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Sub-critical fouling in a membrane bioreactor for municipal wastewater treatment: Experimental investigation and mathematical modelling

机译:膜生物反应器中用于城市污水处理的亚临界结垢:实验研究和数学建模

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Fouling is a major limitation for the application of membrane bioreactors (MBRs) in municipal wastewater treatment; the critical flux concept represents a valid tool for process optimisation in planning fouling control strategies. The paper presents the results obtained on a large pilot MBR equipped with a plate-and-frame ultrafiltration membrane. The experimental assessment of flux criticality was carried out by flux-stepping tests showing the positive impact of liquid temperature on the value of the critical threshold. The reliability of short-term tests was then verified over a long period by determining the time of sustainability,t_(sust) of six different sub-critical fluxes ranging between 17 and 30Lm~(-2)h~(-1). An exponential fitting was observed in terms of fouling rate both before and after t_(sust), though fouling after t_(sust) is likely to be ascribed not only to cake formation. Finally, a new mathematical formulation was proposed according to the local flux approach to model the sub-critical TMP transients. The model involves both bound and free forms of EPS and, once experimentally calibrated, it provided a fair prediction of the TMP jump.
机译:膜污染是膜生物反应器(MBR)在市政废水处理中的主要限制;临界通量概念代表了在计划结垢控制策略中进行过程优化的有效工具。本文介绍了在配备板框超滤膜的大型MBR中获得的结果。通量逐步测试对通量临界值进行了实验评估,显示出液温对临界阈值的积极影响。然后通过确定六个不同的亚临界通量在17和30Lm〜(-2)h〜(-1)之间的持续时间t_(sust),来验证短期测试的可靠性。尽管在t_(sust)之前和之后的结垢率方面都观察到了指数拟合,但是t_(sust)之后的结垢可能不仅归因于滤饼的形成。最后,根据局部通量方法,提出了一种新的数学公式来模拟次临界TMP瞬变。该模型涉及EPS的束缚和自由形式,并且通过实验校准后,它可以为TMP跳跃提供合理的预测。

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