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Experimental investigation of oily wastewater treatment using combined membrane systems

机译:复合膜系统处理含油废水的实验研究

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Investigations were carried out for purification of oily wastewater by a combined ofnultrafiltration/reverse osmosis (UF/RO) processes. Laboratory-scale UF using polysulfone (PS) andnpolyacrylonitrile (PAN) membranes were employed with typical oily wastewater collected fromnAPI unit of Tehran refinery. The PAN membrane showed higher rejection, more permeation fluxnand less fouling resistance than the PS membrane. Both membranes produced permeate with oilnand grease contents generally less than 5 ppm. Rejection of chemical oxygen demand (COD) andnbiological oxygen demand (BOD5) were found to be 65% for UF treatment. In this work, Hermia’snmodels were used to investigate the fouling mechanism involved in UF of the oily wastewater.nThe results showed that the best fit to experimental data corresponds to the cake layernformation model followed by the intermediate blocking model for both the UF membranes.nFor further treatment of the UF permeates, RO was applied using a thin film composite polyamidenmembrane. The rejection of COD, BOD5 and total dissolved solid (TDS) after UF/RO treatmentnincreased up to 98%, 98% and 95%, respectively. The results showed that the final permeatenhas very high quality and even better than that is currently introduced to the cooling towersnin Tehran refinery.
机译:通过超滤/反渗透(UF / RO)组合工艺进行了含油废水的净化研究。使用聚砜(PS)和聚丙烯腈(PAN)膜的实验室规模超滤与从德黑兰炼油厂的nAPI单元收集的典型含油废水一起使用。与PS膜相比,PAN膜显示出更高的截留率,更高的渗透通量和更低的抗污性。所生产的两种膜都渗透的油脂含量通常小于5 ppm。发现超滤处理的化学需氧量(COD)和生物需氧量(BOD5)拒绝率为65%。在这项工作中,使用Hermia的n模型来研究含油废水超滤的结垢机理。n结果表明,对实验数据的最佳拟合对应于滤饼层形成模型,然后是两个超滤膜的中间阻塞模型。为了进一步处理超滤渗透物,使用了一种薄膜复合聚酰胺膜来进行反渗透。 UF / RO处理后,COD,BOD5和总溶解固体(TDS)的截留率分别提高了98%,98%和95%。结果表明,最终渗透液的质量很高,甚至比德黑兰炼油厂目前引入冷却塔的质量更高。

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