InfocusPaul
Industrial
- Jan 23, 2007
- 1
Hello forum,
I'm involved with a couple of large independent storage terminals (liquid hydrocarbons for the most) over here in Europe as an API 570/653 inspector. The terminals are tanker offload facilities, and the owners are trying to put together a responsible piping inspection program based around API/ASME, but have very little construction/maintenance history (>40 yr old facilities).
Does any body out there have experience of a similar situation. We would like to make some design checks for tmin and also future operating pressures, but we are not sure whether the piping should be accepted under B31.3 or B31.4 scope. I'm aware this will be the owners decision but it would be good to hear advice from the experts, as I'm sure you all realise the different stress values, weld efficiency etc involved. I would like to try and assist to get a balance of safety but not over cautious and call unnecessary repairs.
Thanks in advance.
I'm involved with a couple of large independent storage terminals (liquid hydrocarbons for the most) over here in Europe as an API 570/653 inspector. The terminals are tanker offload facilities, and the owners are trying to put together a responsible piping inspection program based around API/ASME, but have very little construction/maintenance history (>40 yr old facilities).
Does any body out there have experience of a similar situation. We would like to make some design checks for tmin and also future operating pressures, but we are not sure whether the piping should be accepted under B31.3 or B31.4 scope. I'm aware this will be the owners decision but it would be good to hear advice from the experts, as I'm sure you all realise the different stress values, weld efficiency etc involved. I would like to try and assist to get a balance of safety but not over cautious and call unnecessary repairs.
Thanks in advance.