If you had high levels of H2S and COS, I'd consider a thermal oxidation of both (creating CO2, H2O, and SO2), followed by a scrubber (caustic-based for high removal rates), operated at 6-9 pH - above 9 pH, you'll tend to scrub CO2 as well). The low ppm amounts mean that running costs (combustion fuel and scrubber caustic) will be minimal. Look up DynaWave MECS for the capability to scrub/quench hot gases in one step.
I believe the above is what one of your consultants is leaning towards. This has a few cons, however.
- You'd be putting O2, N2 (if using air for combustion), and H2O into your gas stream due to combustion.
- The low ppm amounts, however, may mean that the initial capital cost may be too high to be attractive.
- Caustic scrubbing of SO2 will lead to Na2SO3, which will need to be oxidized in another step to Na2SO4 to prevent re-release of SO2 to atmosphere.
FYI, GATech90's suggestions of adsorption beds also require hydrolysis of the COS into H2S before adsorption per the manufacturers site. I'm unfamiliar with this technology, though.