Reaction kinetics and removal of COD with treatment of TCE with the synthetic wastewater in UASB reactors

ISSN: 1308772X
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Abstract

The aim of this work was to treat chloroforms (CFs) by upflow anaerobic sludge bed reactors (UASB) and to determine Chemical Oxygen Demand (COD) % removal. The aim of this study was to investigate biological treatment of CFs in high flow rate reactors. Resistance capacity of microorganisms was investigated in a UASB designed as automated control system by feeding with addition of co-substrate, by loading different ratio of organic matter and VOCs, hydraulic retention time, at stable condition of Chemical Oxygen Demand (COD), Volatile Fatty Acids (VFA), pH, alkalinity, temperature (35°C) etc. during the anaerobic treatment. The resulting removal rates for chloroform ranged between 60-70% of COD. The chloroform decomposition ratio was approximately 96%. The highest methane ratio in the obtained biogas was 68.6% for CF. Also inhibition concentrations (IC) in 24 hour were determined as IC50; 27.8 mg/L and IC25; 7.4 mg/L. © Sila Science.

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Ozdemir, C., Sen, N., & Kalipci, E. (2012). Reaction kinetics and removal of COD with treatment of TCE with the synthetic wastewater in UASB reactors. Energy Education Science and Technology Part A: Energy Science and Research, 28(2), 689–698.

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