Chemical Industry and Chemical Engineering Quarterly 2011 Volume 17, Issue 4, Pages: 517-524
https://doi.org/10.2298/CICEQ110428037B
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Recovery of UAPB from high organic load during startup for phenolic wastewater treatment
Bakhshi Zeinab (Babol Noshirvani University of Technology, Department of Civil Engineering, Babol, Iran)
Najafpour Ghasem (Babol Noshirvani University of Technology, Department of Chemical Engineering, Babol, Iran)
Navayi Neya Bahram (Babol Noshirvani University of Technology, Department of Civil Engineering, Babol, Iran)
Kariminezhad Esmaeel (Babol Noshirvani University of Technology, Department of Civil Engineering, Babol, Iran)
Pishgar Roya (Babol Noshirvani University of Technology, Department of Civil Engineering, Babol, Iran)
Moosavi Nafise (Babol Noshirvani University of Technology, Department of Civil Engineering, Babol, Iran)
Biodegradation of synthetic wastewater containing phenol by upflow anaerobic
packed bed reactor (UAPB) was studied in this work. The reactor was operated
at a hydraulic retention time (HRT) of 24 h and under mesophilic (30±1ºC)
conditions. The startup operation was conducted for 150 days; split into 4
phases. The phenol concentration was stepwise increased. The concentration of
phenol in phases 1, 2, 3 and 4 were 100, 400, 700 and 1000 mg/l,
respectively. In phase 1, the reactor reached steady state conditions on the
8th day with a phenol removal efficiency and biogas production rate of 96.8%
and 1.42 l/d, respectively. For an increase of the initial phenol
concentration in phase 2, a slight decrease in phenol removal efficiency was
observed. Similar trends were observed in phases 3 and 4 of startup. Due to
the high phenol concentration a sudden decrease in removal efficiency and
biogas production was observed. The surviving microorganisms were gradually
adapted and acclimated to high phenol concentrations. In phases 3 and 4, the
phenol removal efficiency at steady state conditions were 98.4 and 98%,
respectively. The maximum biogas production was observed at day 130 with a
value of 3.57 l/d that corresponds to phenol concentration of 1000 mg/l.
Keywords: phenol, upflow anaerobic packed bed, biogas, biodegradation, startup