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Simultaneous Nitrification-Denitrification and Clarification in a Pseudoliquified Activated Sludge System

机译:液化活性污泥系统中同时硝化-反硝化和澄清

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This paper describes results from a pilot study of a novel wastewater treatment technology, which incorporates nutrient removal and solids separation to a single step. The pseudoliquified activated sludge process pilot system was tested on grit removal effluent at flowrates of 29.4 to 54.7 m /d, three different solid residence times (SRT) (15, 37, and 57 days), and over a temperature range of 12 to 28 deg C. Despite wide fluctuations in the influent characteristics, the system performed reliably and consistently with respect to organics and total suspended solids (TSS) removals, achieving biochemical oxygen demand (BOD) and TSS reductions of >96 percent and approximately 90 percent, respectively, with BOD_5 and TSS concentrations as low as 3 mg/L. Although the system achieved average effluent ammonia concentrations of 2.7 to 3.2 mg/L, nitrification efficiency appeared to be hampered at low temperatures (<15 deg C). The system achieved tertiary effluent quality with denitrification efficiencies of 90 and 91 percent total nitrogen removal efficiency at a total hydraulic retention time of 4.8 hours and an SRT of 12 to 17 days. With ferric chloride addition, effluent phosphorous concentrations of 0.5 to 0.8 mg/L were achieved. Furthermore, because of operation at high biomass concentrations and relatively long biological SRTs, sludge yields were over 50 percent below typical values for activated sludge plants. The process was modeled using activated sludge model No. 2, as a two-stage system comprised an aerobic activated sludge system followed by an anoxic system. Model predictions for soluble BOD, ammonia, nitrates, and orthophosphates agreed well with experimental data.
机译:本文介绍了一项新型废水处理技术的试验研究结果,该技术将营养物去除和固体分离整合到一个步骤中。在流量为29.4至54.7 m / d,三种不同的固体停留时间(SRT)(15、37和57天),温度范围为12至28的条件下,对假液化活性污泥工艺中试系统进行了测试。尽管进水特性波动很大,但该系统在去除有机物和总悬浮固体(TSS)方面仍可靠且始终如一地运行,分别实现生化需氧量(BOD)和TSS降低> 96%和约90% ,其BOD_5和TSS浓度低至3 mg / L。尽管系统的平均出水氨浓度为2.7至3.2 mg / L,但在低温(<15摄氏度)下硝化效率似乎受到了阻碍。该系统以4.8小时的总水力停留时间和12至17天的SRT达到了三级废水质量,脱氮效率分别为90%和91%的总氮去除效率。加入氯化铁后,废水中的磷浓度达到0.5至0.8 mg / L。此外,由于在高生物质浓度下运行且生物SRT相对较长,因此污泥产率比活性污泥厂的典型值低50%以上。该过程使用2号活性污泥模型进行建模,这是一个两阶段系统,包括好氧活性污泥系统和缺氧系统。可溶性BOD,氨,硝酸盐和正磷酸盐的模型预测与实验数据非常吻合。

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