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Operational factors of submerged inorganic membrane bioreactor for organic wastewater treatment: sludge concentration and aeration rate

机译:淹没式无机膜生物反应器处理有机废水的操作因素:污泥浓度和曝气速率

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Various sludge concentrations and aeration rates were evaluated to find the optimal operation condition of a submerged ceramic membrane filtration system. 5.6 g/L of sludge was diluted with water to concentrations of 2.8 g/L and 1.4 g/L, and the three sludge concentrations were compared in terms of filtration characteristics such as pressure and filtrate flux. Flux was at the highest value of about 30 L/m(2).hr at 50 kPa when sludge concentration was 1.4 g/L. In contrast, when sludge concentrations increased to 2.8 g/L and 5.6 g/L, the flux at 50 kPa decreased significantly to 18 L/m(2).hr and 10 L/M-2.hr, respectively. It was concluded that the sludge concentration directly affected the filtration efficiency, and low sludge concentration was suitable for improving filtration efficiency. Adjusting the aeration rate from 2 L/min to 4 L/min at 5.6 g/L of sludge and 50 kPa of pressure increased flux from 10 L/m2.hr to 13 L/M2.hr. It was obvious that the vigorous aeration improved the filtration efficiency, but the aeration rate did not seem to be high enough to maintain flux lower than critical flux. [References: 12]
机译:对各种污泥浓度和曝气速率进行了评估,以找到浸没式陶瓷膜过滤系统的最佳运行条件。用水将5.6 g / L的污泥稀释至2.8 g / L和1.4 g / L的浓度,并根据压力和滤液通量等过滤特性比较了三种污泥的浓度。当污泥浓度为1.4 g / L时,通量在50 kPa时约为30 L / m(2).hr的最大值。相反,当污泥浓度增加到2.8 g / L和5.6 g / L时,在50 kPa处的通量分别显着下降到18 L / m(2).hr和10 L / M-2.hr。结论是污泥浓度直接影响过滤效率,低污泥浓度适合提高过滤效率。在5.6 g / L的污泥和50 kPa的压力下,将曝气速率从2 L / min调整为4 L / min,使通量从10 L / m2.hr增加到13 L / M2.hr。显然,剧烈通气可以提高过滤效率,但是通气率似乎不足以维持通量低于临界通量。 [参考:12]

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