My interpretation form nace is presenence of some sort of gas or vapor is necessery in a sour service to create the environment as described in nace. If the appliction for example is a liquid full vessel oil or water where under normao operating conditions no gas or vapor present, is this still...
How to determine that you have sour service or seever corrosive environment for a vessel, when the only thing you are provided with is co2 content of the vapor?
what are the implications of having a solid baffle partition in pressure vessel? how should I approach to design the baffle and what is max differential pressure i can design the baffle for to comply with ASME?
