Environmental Simulation and Pollution Control State Key Joint Laboratory, State Environmental Protection Key Laboratory of Microorganism Application and Risk Control (SMARC), School of Environment, Tsinghua University, Room 524, Beijing 100084, PR China.
Environmental Simulation and Pollution Control State Key Joint Laboratory, State Environmental Protection Key Laboratory of Microorganism Application and Risk Control (SMARC), School of Environment, Tsinghua University, Room 524, Beijing 100084, PR China; Beijing Laboratory for Environmental Frontier Technologies, Beijing 100084, PR China.
Water Res. 2022 Jul 15;220:118672. doi: 10.1016/j.watres.2022.118672. Epub 2022 May 26.
Ultrafiltration (UF) was often used as pretreatment in front of reverse osmosis (RO) unit because of its high rejection efficiency of microbes and particles. However, in some cases UF pretreatment might show adverse effects on the RO membrane flux. In this study, the effects of UF pretreatment on secondary effluent water quality and its RO membrane fouling characteristics were explored. There was almost no change of water quality after UF with different molecular weight cut-off (MWCO) membranes (100, 30 and 10 kDa), including total dissolved solid (TDS), alkalinity, conductivity, ion concentrations, etc., while pH increased a little and dissolved organic carbon (DOC) declined by about 1 mg/L. On the contrary, the RO membrane flux of UF permeates presented clear decline in comparison to the secondary effluent. The membrane fouling velocity and steady-state flux of secondary effluent was 0.052 and 0.656, while fouling velocity increased (0.077, 0.071, 0.067) and steady-state flux decreased significantly (0.397, 0.416, 0.448) after 100, 30, 10 kDa UF membrane pretreatment. Scanning electron microscope (SEM) images showed many crystals on the fouled membrane surfaces, which turned out to be CaCO by Energy dispersive spectrometer (EDS) analysis and precipitation calculation. After the addition of UF retentates to UF permeates, scaling was prevented and crystals on the RO membrane almost disappeared, which implied the anti-scaling effect of the UF retentates with low concentration. According to anti-scaling performance experiments, the anti-scaling performance of 100 k, 30 k, 10 k retentates was 2.7%, 4.0% and 7.3%, respectively. Excitation emission matrix (EEM) and fourier transform infra-red (FTIR) results showed that these retentates retained by different MWCO membranes were similar and composed of protein-like substances and soluble microbial products. The effect of key minority components in RO system deserved further exploration.
超滤(UF)因其对微生物和颗粒的高去除效率,常被用作反渗透(RO)装置的预处理。然而,在某些情况下,UF 预处理可能会对 RO 膜通量产生不利影响。本研究探索了 UF 预处理对二级出水水质及其 RO 膜污染特性的影响。不同截留分子量(MWCO)的 UF 膜(100、30 和 10 kDa)处理后水质几乎没有变化,包括总溶解固体(TDS)、碱度、电导率、离子浓度等,而 pH 值略有升高,溶解有机碳(DOC)下降约 1 mg/L。相比之下,UF 透过液的 RO 膜通量明显下降。二级出水的膜污染速率和稳态通量分别为 0.052 和 0.656,而经过 100、30 和 10 kDa UF 膜预处理后,膜污染速率分别增加(0.077、0.071、0.067),稳态通量显著降低(0.397、0.416、0.448)。扫描电子显微镜(SEM)图像显示,污染膜表面有许多晶体,经能谱仪(EDS)分析和沉淀计算确定为碳酸钙。将 UF 截留液添加到 UF 透过液中后,结垢得到了抑制,RO 膜上的晶体几乎消失,这表明低浓度 UF 截留液具有抗结垢效果。根据抗结垢性能实验,100 kDa、30 kDa、10 kDa 截留液的抗结垢性能分别为 2.7%、4.0%和 7.3%。激发发射矩阵(EEM)和傅里叶变换红外(FTIR)结果表明,不同 MWCO 截留液的保留物质相似,主要由类蛋白物质和可溶微生物产物组成。RO 系统中关键少数组分的影响值得进一步探讨。