Spatial and temporal variations of monitoring performance parameters in horizontal-flow anaerobic immobilized sludge (HAIS) reactor treating synthetic substrate
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- 作者：Zaiat ; M. ; Vieira ; L.G.T. ; Foresti ; E.
- 关键词：anaerobic wastewater treatment ; horizontal-flow anaerobic immobilized sludge (HAIS) reactor ; synthetic substrate ; bioparticles of polyurethane foam
- 刊名：Water Research
- 出版年：1997
- 出版时间：July, 1997
- 年：1997
- 卷：31
- 期：7
- 页码：1760-1766
- 全文大小：618 K
文摘
This paper reports on experiments with a lab-scale horizontal-flow anaerobic immobilized sludge (HAIS) reactor treating synthetic substrate aiming to observe temporal and spatial variations of its monitoring performance parameters. The bench-scale HAIS reactor was filled with polyurethane foam matrices containing immobilized anaerobic sludge taken from an upflow anaerobic sludge blanket (UASB) reactor treating diluted piggery wastewater. A synthetic substrate composed of glucose as the main carbon source (chemical oxygen demand — COD of 2090 mg 1−1) was used for feeding the HAIS reactor in two experiments with bed porosities (?) of 0.4 and 0.24 and at hydraulic detention times (HDT) of 8.0 and 4.8 h, respectively. The temperature was maintained at 30°C, and COD, volatile fatty acids (VFA), total alkalinity (TA) and pH were monitored in the effluent stream (length to diameter ratio — L/D of 20) and intermediate ports along the reactor's length (L/D of 4, 8, 12 and 16). CH4 concentration in the gas was determined daily for evaluating the start-up period duration. The short start-up period duration (6 days) in both the experiments confirmed that a HAIS reactor can provide favorable environmental conditions for rapid biomass acclimatization, growth and retention. COD removal efficiencies of 98 % were attained in the first experiment (? of 0.4) and the effluent VFA concentration was lowered to 15 mg 1−1. At the L/D ratio of 4 in the first sampling port, corresponding to a HDT of 1.6 h, the COD removal efficiency achieved 72 % . In the second experiment (? of 0.24), the maximum COD removal efficiency was 80 % and the effluent VFA leveled 350 mg 1−1. Channeling due to the low bed porosity was found to be the main factor responsible for the poor performance of the reactor operating at ? of 0.24.