moltenmetal
Chemical
- Jun 5, 2003
- 5,504
We have a small non-fired (electric) high pressure (2000 psig operating) continuous process steam generator in our scope on a particular project. The vessel will be ASME VIII-1 and the steam piping will be to B31.3. Both are carbon steels or low alloys.
The steam generator feed will be boiler feed quality and deoxygenated water. We're not sure what, if any, corrosion inhibitor chemicals will be added. The steam is directly used in their process, so inhibitors will be chosen with this in mind.
I've done a bit of searching and know there are stipulations in ASME I and in B31.1 which prohibit the use of stainless steels in these services, presumably over fears of SCC. I'm wondering just how much these rules are extended in practice to instrumentation which serves as part of the pressure boundary, i.e. control valves, level instruments, instrument impulse lines etc. The challenge is that at this scale, many of the preferred instruments are not readily available in carbon steel.
Is the prohibition absolute in practice, and applied to all pressure-retaining components including instruments and valves? Or can stainless steel components be used with periodic inspection and replacement? This plant will not operate continuously and there will be plenty of downtime to permit this, and plenty of process-related reasons to do the PM already.
The steam generator feed will be boiler feed quality and deoxygenated water. We're not sure what, if any, corrosion inhibitor chemicals will be added. The steam is directly used in their process, so inhibitors will be chosen with this in mind.
I've done a bit of searching and know there are stipulations in ASME I and in B31.1 which prohibit the use of stainless steels in these services, presumably over fears of SCC. I'm wondering just how much these rules are extended in practice to instrumentation which serves as part of the pressure boundary, i.e. control valves, level instruments, instrument impulse lines etc. The challenge is that at this scale, many of the preferred instruments are not readily available in carbon steel.
Is the prohibition absolute in practice, and applied to all pressure-retaining components including instruments and valves? Or can stainless steel components be used with periodic inspection and replacement? This plant will not operate continuously and there will be plenty of downtime to permit this, and plenty of process-related reasons to do the PM already.