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Modelling approach to better control biofouling in fluidized bed membrane bioreactor for wastewater treatment

机译:用于废水处理的流化床膜生物反应器中更好地控制生物结垢的建模方法

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摘要

A mathematical model has been developed to better understand fouling mitigation mechanisms in particle-sparged membrane bioreactor. The model developed herein assumes two fouling mechanisms, (i) the pore blocking leading to the decrease in membrane surface porosity and (ii) the progressive development of compressible cake layer on the membrane surface. The model has been validated by comparison with trans-membrane pressure data registered from the bioreactor filtering a synthetic solution consisting of bentonite, sodium alginate and bovin serum albumine (BSA). Two nonporous media have been tested, Polyethylene terephthalate (PET) beads and silica particles with different dosage (0,10, 30, 50 and 70% (v/v)). Compared to the experimental data, the model shows satisfactory fitting with R-2 >= 93%. For both media tested, an optimal dosage to minimize fouling rate was observed at 50% (v/v). Even if both fouling mechanisms have been mitigated by adding fluidized media, pore blocking was more pronounced than cake formation. Moreover, better pore blocking mitigation was observed with PET media (50% (v/v)) having bigger size and lower density than silica particles. (C) 2017 Elsevier Ltd. All rights reserved.
机译:已经开发出数学模型以更好地理解颗粒稀疏的膜生物反应器中的结垢缓解机制。本文开发的模型假定了两种结垢机理:(i)孔堵塞导致膜表面孔隙率降低,以及(ii)膜表面上可压缩饼层的逐步发展。通过与生物反应器记录的跨膜压力数据进行比较,验证了该模型,该数据过滤了由膨润土,藻酸钠和牛血清白蛋白(BSA)组成的合成溶液。已测试了两种无孔介质,即聚对苯二甲酸乙二醇酯(PET)珠和具有不同剂量(0、10、30、50和70%(v / v))的二氧化硅颗粒。与实验数据相比,该模型显示出令人满意的拟合,R-2> = 93%。对于两种测试介质,在50%(v / v)处均观察到了最小化结垢率的最佳剂量。即使通过添加流态化介质缓解了两种结垢机理,孔堵塞也比形成滤饼更为明显。此外,与二氧化硅颗粒相比,PET介质(50%(v / v))具有更大的尺寸和更低的密度,可以更好地缓解孔堵塞。 (C)2017 Elsevier Ltd.保留所有权利。

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