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Non-woven fabric filter separation activated sludge reactor for domestic wastewater reclamation

机译:用于生活污水再生的无纺布过滤分离活性污泥反应器

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A non-woven fabric filter was experimentally evaluated for solid-liquid separation in an activated sludge reactor as an alternative membrane. A polypropylene fabric filter (70, 50 and 35 g/m(2)) was used for the experiment. The pilot system was operated in A/O (Anaerobic/Oxic) type in which the filter module was submerged into the oxic compartment. The filtration module consists of 10 plate type rectangular filter elements with effective filtration area, 2 m(2). Gravity filtration was carried out for solid-liquid separation by changing the water head 0.05-0.5 m without backwashing during the system operation. Initial permeate flux was set at 0.4 m/dx. C/N ratio of raw wastewater was controlled at 4.5 in terms of BOD/T-N. The fabric filter system showed a good performance enough for domestic wastewater treatment. Effluent solid concentration was 3.2 mg/L (93.5% removal). COD removal efficiency was 91.6% producing an effluent concentration around 13 mg/L. 66% of total nitrogen removal could be obtained at the adjusted C/N ratio of influent wastewater. However phosphorus removal was very low at 23%. It was found that the initial flux of 0.4 m/d should be maintained for stable performance of the system. [References: 6]
机译:实验评估了无纺布过滤器在活性污泥反应器中作为替代膜的固液分离。聚丙烯织物过滤器(70、50和35 g / m(2))用于实验。先导系统以A / O(厌氧/有氧)类型运行,其中过滤器模块浸入有氧隔室中。过滤模块由10个板式矩形过滤器元件组成,有效过滤面积为2 m(2)。在系统运行过程中,通过在不进行反冲洗的情况下,通过改变水头0.05-0.5 m进行重力过滤以进行固液分离。初始渗透通量设定为0.4 m / dx。以生化需氧量/总氮为标准,原废水的碳氮比控制在4.5。织物过滤器系统显示出足以用于生活污水处理的良好性能。出水固体浓度为3.2 mg / L(去除93.5%)。 COD去除效率为91.6%,产生的废水浓度约为13 mg / L。在调整后的进水C / N比下,可以获得66%的总氮去除率。然而,除磷非常低,仅为23%。已发现应保持0.4 m / d的初始通量,以使系统稳定运行。 [参考:6]

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