Université de Toulouse; INSA, UPS, INP; LISBP, 135 Avenue de Rangueil, F-31077 Toulouse, France.
Water Res. 2010 Apr;44(7):2113-24. doi: 10.1016/j.watres.2009.12.021. Epub 2009 Dec 16.
This work aims to characterise the impact of hydrodynamics on sludge properties and consequently on fouling mechanisms in side-stream membrane bioreactors (MBRs). Two side-stream processes which generate very different shear stresses are compared, without filtration. This operating mode permits specific quantification of the impact of the external loop (and of induced shear stress) on floc structure/morphology, supernatant quality and fouling propensity. The study shows that low constraints (7 x 10(-3) Pa) generated on submerged side-stream hollow fibre modules have no significant impact on sludge properties. In contrast, high shear stresses (72 Pa) associated with a crossflow configuration induce very significant modifications of the mixed liquor which increases its fouling propensity (measured in a standard filtration cell). A theoretical explanation of the role of turbulence on the floc size distribution is given. Based on a Kolmogorov microscale calculation, it seems possible to predict the mean floc size reached in both filtration systems, for a given shear stress intensity. Disaggregation is characterised by a two-step kinetic: first a short-term breakage attributed to fragmentation and loss of weak strength bonds, and secondly a longer-term breakage probably due to erosion phenomena and removal of high strength bonds. Only the second step induces a significant release and an accumulation of soluble protein-like substances. Soluble organic matter strongly enhances the fouling propensity of the mixed liquor. This seems to be amplified by the concentration of protein-like substances. The importance of considering the protein and carbohydrate content as well as floc size is also pointed out in the paper.
本工作旨在研究水动力条件对污泥特性的影响,进而研究侧流膜生物反应器(MBR)中的污染机制。对比了两种产生不同剪切应力的侧流工艺,且过程中不进行过滤。这种操作模式可以对外部循环(以及诱导剪切应力)对絮体结构/形态、上清液质量和污染倾向的影响进行具体量化。研究表明,在浸没式侧流中空纤维模块中产生的低约束(7×10^(-3)Pa)对污泥特性没有显著影响。相比之下,与错流配置相关的高剪切应力(72Pa)会引起混合液的显著变化,从而增加其污染倾向(在标准过滤池中进行测量)。本文给出了湍流对絮体粒径分布作用的理论解释。根据科尔莫戈罗夫微尺度计算,对于给定的剪切应力强度,似乎有可能预测两种过滤系统中达到的平均絮体尺寸。解絮作用由两步动力学来描述:首先是由于碎片化和弱结合键的损失导致的短期解絮,其次是由于侵蚀现象和高结合键的去除导致的长期解絮。只有第二步会引起大量可溶性蛋白样物质的释放和积累。可溶性有机物强烈增强了混合液的污染倾向。这似乎被蛋白样物质的浓度放大了。本文还指出了考虑蛋白质和碳水化合物含量以及絮体大小的重要性。