We are designing an Odor control system for a lift station, volume is roughly 1,125 m3.
The sanitary sewage will have anaerobic condition for 5 days in LS. The normal design practice for OC is min 10 ppmv H2S in feed to the Activated carbon absorber.
Can anyone highlight will there be a surge in H2S concentration due to anaerobic condition, say for 5 days or more
If yes what will be the concentration or how this can be estimated