The impact of fouling on N-nitrosamine rejection by nanofiltration (NF) and reverse osmosis (RO) membranes was investigated in this study. Membrane fouling was simulated using tertiary treated effluent and several model fouling solutions (that contained sodium alginate, bovine serum albumin, humic acid or colloidal silica) to elucidate the changes in rejection behaviour of N-nitrosamines. In general, the rejection of N-nitrosamines increased when the membranes were fouled by tertiary effluent. The rejection of small molecular weight N-nitrosamines was most affected by membrane fouling. In particular, the rejection of N-nitrosodimethylamine (NDMA) by the ESPA2 membrane increased from 34 to 73% after membrane fouling caused by tertiary effluent. The results also indicate that the impact was less apparent for the lowest permeability membrane (i.e., ESPAB), and the rejection of N-nitrosamines by the ESPAB membrane was over 82% regardless of membrane fouling. The effect of membrane fouling caused by model foulants on N-nitrosamine rejection was considerably less than that caused by tertiary effluent. Size exclusion chromatography analyses revealed that the tertiary effluent contains a high fraction of low molecular weight (\u3c 500 g/mol) organic substances. It appears that these low molecular weight foulants present in the tertiary effluent can restrict the solute pathway within the active skin layer of membranes, resulting in the observed increase of solute rejection.
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机译:在本研究中,研究了结垢对纳滤(NF)和反渗透(RO)膜对N-亚硝胺排斥的影响。使用三级处理污水和几种模型污垢溶液(包含藻酸钠,牛血清白蛋白,腐殖酸或硅胶)模拟膜污染,以阐明N-亚硝胺排斥行为的变化。通常,当三级流出物污染膜时,N-亚硝胺的排斥率会增加。小分子量N-亚硝胺的排斥最受膜污染的影响。尤其是,由三级流出物引起的膜污染后,ESPA2膜对N-亚硝基二甲胺(NDMA)的排斥率从34%增加到73%。结果还表明,对于最低渗透率的膜(即ESPAB),影响不明显,并且无论膜是否结垢,ESPAB膜对N-亚硝胺的排斥率都超过82%。模型污垢引起的膜污染对N-亚硝胺排斥的影响远小于第三种废水造成的影响。尺寸排阻色谱分析表明,第三级流出物中含有高比例的低分子量(500 g / mol)有机物。似乎存在于第三流出物中的这些低分子量污垢物可以限制膜的活性表皮层内的溶质途径,从而导致观察到的溶质截留率增加。
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