In this paper, chemical reaction engineering models that incorporate mass transfer and kinetics are used to analyze corrosion inhibitor performance in different apparatus in the laboratory and field. The different models will be compared with the view of developing a set of transferable parameters that are apparatus independent. Equations that govern both adsorption of inhibitor to the surface with the build up of a porous corrosion product layer are developed.

Subject
Inhibitor performance, Corrosion rate, Adsorption, Adsorption isotherms, Corrosion reactions, Partial pressures, Corrosion products, Mass transfer, Experimental data, Corrosion inhibitors, Brines, Carbon dioxide, Oil
Keywords:
kinetics, adsorption, carbon dioxide, corrosion inhibition, ferrous carbonate, corrosion product layer
© 2001 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).
2001
Association for Materials Protection and Performance (AMPP)
You do not currently have access to this content.