Canadian Athabasca oilsand bitumen crudes, characterized as corrosive by the classical naphthenic model, are producing negligible naphthenic acid corrosion in crude and vacuum units after more than 50 years of cumulative operation. A new theory proposes that the corrosivity of naphthenic acids in Athabasca oilsand bitumen crudes is a function of its molecular weight, molecular structure, true boiling point, reactive sulfidic species, and local environment. The concept of α (bad type) and β (good type) naphthenic acids is introduced. The α naphthenic acids are characterized as corrosive, with low molecular weights, and β as non-corrosive and inhibitive, with high molecular weights. Hot extraction wash of the raw oil sand mixture appears to preferentially remove the higher water-soluble α fraction leaving the less corrosive, less water-soluble, β fraction. Naphthenic acid surviving after thermal hydroprocessing tends to be of the inhibitive β type. Case histories, material selection, and corrosion reduction possibilities with opportunity crudes are discussed.

Subject
Sulfur, Steel structures, Acid inhibitors, Crude oil inhibition, Naphthenic acid, Corrosivity, Asphalt, Acid attack, Molecular weight, Refineries, Molecular structure, Corrosion modeling, Crude
Keywords:
Naphthenic acid, TAN, naphthenic acid corrosion (NAC), oilsand bitumen crude, opportunity crude, alpha, beta, reactive sulfur
© 2004 Association for Materials Protection and Performance (AMPP). All rights reserved. No part of this publication may be reproduced, stored in a retrieval system, or transmitted, in any form or by any means (electronic, mechanical, photocopying, recording, or otherwise) without the prior written permission of AMPP. Positions and opinions advanced in this work are those of the author(s) and not necessarily those of AMPP. Responsibility for the content of the work lies solely with the author(s).
2004
Association for Materials Protection and Performance (AMPP)
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