This is an amazing thread, thank you all! A landfill gas pilot project has had two failures of a S/S bellows pump (the sales engineer has not been helpful in describing the composition of the stainless steel, other than to say it is not passivated). In one case corrosion appears to be the culprit. Hydrogen sulfide gas has been found at 25 ppm, which could be the main problem on corrosion. An in-line heat exchanger brings the relative humidity down prior to the bellows pump, but is only functional when operating, and there have been a number of start-stop cycles which might introduce condensation to the internals when cold. A critical meter is also S/S and may need protection, in addition to the new replacement bellows. I'd like to know whether passivation can be done after surface corrosion has already taken place, and whether it would be useful to pursue this approach.
Also, I am currently considering making an H2S gas removal subsystem, using DMEA, which seems better than NaOH for handling and overall effect on the S/S. Probably a small CCE packed-tower would handle it. Any thought or suggestions on this problem?