TECHNICAL PAPERS
Mar 1, 2005

Biotransformation of Carbon Tetrachloride and Anaerobic Granulation in a Upflow Anaerobic Sludge Blanket Reactor

Publication: Journal of Environmental Engineering
Volume 131, Issue 3

Abstract

Carbon tetrachloride (CT) in a synthetic wastewater was effectively degraded in a 2l upflow anaerobic sludge blanket reactor during the granulation process by increasing the chemical oxygen demand (COD) and CT loadings. The effect of operational parameters such as influent CT concentrations, COD, CT loading, food to mass (F/M) ratio, and specific methanogenic activity (SMA) were also detected during granulation. Over 97% of CT was removed at 37°C , at a COD loading rate of 10gLday . Chemical oxygen demand and CT removal efficiencies of 92 and 88% were achieved when the reactor was operating at CT and COD loading rates of 17.5mgLday and 12.5gLday , respectively. This corresponds to an hydraulic retention time of 0.28day and an F/M ratio of 0.57gCODgvolatilesuspendedsolids(VSS)day . In 4weeks , the seed sludge developed the CT degrading capability that was not very sensitive to shocks. The granular sludge cultivated had a maximum diameter of 2.5mm and SMA of 1.64gCODgVSSday . Glucose biodegradation by CT acclimated anaerobic granules was expressed with competitive inhibition. However the competitive inhibition was not significant since the competitive inhibition coefficient (Ki) was as high as 18.72mgL . Kinetic coefficients of k (maximum specific substrate utilization rate), Ks (half velocity coefficient), Y (growth yield coefficient), and b (decay coefficient) were determined as 0.6day , 1.1mgL , 0.23gVSSg glucose-COD, and 0.01day , respectively, based on growth substrate glucose–COD during CT biotransformation. The CT was treated via biodegradation and this contributed to 89% of the total removal. The removal contributions from biomass adsorption, abiotic transformation, and volatilization were negligible. Adsorption and volatilization accounted for only 0.8 and 0.5% of the total removal, respectively.

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Acknowledgments

The writer would like to express her thanks to TÜBİTAK (The Turkish Scientific and Technical Research Council) for financial support under Grant No. YDABÇAG-485 and to Dokuz Eylül University Support Foundation, Grant No. 0908.97.02.03.

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Go to Journal of Environmental Engineering
Journal of Environmental Engineering
Volume 131Issue 3March 2005
Pages: 425 - 433

History

Received: Mar 20, 2001
Accepted: Apr 13, 2004
Published online: Mar 1, 2005
Published in print: Mar 2005

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Delia Teresa Sponza [email protected]
Professor, PhD, Engineering Faculty, Environmental Engineering Dept., Dokuz Eylül Univ., Buca Kaynaklar Campus, İzmir, Turkey. E-mail: [email protected]

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