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Effect of solids residence time on dynamic responses in chemical P removal

机译:固体停留时间对化学除磷动态响应的影响

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摘要

The impact of solids residence time (SRT) on the dynamics of phosphorus (P) removal by hydrous ferric oxide (HFO) floc was characterized through experimental and modeling studies. Three abiotic process conditions were considered in systems operated over a range of SRTs (similar to 3 to 27 days): uptake in sequencing batch reactors (SBRs) under (a) constant and (b) dynamic P loading conditions, and (c) uptake in batch sorption tests with preformed HFO solids. P removal under all conditions was characterized by an initial period of fast removal followed by a period of slower removal until pseudo-equilibrium was reached. The initial removal rate increased with increasing P concentrations and was attributed to a larger concentration gradient between soluble-and adsorbed-phase concentrations. A kinetic model was developed and found to describe the dynamic behavior of P adsorption onto HFO floc under all conditions tested. A consistent mass transfer rate coefficient (k) was found to describe mass transfer over a range of SRTs for low initial P concentrations. At elevated SRTs (23-27 days) and elevated influent P concentrations, k values were found to deviate from those estimated at reduced SRTs. Differences in process mixing conditions were reflected in the estimated rate coefficients (k). Integration of the kinetic model with existing equilibrium models in wastewater process simulators will improve the ability to predict P uptake onto HFO floc under dynamic loading conditions in water resource recovery facilities. Models that consider the kinetics of P uptake will be particularly relevant for facilities that are required to achieve ultralow P concentrations. (C) 2019 Water Environment Federation
机译:通过实验和模型研究表征了固体停留时间(SRT)对水合氧化铁(HFO)絮凝物去除磷(P)动力学的影响。在一系列SRT(约3至27天)上运行的系统中考虑了三种非生物工艺条件:在(a)恒定和(b)动态P加载条件下,在顺序分批反应器(SBR)中的吸收,以及(c)吸收使用预制的HFO固体进行分批吸附测试。在所有条件下去除P的特征是,先进行快速去除,然后再进行较慢的去除,直到达到伪平衡为止。初始去除率随P浓度的增加而增加,并且归因于可溶性相和吸附相之间的浓度梯度较大。建立了动力学模型,发现该模型描述了在所有测试条件下P吸附到HFO絮凝物上的动力学行为。发现一致的传质速率系数(k)描述了对于低初始P浓度在一系列SRT上的传质。在升高的SRT(23-27天)和升高的进水P浓度下,发现k值与降低的SRT所估计的k值不同。工艺混合条件的差异反映在估计的速率系数(k)中。在废水处理模拟器中将动力学模型与现有的平衡模型进行集成将提高在水资源回收设施中动态装载条件下预测HFO絮凝物对P吸收的能力。考虑到P吸收动力学的模型对于达到超低P浓度所需的设施特别重要。 (C)2019水环境联合会

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