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Bioresour Technol ; 148: 334-42, 2013 Nov.
Article in English | MEDLINE | ID: mdl-24061065

ABSTRACT

In the present study, the feasibility of a bioengineered two-stages sequential batch reactor (BTSSBR) followed by filtration-adsorption process was investigated to treat the agrochemical effluent by overcoming factor affecting process stability such as microbial imbalance and substrate sensitivity. An air stripper stripped 90% of toxic ammonia, and combined with other streams for bio-oxidation and filtration-adsorption. The BTSSBR system achieved bio-oxidation at 6 days hydraulic retention time by fending off microbial imbalance and substrate sensitivity. The maximum reduction in COD and BOD by heterotrophic bacteria in the first reactor was 87% and 90%, respectively. Removal of toxic ammoniacal-nitrogen by autotrophic bacteria in a post-second stage bio-oxidation was 97%. The optimum filtration and adsorption of pollutants were achieved at a filtration rate of 10 and 9 m(3)m(-2)h(-1), respectively. The treatment scheme comprising air stripper, BTSSBR and filtration-adsorption process showed a great promise for treating the agrochemical effluent.


Subject(s)
Agriculture , Batch Cell Culture Techniques/instrumentation , Bioengineering/instrumentation , Bioreactors , Waste Disposal, Fluid , Adsorption , Air , Ammonia/isolation & purification , Biodegradation, Environmental , Biological Oxygen Demand Analysis , Chemical Phenomena , Feasibility Studies , Filtration , Oxidation-Reduction , Reference Standards , Time Factors , Water Purification
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