Hi All,
All things being equal would the ID of a 316L SS Pipe corrode faster in theory if it were constantly full of fluid or drained between transfers? Seemed like a straightforward answer at first until I noticed posting with respect to corrosion rings in vessels at the junction of liquid to...
Does anyone know of an allowance in B31.3 that lets a Designer use actual Yield Stress values of material taken from the associated MTR rather than the values published in the strength tables?
We have a piping system that had to have extensive stress analysis done with a lot of manipulation of...
I'm currently trying to validate a Pressure Vessel for use as a blast containment vessel for tubes under reasonably high pressure and temperature (1885 psig @ 600°F) in an R&D test application. There is a fair amount of literature on equating the energy produced by a BLEVE (Boiling-Liquid...