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Sequential batch membrane bio-reactor for wastewater treatment: The effect of increased salinity

机译:间歇式膜生物反应器用于废水处理:盐度增加的影响

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In this work, a sequential batch membrane bioreactor pilot plant is investigated to analyze the effect of a gradual increase in salinity on carbon and nutrient removal, membrane fouling and biomass kinetic parameters. The salinity was increased by 2 g NaCl L-1 per week up to 10 g NaCl L-1. The total COD removal efficiency was quite high (93%) throughout the experiment. A gradual biomass acclimation to the salinity level was observed during the experiment, highlighting the good recovery capabilities of the system. Nitrification was also influenced by the increase in salinity, with a slight decrease in nitrification efficiency (the lowest value was obtained at 10 g NaCl L-1 due to lower nitrifier activity). Irreversible cake deposition was the predominant fouling mechanism observed during the experiment. Respirometric tests exhibited a stress effect due to salinity, with a reduction in the respiration rates observed (from 8.85 mgO(2) L-1 h(-1) to 4 mgO(2) L-1 h(-1)). (C) 2016 Elsevier Ltd. All rights reserved.
机译:在这项工作中,对连续的膜生物反应器中试工厂进行了研究,以分析盐分逐渐增加对碳和养分去除,膜污染和生物质动力学参数的影响。盐度每周增加2 g NaCl L-1,直至增加10 g NaCl L-1。在整个实验过程中,总COD去除效率非常高(93%)。在实验过程中观察到生物量逐渐适应盐度水平,突出了系统的良好恢复能力。硝化作用还受盐度增加的影响,硝化效率略有下降(由于硝化活性降低,在10 g NaCl L-1处获得最低值)。在实验期间观察到的主要结垢机理是不可逆的饼状沉积。呼吸测试显示由于盐度而产生的压力效应,观察到的呼吸频率降低(从8.85 mgO(2)L-1 h(-1)降至4 mgO(2)L-1 h(-1))。 (C)2016 Elsevier Ltd.保留所有权利。

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