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Biodegradation of 2,4-dichlorophenol in Packed-Bed Biofilm Reactor: Effect of Hydraulic Retention Time, Biogenic Substrate, and Loading Rate
被引:3
作者:
Patel, Bhishma P.
[1
]
Kumar, Arvind
[1
]
机构:
[1] Natl Inst Technol, Dept Chem Engn, Environm Pollut Abatement Lab, Rourkela 769008, Odisha, India
关键词:
packed bed reactor;
biofilm;
2,4-dichlorophenol;
biodegradation;
hydraulic retention time;
wastewater;
MICROBIAL-DEGRADATION;
LOOP BIOREACTOR;
UASB-REACTOR;
PHENOL;
SLUDGE;
PENTACHLOROPHENOL;
CHLOROPHENOLS;
PERFORMANCE;
KINETICS;
MIXTURES;
D O I:
10.2175/106143016X14733681695726
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
The removal of 2,4-dichlorophenol (2,4-DCP) by a pure culture of Bacillus endophyticus strain immobilized on ceramic balls was studied in a packed bed biofilm reactor (PBBR). The biodegradation of 2,4-DCP was studied in fed-batch and continuous mode and the effect of different parameters such as hydraulic retention time (HRT), biogenetic substrate concentration, and loading rate on the removal of 2,4-DCP were evaluated. Field emission scanning electron microscope (FESEM) results established the biofilm formation on the ceramic beads. The maximum volumetric removal rate found to be 127.2 mg/L.d at loading rate of 172.8 mg/L.d with 73.6% degradation (12.5 hours of HRT, 90 mg/L of 2,4-DCP, 0.2 g/L of peptone). The bioreactor showed more than 98% removal of 2,4-DCP at loading rate of 115.2 mg/L.d at 12.5 hours of HRT and 0.2 g/L of peptone. Effect of peptone showed that lower peptone concentration increases the removal efficiency; however, some peptone is necessary to maintain the 2,4DCP removal efficiency.
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页码:2191 / 2197
页数:7
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