Removal of chlorophenols in sequential anaerobic-aerobic reactors.
Combination of upflow anaerobic sludge blanket (UASB) and aerobic rotating biological contactor (RBC) reactors having higher biomass concentration and higher sludge retention time (SRT) was applied for the sequential treatment of priority pollutant chlorophenol containing wastewater. Target compounds 2-chlorophenol (2-CP) and 2,4-dichlorophenol (2,4-DCP) present in two simulated wastewaters at a concentration of 30 mg/l each individually were sequentially treated in continuous mode by combined UASB-I, RBC-I and combined UASB-II, RBC-II reactors, respectively after the acclimation of their biomass with the corresponding chlorophenol. Reactor combinations took 190 and 215 days for acclimation with 30 mg/l of 2-CP and 2,4-DCP respectively. Hydraulic retention time (HRT) studies showed that 12h HRT of UASB-I and 23 h HRT of RBC-I as well as 12h HRT of UASB-II and 28.8h HRT of RBC-II were the optimum combinations for the treatment of simulated wastewater containing 2-CP and 2,4-DCP respectively. Optimum HRT combinations produced 2-CP and 2,4-DCP effluent having corresponding chlorophenol concentration of below detectable limit (BDL) and 0.1 mg/l respectively. Half velocity coefficients (Ks) for 2-CP and 2,4-DCP biodegradation in UASB reactors were determined to be 5.07 mg 2-CP/l and 6.49 mg 2,4-DCP/l. Optimum ratio of substrate (chlorophenol): co-substrate (sodium acetate) was 1:100.
Majumder
Partha Sarathi
PS
Centre for Environmental Science and Engineering, Indian Institute of Technology, Powai, Mumbai 400 076, India.
Gupta
S K
SK
D000332:Aerobiosis; D000693:Anaerobiosis; D018441:Biofilms; D019149:Bioreactors; D002733:Chlorophenols / Q000737:chemistry*; D013997:Time Factors; D014865:Waste Disposal, Fluid / Q000379:methods
D002733:Chlorophenols; C030683:2-chlorophenol; C004762:2,4-dichlorophenol