Inspectioneering Journal

Combining NDE and Engineering Analysis to Optimize Tube Life in Steam Reformers

Part 2

By Richard D. Roberts at Quest Integrity Group, and John Brightling at Johnson Matthey Catalyst. This article appears in the November/December 2005 issue of Inspectioneering Journal.
This article is part 2 of a 2-part series.
Part 1Part 2


Part 1 in this 2 parts series laid the technical foundation for the methodology and technology. Part 2 will now demonstrate both through actual applications.

Case Study 1- Tunnel Port Effect

Correct sizing of tunnels and ports is essential to balance fluegas flows within the box.

Fluegas maldistribution will contribute to the variation in tube temperatures and lead to reduced furnace efficiency and limited firing rates. Also, in some circumstances, poor design of the tunnels and ports can have a much more dramatic effect; it can lead to premature tube failure. The failure is caused by localised creep damage at the bottom of the tubes and is shown schematically in Figure 6. The area of damage is typically 100 to 150 mm (4 to 6 inches) long, with the tube above and below the failure showing no damage.

Figure 6. Typical Furnace Tunnel Arrangement
Figure 6. Typical Furnace Tunnel Arrangement

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Posted by Udayan Patel on February 13, 2018
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