & Fractionation Sec. 200 Atmospheric Distillation 370-480 m3/hr Kero 60 m3/hr Sec. 550 Jet Fuel Plant 15-40 m3/hr Naphtha C-201 Sec. 850 Kero/ Gasoil HT 40-90 m3/hr Kero/ Gasoil Hydrotereating LGO 80-110 m3/hr Gasoline HVBN HGO 25 m3/hr Sec. 800 Gasoil HT 65-130 m3/hr Crude oil To Gasoil HT & HDA Jet Fuel LVGO 10-20 m3/hr Sec. 1000 Vac. Distil. 140-200 m3/hr VB Naphtha LVBN VBGO Sec. 600 Tar Gas HVGO 90-120 m3/hr ThermoCracking 90-115 m3/hr Fractionation Storage and Blending Visbreaking 60-80 m3/hr Diesel Vac. Btm. 70 m3/hr Sec. 4700 Gas Plant 16-24 m3/hr Gas Plant Light Ends HT & Fractionation 220 m3/hr Overhead Sec. 4600 Isomerisation 95 m3/hr Gasoil Sec. 4200 Atmospheric Distillation 230-280 m3/hr Sec. 4400 Reforming 105 m3/hr Light Kero 6-20 m3/hr To Kero/ Gasoil Hydrotreating C-4201 HFO ULGO 51 m3/hr Sec. 4800 Gasoil HT 145 m3/hr Condensate/ crude oil LAGO 10-25 m3/hr To Vacuum Distillation

  27. Kalundborg MPC implementations

  28. Raffinaderi udfordringer • At levere de rigtige produkter • i de rigtige mængder • til den rigtige tid • og til den rigtige pris. • Indsats områder: • Sikkerhed • Miljø • Raffinaderi økonomi • Produkt kvalitet • Driftspålidelighed • Teknologi-udvikling

  29. Spørgsmål? Introduktion til Kalundborg raffinaderiet Anne-Katrine Ipsen Proces Control Advisor d01ai@statoil.com, tel: +45 59 57 45 30 www.statoil.com

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