Sundaresan N, Philip L
Department of Civil Engineering, Indian Institute of Technology Madras, India.
Water Sci Technol. 2008;58(4):819-30. doi: 10.2166/wst.2008.340.
Studies were undertaken on the performance evaluation of three different types of aerobic reactors, namely, activated sludge process, fluidized bed reactor and submerged bed reactor. Initially synthetic wastewater was used for stabilizing the system and later domestic wastewater of IIT Madras was used as the feed for the biological systems. The hydraulic retention time was maintained as 24 h. The seed sludge was collected from IIT Madras sewage treatment plant. The inlet COD to the reactors with synthetic wastewater was 1,000 +/- 20 mg/L and with real wastewater, it was 150 to 350 mg/L. The performance of the reactors was evaluated based on the soluble COD and nitrogen removal efficiency. The pH, temperature, dissolved oxygen (DO) and mixed liquid suspended solid (MLSS) concentration were measured periodically. The reactors were acclimatized at 35 degrees C in batch mode and changed to continuous mode at 30 degrees C. After the systems attained its steady state at a particular temperature, the temperature was reduced from 35 degrees C to 5 degrees C stepwise, with each step of 5 degrees C. The start-up time for submerged bed reactor was slightly more than fluidized and conventional activated sludge process.The COD removal efficiency of the three reactors was higher with synthetic wastewaters as compared to actual domestic wastewater. Submerged bed reactor was more robust and efficient as compared to activated sludge and fluidized bed reactors. The COD removal efficiency of the reactors was relatively good until the operating temperature was maintained at 15 degrees C or above. At 10 degrees C, submerged bed reactor was able to achieve 40% COD removal efficiency whereas; the fluidized bed and conventional ASP reactors were showing only 20% COD removal efficiency. At 5 degrees C, almost all the systems failed. Submerged bed reactor showed around 20% COD removal efficiency. However, this reactor was able to regain its 90% of original efficiency, once the temperature was raised to 10 degrees C. At higher temperatures, the nitrification efficiency of the reactors was above 80-90%. As the temperature reduced the nitrification efficiency has reduced drastically. In summary, submerged bed reactors seems to be a better option for treating domestic wastewaters at low temperature regions.
对三种不同类型的好氧反应器进行了性能评估,即活性污泥法、流化床反应器和淹没式床反应器。最初使用合成废水来稳定系统,后来将印度理工学院马德拉斯分校的生活污水用作生物系统的进料。水力停留时间保持为24小时。接种污泥取自印度理工学院马德拉斯分校污水处理厂。合成废水进入反应器的化学需氧量(COD)为1000±20mg/L,实际废水的COD为150至350mg/L。基于可溶性COD和脱氮效率对反应器的性能进行评估。定期测量pH值、温度、溶解氧(DO)和混合液悬浮固体(MLSS)浓度。反应器在35℃下以间歇模式进行驯化,并在30℃时改为连续模式。在系统在特定温度下达到稳态后,温度从35℃逐步降至5℃,每步降低5℃。淹没式床反应器的启动时间略长于流化床和传统活性污泥法。与实际生活污水相比,三种反应器对合成废水的COD去除效率更高。与活性污泥和流化床反应器相比,淹没式床反应器更坚固且效率更高。直到操作温度保持在15℃或以上,反应器的COD去除效率相对良好。在10℃时,淹没式床反应器能够实现40%的COD去除效率,而流化床和传统活性污泥法反应器仅显示20%的COD去除效率。在5℃时,几乎所有系统都失效。淹没式床反应器显示出约20%的COD去除效率。然而,一旦温度升至10℃,该反应器能够恢复其90%的原始效率。在较高温度下,反应器的硝化效率高于80-90%。随着温度降低,硝化效率急剧下降。总之,淹没式床反应器似乎是在低温地区处理生活污水的更好选择。