The enzyme-accelerated biodegradation of total petroleum hydrocarbons (TPH) was investigated in a sequencing continuous-inflow reactor (SCR) at different operational parameters of H2O2/TPH ratio, initial TPH concentration and hydraulic retention time (HRT). The optimum H2O2/TPH mass ratio was determined to be 0.35 at which the complete TPH removal of inlet TPH concentrations up to 4g/L at HRT of 24h, corresponding to the loading rate of 4kgTPH/m3.d, was attained. The average COD removal efficiency at this loading rate was 96.7%. With increasing the inlet TPH concentration from 1 to 2.5g/L, the biomass bacterial activity as dehydrogenase activity (DHA) increased from 7.5 to 27.1μgTF/gbiomass.d and remained almost unchanged with further increase of TPH concentration. The peroxidase activity (PA) remained high between 382 and 410U/gbiomass. In addition, the complete removal of 1g/L TPH (88.7% COD removal) was observed at HRT of as small as 4h (corresponding to the loading rate of 6kgTPH/m3.d) under optimum H2O2/TPH mass ratio. With the decrease of HRT from 24h to 4h at the constant TPH concentration of 1g/L the value of DHA remained between 24.4 and 28.4μgTF/gbiomass.d while the PA value increased from 287.9 to 394.4U/gbiomass. Total production of biosurfactants was 131mg/L (38mg/L rhamnolipid and 93mg/L surfactin) when the SCR was operated at TPH loading rate of 6kg/m3.d.Finally, the enhanced enzymatic biodegradation of TPH by using diverse microbial consortia capable of in-situ production of peroxidase and biosurfactant generation in the SCR is a very efficient and promising technique for accelerated biodegradation and COD removal of petroleum hydrocarbons.
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