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Dynamic simulation of a WWTP operated at low dissolved oxygen condition by integrating activated sludge model and a floe model

机译:结合活性污泥模型和絮凝物模型对低溶解氧条件下污水处理厂的动态模拟

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While an aeration tank in an activated sludge process is often operated with high dissolved oxygen (DO)concentration to ensure organic degradation and nitrification,it may be operated at low DO concentration to reduce energy consumption and achieve desired denitrification.The ASM1 (Activated Sludge Model No.1)can be used to describe the activated sludge process if the nitrification and denitrification occur either during different phases or in different tanks,but it may encounter problems in simulating the denitrification phenomenon caused by low DO concentration in the aeration tank.In the present work,we developed a model integrating the ASM1 kinetics and a biofloc model to account for the actual anoxic and aerobic rates.Oxygen was assumed the only substrate of both bio-kinetically and flux limiting in the floes and its dispersion coefficient was estimated as 1.2 x 10~(-4)m2 day~(-1)by using a set of measured effluent qualities of a full-scale wastewater treatment plant (WWTP)operating at low DO concentration (~0.80mgL-1)for 60 days.Simulation studies predicted the optimal DO level of 0.36 mgL~(-1)which would lead to minimum total nitrogen of 15.7 mg NL~(-1)and also showed the insignificance of the addition of carbon source for nitrogen removal for the operation under study.The developed model may be helpful for process engineers to predict the plant behaviors under various configurations or operating strategies.
机译:活性污泥工艺中的曝气池通常在高溶解氧(DO)浓度下运行以确保有机降解和硝化作用,但它可以在低DO浓度下运行以减少能耗并实现所需的反硝化效果。 No.1)可用于描述硝化和反硝化在不同阶段或不同罐中发生的活性污泥过程,但在模拟由于曝气池中DO浓度低而引起的反硝化现象时可能会遇到问题。在目前的工作中,我们开发了一个将ASM1动力学模型和一个生物絮凝模型相结合的模型,以说明实际的缺氧率和好氧率。氧被认为是絮凝物中生物动力学和通量限制的唯一底物,其分散系数估计为1.2通过使用一套完整的污水处理厂(WWTP)运营商的测量出的废水水质,得出10〜(-4)m2天〜(-1)在低DO浓度(〜0.80mgL-1)下连续60天ng。模拟研究预测最佳DO浓度为0.36 mgL〜(-1),这将导致最低总氮为15.7 mg NL〜(-1),并且还显示开发的模型可能有助于过程工程师预测各种配置或操作策略下的工厂行为。

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