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API RP 939-C

API RP 939-C, 2nd Edition: Guidelines for Avoiding Sulfidation (Sulfidic) Corrosion Failures in Oil Refineries

CDN $310.00

This publication was last reviewed and confirmed in 2024.

Guidelines for Avoiding Sulfidation (Sulfidic) Corrosion Failures in Oil Refineries

SKU: 8a861522c127 Category:

Description

This recommended practice (RP) is applicable to hydrocarbon process streams with sulfur-containing compounds, without the presence of hydrogen, which operate at temperatures above approximately 500 °F (260 °C) up to about 1000 °F (540 °C). There is considerable debate in the industry as to the correct threshold temperature for hydrogen free sulfidation and in a change in this Edition, the API 571 threshold of 500 °F (260 °C) is adopted herein. Experience has shown that little significant corrosion will occur at operating temperatures below 500 °F (260 °C) for hydrogen free sulfidation services without the influence of naphthenic acid corrosion. Mercaptan corrosion, particularly in condensate service, has been reported below this temperature, but is not explicitly covered in the 2nd Edition of RP 939-C. For hydrogen containing services, the threshold temperature is set at 450 °F (230 °C). A lower threshold limit for sulfur content is not provided because significant corrosion has occu

Edition

2

Published Date

2019-01-10

Status

Current

Pages

59

Language Detail Icon

English

Format Secure Icon

Secure PDF

Abstract

This recommended practice (RP) is applicable to hydrocarbon process streams with sulfur-containing compounds, without the presence of hydrogen, which operate at temperatures above approximately 500 °F (260 °C) up to about 1000 °F (540 °C). There is considerable debate in the industry as to the correct threshold temperature for hydrogen free sulfidation and in a change in this Edition, the API 571 threshold of 500 °F (260 °C) is adopted herein. Experience has shown that little significant corrosion will occur at operating temperatures below 500 °F (260 °C) for hydrogen free sulfidation services without the influence of naphthenic acid corrosion. Mercaptan corrosion, particularly in condensate service, has been reported below this temperature, but is not explicitly covered in the 2nd Edition of RP 939-C. For hydrogen containing services, the threshold temperature is set at 450 °F (230 °C). A lower threshold limit for sulfur content is not provided because significant corrosion has occu

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