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Feasibility study on petrochemical wastewater treatment and reuse using a novel submerged membrane distillation bioreactor

机译:新型浸没式膜蒸馏生物反应器处理石化废水及回用的可行性研究

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摘要

Treatment of wastewater from a petrochemical industry has been investigated using a novel submerged membrane distillation bioreactor (MDBR). A bench scale MDBR system with flat sheet membranes was used in the study. The testing system ran continuously (24-h) over 105 days. Membrane cleaning was conducted when the permeate flux decreased to less than 5.5 L/m~2 h. The results showed that MDBR product quality consistently met the requirements of NEWater of Singapore except for a slightly higher total organic carbon (TOC). The membranes were found to be thermally stable, and good separation characteristics were maintained throughout the whole period of the investigation. A permeate flux of 5.5-8.6 L/m~2 h for more than a month without membrane cleaning was achieved despite variations in the feed wastewater. The flux decline was mainly due to inorganic fouling of the membranes. Membrane permeability could be recovered by chemical cleaning. It was concluded that it was feasible to treat and reuse the wastewater using submersed MDBR technology.
机译:已经使用新型的浸没式膜蒸馏生物反应器(MDBR)研究了石化工业废水的处理。在研究中使用了带有平板膜的台式MDBR系统。测试系统在105天内连续(24小时)运行。当渗透通量降低到小于5.5 L / m〜2 h时进行膜清洗。结果表明,MDBR产品质量始终符合新加坡NEWater的要求,但总有机碳(TOC)略高。发现该膜是热稳定的,并且在整个研究期间都保持了良好的分离特性。尽管进料废水有所变化,但在不进行膜清洁的情况下,仍能实现5.5-8.6 L / m〜2 h的渗透通量,超过一个月。通量下降主要是由于膜的无机结垢。膜的渗透性可以通过化学清洁来恢复。结论是,使用淹没式MDBR技术处理和再利用废水是可行的。

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