Ramakrishnan Anushyaa, Gupta S K
Centre for Environmental Science and Engineering, Indian Institute of Technology Bombay, Powai, Mumbai 400076, India.
J Hazard Mater. 2006 Oct 11;137(3):1488-95. doi: 10.1016/j.jhazmat.2006.04.034. Epub 2006 May 2.
Granulation was examined in four similar anaerobic hybrid reactors 15.5L volume (with an effective volume of 13.5L) during the treatment of synthetic coal wastewater at the mesophilic temperature of 27+/-5 degrees C. The hybrid reactors are a combination of UASB unit at the lower part and an anaerobic filter at the upper end. Synthetic wastewater with an average chemical oxygen demand (COD) of 2,240 mg/L, phenolics concentration of 752 mg/L and a mixture of volatile fatty acids was fed to three hybrid reactors. The fourth reactor, control system, was fed with a wastewater containing sodium acetate and mineral nutrients. Coal waste water contained phenol (490 mg/L); m-, o-, p-cresols (123.0, 58.6, 42 mg/L); 2,4-, 2,5-, 3,4- and 3,5-dimethyl phenols (6.3, 6.3, 4.4 and 21.3mg/L) as major phenolic compounds. A mixture of anaerobic digester sludge and partially granulated sludge (3:1) were used as seed materials for the start up of the reactors. Granules were observed after 45 days of operation of the systems. The granules ranged from 0.4 to 1.2 mm in diameter with good settling characteristics with an SVI of 12 mL/gSS. After granulation, the hybrid reactor performed steadily with phenolics and COD removal efficiencies of 93% and 88%, respectively at volumetric loading rate of 2.24 g COD/Ld and hydraulic retention time of 24 h. The removal efficiencies for phenol and m/p-cresols reached 92% and 93% (corresponding to 450.8 and 153 mg/L), while o-cresol was degraded to 88% (corresponding to 51.04 mg/L). Dimethyl phenols could be removed completely at all the organic loadings and did not contribute much to the residual organics. Biodegradation of o-cresol was obtained in the hybrid-UASB reactors.
在中温27±5℃处理合成煤废水期间,对四个体积为15.5L(有效体积为13.5L)的类似厌氧复合反应器中的颗粒化情况进行了研究。复合反应器是下部UASB单元和上端厌氧滤池的组合。平均化学需氧量(COD)为2240mg/L、酚类浓度为752mg/L且含有挥发性脂肪酸混合物的合成废水被输送到三个复合反应器中。第四个反应器作为控制系统,被输送含有醋酸钠和矿物质营养物的废水。煤废水含有酚(490mg/L);间甲酚、邻甲酚、对甲酚(123.0、58.6、42mg/L);2,4-、2,5-、3,4-和3,5-二甲基酚(6.3、6.3、4.4和21.3mg/L)作为主要酚类化合物。将厌氧消化池污泥和部分颗粒化污泥的混合物(3:1)用作反应器启动的接种材料。系统运行45天后观察到颗粒。颗粒直径在0.4至1.2mm之间,沉降性能良好,污泥体积指数(SVI)为12mL/gSS。颗粒化后,复合反应器稳定运行,在容积负荷率为2.24g COD/L·d和水力停留时间为24h的情况下,酚类和COD的去除效率分别为93%和88%。酚和间/对甲酚的去除效率达到92%和93%(分别对应450.8和153mg/L),而邻甲酚降解到88%(对应51.04mg/L)。在所有有机负荷下,二甲基酚均可被完全去除,且对残留有机物贡献不大。在复合-UASB反应器中实现了邻甲酚的生物降解。