It is advisable to convert the TEMA type to NEU, as designing a flange connection for CEU/DEU types can be challenging, especially considering the need for mechanical cleaning. The shell side fluid can be switched to the tube side, and there are contractors capable of performing mechanical...
Try considering NEU type heat exchanger since you're using corrosion resistant alloy in the tubes and weld overlay on the base metal anyway. That would address a lot of your design issues. Do you need mechanical cleaning for the shell side?
With that pressure as well, it would be difficult...
Just ignore r6155. Apparently, he can't visualize your nozzle based on your description which is a very simple and common nozzle configuration.
@Vessel-SA, if you read ASME Companion Guide to BPVC, they explain the requirement for preheat and PWHT is a function of the thickness of the part...
You can modify the limits of reinforcement in PVElite.
However, if you have that kind of spacing, you'll still have to consider multiple openings and overlapping local stress due to piping external loads if applicable. You can increase the thickness of the shell course where the nozzle is...
I'm fairly certain majority of Owners/Contractors exclude austenitic SS bolts mainly due to Chloride SCC, galling, and it being an intermediate/low strength bolting for pressure retaining components such as flanges. If you're near the shore or the bolts being exposed to rainwater, that can cause...
The total sulfide species content in aqueous phase will need to be calculated to determine if you'll meet the threshold (see NACE MR0175 Part 2 Annex C).
I doubt anyone would adopt changing the dimensions of standard WN flanges (ASME B16.5 and B16.47) and also just minor adjustments on the hub dimensions.
It is implied already in other parts of the Code considering lamination concerns on plates. It is not due to the grain structure. Based on engineering judgment, Option 1 should be avoided.
Red line is lamination :