S.A. Lordo Nalco Company Richard Mathers Nalco Company, Ltd.

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1 Taking Some of the Challenge out of Challenge Crudes S.A. Lordo Nalco Company Richard Mathers Nalco Company, Ltd.

2 Topics What is a Challenge Crude? Assessment Methods Desalting Fouling Corrosion Summary

3 What is a Challenge Crude? Challenge or Opportunity crudes are any crude that is traded at a discount New crudes to market Crudes that are known to have processing problems Distressed cargoes Any crude that a refiner has not processed before

4 Assessment Methods Early assessment can reduce the risk in processing these crudes Several key aspects that are not on the assay How will it affect desalter operation? Will it cause fouling in exchangers and furnaces? Will it cause corrosion?

5 Will it Affect Desalter Operation? Several factors can impact desalting operation Viscosity Gravity Solids Content Asphaltene content / stability Conductivity Operational limitations (i.e., Temp, wash water, etc.) The key characteristic is the crude s emulsification tendency

6 Emulsification Characteristics Portable Electric Desalter (PED) can be used to bench test crudes Relative comparison between crudes and crude slates

7 % Water Separated PED Results Water Separation - Whole Crude No Demulsifier Forties Grane Harding Time (Mins) % Water Separated Whole Crude - With Demulsifier Forties 50 Harding Grane Time (Mins)

8 Crude Conductivity Conductivity increases with temperature and can reduce desalting electric field strength Blending is not predictable CONDUCTIVITY PICOSIMENS/METER TEMPERATURE o C 10% DOBA IN ARAB HVY DOBA ARAB HVY

9 Will it Cause Fouling in Exchangers and Furnaces? Primary fouling mechanism is asphaltene destabilization and precipitation Crude Compatibility Thermal Destabilization Some crudes exhibit other mechanisms Traditional organic polymerization

10 Crude Compatibility Mixing of crudes can result in asphaltene precipitation Nalco Fouling Potential Analyzer (FPA) Measures stability of crude oils and blends Differs from the blending indices Indicates desalter 12 impacts 11 Absorbance Crude A Crude B has higher stability than Crude Crude B Volume of Titrant

11 Asphaltene Dispersancy Test Determines the relative effectiveness of dispersing asphaltenes in nonsolvent medium Field test Aids in dispersant selection Discerns dispersant performance Blank Good Dispersion Poor Dispersion

12 Thermal Destabilization Asphaltene destabilization can be triggered by temperature Temperature decreases the resinasphaltene interaction

13 Hot Liquid Process Simulator Results Used to determine fouling potential of crudes and resids Used to select antifoulants and determine their effectiveness Rod Temp. Outlet Temp. (no Antifoulant) Outlet Temp. (with Antifoulant) Temperature (oc) T = -25 o C (130 min) Begin Antifoulant T = -2 o C (112 min) Time (min)

14 Will it Cause Corrosion? Majority of the challenge crudes on the market are high acid crudes Total acidity Naphthenic acid content Distribution of acids Other species are organic chlorides / undesaltable chlorides / phantom chlorides

15 High Temperature Naphthenic Acid Corrosion Not all TAN is a problem Measure of naphthenic acid content better gauge of corrosivity mg KOH / g Grana Crude - TAN / NAT Analysis TAN NAT Whole Crude C Temperature Range (oc)

16 Distribution of Acid Distribution can be used to determine likely areas of concern Some newer assays have this TAN data Nalco has a library of high acid crude nap acid distributions Relative comparison with respect to field experience

17 Corrosivity testing Laboratory rig used to simulate temperature and shear stress Test metallurgy of the unit Test inhibitor effectiveness Untreated Treated Corrosion Rate, MPY CS 5Cr 9Cr 410SS Test Sample

18 Experience Crudes that this process has been used successfully DOBA Grane CPC

19 Summary Processing opportunity crudes can significantly improve refinery profitability Testing can be done before the crude arrives to identify potential risks in desalting, fouling and corrosion Communication between buyers, refiners and crude process aid suppliers is key to successful introduction Planning ahead can allow the refiner to reduce unknown risks associated with running Challenge/Opportunity Crudes

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