Menu
Search
Filters
Close
Menu

Save 20% on select titles with code HIDDEN24 - Shop The Sale Now

08173 Cavitation and Erosion Damage of Reboiler Stripper Tubes in Gas Manufacturing Industry

Picture for 08173 Cavitation and Erosion Damage of Reboiler Stripper Tubes in Gas Manufacturing Industry
Available for download

Two successive leakages were reported in the heat exchanger composed of 8 rows of finned tubes of the convection section of the condensate stripper re-boiler.  A comprehensive study (Failure Analysis) has been conducted to reveal the form of failure. The failure was recognized as erosion and cavitation damage.

Product Number: 51300-08173-SG
ISBN: 08173 2008 CP
Author: Hussein Rahmatalla, Mohammed Maqbool Ahmed, and Abdulla Radi Al-Hajri
Publication Date: 2008
Industry: Corrosion Monitoring and Control
$0.00
$20.00
$20.00

Two successive leakages were reported in the heat exchanger composed of 8 rows of finned tubes of the convection section of the condensate stripper re-boiler (U-H8300), the 3rd and the 4th rows used in Qatar. A comprehensive study (Failure Analysis) has been conducted to reveal the form of failure, by finding out the root cause of that failure, then suggest and implement the suggested practical solution. The failure was recognized as erosion and cavitation damage. All 8 rows of the re-boiler tubes, except the 1st and the 2nd rows, were made carbon steel as per ASTM 106 Grade B. The most severe working conditions were encountered in the early stages of the stripping process, i.e., in the 1st and 2nd rows, where the amount of the gas carried, temperature and pressure were higher. However no failure occurred in the tubes of the 1st and 2nd rows, simply because they are made from higher corrosion resistance alloys, AISI 316 stainless steel. Moreover, no failure has been yet reported in the 5th-8th row tubes. This was due to the working conditions were less severe in the 5th-8th row tubes, although they were made from same carbon steel (ASTM 106 Grade B).

Key Words: Cavitation corrosion, Erosion-corrosion, Re-boiler tube, Cavitation–erosion, ASTM steels, Failure analysis, Leakage, Heat exchanger

 

Two successive leakages were reported in the heat exchanger composed of 8 rows of finned tubes of the convection section of the condensate stripper re-boiler (U-H8300), the 3rd and the 4th rows used in Qatar. A comprehensive study (Failure Analysis) has been conducted to reveal the form of failure, by finding out the root cause of that failure, then suggest and implement the suggested practical solution. The failure was recognized as erosion and cavitation damage. All 8 rows of the re-boiler tubes, except the 1st and the 2nd rows, were made carbon steel as per ASTM 106 Grade B. The most severe working conditions were encountered in the early stages of the stripping process, i.e., in the 1st and 2nd rows, where the amount of the gas carried, temperature and pressure were higher. However no failure occurred in the tubes of the 1st and 2nd rows, simply because they are made from higher corrosion resistance alloys, AISI 316 stainless steel. Moreover, no failure has been yet reported in the 5th-8th row tubes. This was due to the working conditions were less severe in the 5th-8th row tubes, although they were made from same carbon steel (ASTM 106 Grade B).

Key Words: Cavitation corrosion, Erosion-corrosion, Re-boiler tube, Cavitation–erosion, ASTM steels, Failure analysis, Leakage, Heat exchanger

 

Product tags
Also Purchased
Picture for Corrosion Related Tube Failures in Amine Reboiler Units
Available for download

51313-02368-Corrosion Related Tube Failures in Amine Reboiler Units

Product Number: 51313-02368-SG
ISBN: 02368 2013 CP
Author: Janardhan Saithala
Publication Date: 2013
$20.00
Picture for Failure Analysis and Investigation Methods of Boiler Tubes Corrosion/Case Study
Available for download

51316-7188-Failure Analysis and Investigation Methods of Boiler Tubes Corrosion/Case Study

Product Number: 51316-7188-SG
ISBN: 7188 2016 CP
Author: hajatolah almasi
Publication Date: 2016
$20.00

The purpose of this study is to investigate the effect of amount of oxygen on corrosion rate of steam loop. Consequently, to eliminate failure, more effective steam quality monitoring concept is recommended.
Picture for 06458 UNDER-DEPOSIT CORROSION MECHANISMS IN
Available for download

06458 UNDER-DEPOSIT CORROSION MECHANISMS IN BOILERS

Product Number: 51300-06458-SG
ISBN: 06458 2006 CP
Author: A.G. Howell
$20.00

Under-deposit corrosion is a common mode of failure in boiler tubes. Mechanisms include phosphate attack, caustic gouging, hydrogen damage, and wall thinning due to metal loss. Many aspects of these mechanisms and their mitigation are well-understood, while certain specific details remain uncertain or subject to controversy.

 
Categories
Industry
Recently viewed
Popular tags
View all

Association for Materials Protection and Performance

© AMPP All Rights Reserved.
Membership Terms of Content Use
Contact Customer Support