Abstract
Treatment of a mixture of NH3, H2S, and ethylmercaptan (EM) was investigated for more than 15 months in two biotrickling filters packed with poplar wood chips and polyurethane foam. Inlet loads ranging from 5 to 10 g N-NH3 m(3) hr(1), from 5 to 16 g S-H2S m(3) hr(1), and from 0 to 5 g EM m(3) hr(1) were applied. During startup, the biotrickling filter packed with polyurethane foam was re-inoculated due to reduced biomass retention as well as a stronger effect of nitrogen compounds inhibition compared with the biotrickling filter packed with poplar wood. Accurate pH control between 7 and 7.5 favored pollutants abatement. In the long run, complete NH3 removal in the gas phase was achieved in both reactors, while H2S removal efficiencies exceeded 90%. EM abatement was significantly different in both reactors. A systematically lower elimination capacity was found in the polyurethane foam bioreactor. N fractions in the liquid phase proved that high nitrification rates were reached throughout steady-state operation in both bioreactors. CO2 production showed the extent of the organic packing material degradation, which allowed estimating its service lifetime in around 2 years. In the long run, the bioreactor packed with the organic packing material had a lower stability. However, an economic analysis indicated that poplar wood chips are a competitive alternative to inorganic packing materials in biotrickling filters.
Original language | English |
---|---|
Pages (from-to) | 462-471 |
Number of pages | 10 |
Journal | Journal of the Air and Waste Management Association |
Volume | 63 |
Issue number | 4 |
DOIs | |
Publication status | Published - 1 Apr 2013 |
Keywords
- HYDROGEN-SULFIDE
- AMMONIA REMOVAL
- BIOFILTRATION
- BIOFILTER
- GASES
- AIR
- BEHAVIOR
- SYSTEM
- STATE