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Experiences with pre-precipitation of phosphorus in a vertical flow constructed wetland in Austria

机译:奥地利垂直流人工湿地中磷的预沉淀经验

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Using constructed wetlands (CWs) with vertical flow and intermittent loading, high organic matter and ammonium removal can be achieved. In the case of additional requirements for phosphorus removal, which in Austria often occurs if the treated wastewater is discharged into small sensitive receiving waters, additional measures have to be taken. The objective of this work was to investigate the applicability of conventional phosphorus pre-precipitation with sodium aluminate for a CW system. The experiment was carried out at a full-scale CW in Oberwindhag in Lower Austria, a two-stage vertical flow CW with intermittent loading designed for a size of 60 person equivalents (PE). The goal was to reach the required value of 1.6 mg/L PO_(4-)P for the effluent of the system. Prior to the experiments the plant was in operation for 3 years without measures for phosphorus removal. After pre-precipitation with sodium aluminate was activated, three different dosages were investigated. Satisfying results in the preliminary treatment chambers were not obtained until a high dosage (β = 3.5, i.e. 3.5 times the dose required from stoichiometry) was applied. After an adaptation time of several months the required effluent concentration of 1.6 mg PO_(4-)P/L could be reached and maintained. However, the additional phosphorus pre-precipitation increases the yearly operating costs of a vertical flow CW system significantly, e.g. for 60 and 25 PE, by 15 and 38%, respectively, thus indicating the need for optimizing the dosing of the chemical.
机译:使用具有垂直流和间歇负荷的人工湿地(CW),可以实现高有机物和铵的去除。对于除磷有额外的要求,在奥地利,如果将处理后的废水排放到敏感的小型接收水中通常会发生除磷的要求,则必须采取其他措施。这项工作的目的是研究传统的磷铝酸钠预沉淀法在连续波系统中的适用性。该实验在下奥地利州Oberwindhag的大型CW上进行,这是一种具有间歇载荷的两阶段垂直流CW,设计用于60人当量(PE)。目标是达到系统废水所需的1.6 mg / L PO_(4-)P值。在实验之前,该设备已经运行了3年,没有采取任何除磷措施。用铝酸钠预沉淀后,研究了三种不同的剂量。直到施加高剂量(β= 3.5,即化学计量所需剂量的3.5倍),才能在初步处理室中获得满意的结果。经过几个月的适应时间后,可以达到并维持所需的污水浓度1.6 mg PO_(4-)P / L。但是,额外的磷预沉淀会显着增加立式CW系统的年运行成本,例如60和25 PE分别增加15%和38%,因此表明需要优化化学药品的剂量。

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