2.4. Treatment performance
The influent to the biological compartment of the Alto Seveso
WWTP, after preliminary treatments to remove grit, sand and
coarse material, was used in our tests. The experimental
SBBGR campaign lasted 200 days. During the first 3 months of
the experimentation particular attention was paid to the
generation of the particular biomass of SBBGR (i.e., a mixture
of biofilm and granules packed in the filling material) by
operating with a high value of hydraulic retention time (HRT),
i.e. 25e30 h, and 8 h-treatment cycles. Thanks to the design of
the reactor, granulation is simply achieved using such a slow
increasing step-feed approach: more details about the startup
of an SBBGR can be found in De Sanctis et al. (2010). Afterwards,
in order to evaluate the maximum treatment
capability of the system, the HRT was progressively reduced
down to 11 h and the OLR increased up to 2 kgCOD/m3 d by
increasing the wastewater volume fed to plant and reducing
the duration of the cycle from 8 to 6 h. During this final
experimental period, feeding, reaction phase and drawing
lasted 15, 330 and 15 min, respectively.
Treatment performance was evaluated by measuring
several parameters of influent and effluent, two or three times
2.4. Treatment performanceThe influent to the biological compartment of the Alto SevesoWWTP, after preliminary treatments to remove grit, sand andcoarse material, was used in our tests. The experimentalSBBGR campaign lasted 200 days. During the first 3 months ofthe experimentation particular attention was paid to thegeneration of the particular biomass of SBBGR (i.e., a mixtureof biofilm and granules packed in the filling material) byoperating with a high value of hydraulic retention time (HRT),i.e. 25e30 h, and 8 h-treatment cycles. Thanks to the design ofthe reactor, granulation is simply achieved using such a slowincreasing step-feed approach: more details about the startupof an SBBGR can be found in De Sanctis et al. (2010). Afterwards,in order to evaluate the maximum treatmentcapability of the system, the HRT was progressively reduceddown to 11 h and the OLR increased up to 2 kgCOD/m3 d byincreasing the wastewater volume fed to plant and reducingthe duration of the cycle from 8 to 6 h. During this finalexperimental period, feeding, reaction phase and drawinglasted 15, 330 and 15 min, respectively.Treatment performance was evaluated by measuringseveral parameters of influent and effluent, two or three times
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