gearteeth
Materials
- Jul 24, 2014
- 17
I have some atmospheric storage tanks constructed of solid 316L stainless steel, that contain spent caustic produced as a by-product of refinery processes. They operate at ambient temperatures, 100F is the hottest temperature seen by temperature indicators. pH is in the range of 13-13.5. Sampling shows chloride concentrations to be around ~1000 ppm as measured by chlora analyzer following a recent process change. O2 ingress into the tank is a given, no nitrogen blanket. H2S is present as well.
I’m concerned about the potential for chloride stress corrosion cracking. Industry documentation reports that temperature and pH are in our favor, but both come with caveats. There have been instances of cracking below 140F, and even though the bulk environment is alkaline, local environments may be different particularly within equipment as large as a tank.
I’ve been reading MTI publication on SCC, Nickel institute document on material selection for caustic service, and API publications. Is there anything out there that can help me better understand our risk? Any inspection recommendations?
I’m concerned about the potential for chloride stress corrosion cracking. Industry documentation reports that temperature and pH are in our favor, but both come with caveats. There have been instances of cracking below 140F, and even though the bulk environment is alkaline, local environments may be different particularly within equipment as large as a tank.
I’ve been reading MTI publication on SCC, Nickel institute document on material selection for caustic service, and API publications. Is there anything out there that can help me better understand our risk? Any inspection recommendations?