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Biodegradation of catechol (2-hydroxy phenol) bearing wastewater in an UASB reactor
The present study deals with the biodegradation of catechol through co-metabolism with glucose in aqueous solution as primary substrate in an upflow anaerobic sludge blanket (UASB) reactor. Batch studies indicated that the 1000 mg l −1 glucose concentration was sufficient to cometabolize and degrade...
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Published in: | Chemosphere (Oxford) 2007-10, Vol.69 (5), p.816-824 |
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Main Authors: | , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | The present study deals with the biodegradation of catechol through co-metabolism with glucose in aqueous solution as primary substrate in an upflow anaerobic sludge blanket (UASB) reactor. Batch studies indicated that the 1000
mg
l
−1 glucose concentration was sufficient to cometabolize and degrade catechol in an aqueous solution up to a concentration of 1000
mg
l
−1. The reactor operated at 35
±
2
°C, and at a constant hydraulic retention time of 8
h with a gradual stepwise increase in catechol concentration from 100 to 1000
mg
l
−1 along with glucose as a cosubstrate. The results showed that the catechol was successfully mineralized in an UASB reactor in which microbial granulation was achieved with only glucose as the substrate. The reactor showed ⩾95% COD removal efficiency with 500–1000
mg
l
−1catechol concentration in the feed and a glucose concentration of 1500
mg
l
−1 as a cosubstrate. Similar efficiency was obtained at a constant catechol concentration of 1000
mg
l
−1 with 500–1000
mg
l
−1 glucose concentration. Once the reactor got acclimatized with catechol, higher concentrations of catechol can be mineralized with a minimum amount of glucose as the cosubstrate without affecting the performance of the UASB reactor. |
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ISSN: | 0045-6535 1879-1298 |
DOI: | 10.1016/j.chemosphere.2007.04.064 |