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GUIDELINES FOR AVOIDING SULFIDATION (SULFIDIC) CORROSION FAILURES IN OIL REFINERIES
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Available format(s): Hardcopy, PDF
Superseded date: 16-01-2019
Language(s): English
Published date: 01-01-2009
Publisher: American Petroleum Institute
Introduction1 Scope2 Normative References3 Definitions and Acronyms 3.1 Definitions 3.2 Acronyms4 Basics of Sulfidation Corrosion5 Location of Sulfidation Corrosion6 Effects of Process and Material Variables on Corrosion Rates 6.1 Introduction 6.2 H[2]-free Sulfidation 6.3 H[2]/H[2]S Corrosion7 Practical Guidelines for Avoiding Sulfidation Corrosion Failures 7.1 For Existing Units and Components 7.2 New and Replacement Components8 Limitations of Current Knowledge Base9 IncidentsAnnex A (informative) - Failure Experience SummaryAnnex B (informative) - Sulfidation Corrosion Prediction ToolsAnnex C (informative) - Corrosion Data for Carbon Steel Piping with Higher and Lower Si ContentsBibliography
Applies to hydrocarbon process streams containing sulfur compounds, with and without the presence of hydrogen, which operate at temperatures above approximately 450 degrees F (230 degrees C) up to about 1000 degrees F (540 degrees C).
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