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Enhanced Primary Treatment in Floating Filters

机译:浮式过滤器的强化初级处理

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Experiments were carried out on the use of a floating filter for primary treatment of municipal wastewater. The floating filter used is based on up-flow filtration through a randomly packed filter-bed consisting of plastic biofilm carriers that are normally used in the Kaldnes moving bed biofilm process. It was demonstrated that, because of the high porosity of the filter bed, head-loss was low, resulting in long filter runs and high sludge accumulation capacities. The SS-removal efficiency experienced was in the range of 75-85percent at a filtration rate in the range of 5-15m/h, making this concept a very interesting one for primary treatment. The key design parameter was found to be the sludge loading rate (kgSS/m~2h). At a typical filter depth of 1 m, a filter run time of 5 hrs was experienced at a surface loading of 2 kgSs/m~2h while doubling the filter run time required cutting the sludge surface loading in half. Pre-coagulation with cationic polymer, possibly in combination with a low metal-coagulant dose, did not significantly improve performance.
机译:使用浮式过滤器对市政废水进行初步处理进行了实验。所使用的浮式过滤器基于通过随机填充的滤床的向上流动过滤,该滤床由通常在Kaldnes移动床生物膜工艺中使用的塑料生物膜载体组成。事实证明,由于滤床的孔隙率高,压头损失低,从而导致滤清器运行时间长和污泥积聚能力高。在过滤速度为5-15m / h的情况下,经历的SS去除效率在75%至85%的范围内,这使得该概念成为初级处理中非常有趣的一个概念。关键设计参数为污泥负荷率(kgSS / m〜2h)。在典型的过滤器深度为1 m的情况下,在2 kgSs / m〜2h的表面负荷下经历了5个小时的过滤器运行时间,而将需要将污泥表面负荷减半的过滤器运行时间加倍。用阳离子聚合物进行预凝结(可能与低金属凝结剂量结合使用)并不能显着改善性能。

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