Anup Sera
Mott MacDonald Group
GMT 10:28
20th May 2007
Please advice whether Sulfide Stress Cracking is a matter of concern in pipelines transporting Fuel Oils (500 cSt to 1000 cSt @ 50deg Cels)?
If yes, should the material selection be as per NACE MR0175/ISO 15156?
How can I estimate (approximate figure, as details are not available) the amount of Hydrogen Sulfide generated in Fuel Oils given the Sulphur content, water content and physical variables such as presure, temperature etc.?