Department of Civil and Environmental Engineering, Michigan State University, East Lansing, MI 48824, USA.
Department of Civil and Environmental Engineering, Michigan State University, East Lansing, MI 48824, USA.
Water Res. 2016 Jan 1;88:750-757. doi: 10.1016/j.watres.2015.10.066. Epub 2015 Nov 7.
Pressure relaxation and permeate backwash are two commonly used physical methods for membrane fouling mitigation in membrane bioreactor (MBR) systems. In order to assess the impact of these methods on virus removal by MBRs, experiments were conducted in a bench-scale submerged MBR treating synthetic wastewater. The membranes employed were hollow fibers with the nominal pore size of 0.45 μm. The experimental variables included durations of the filtration (tTMP>0), pressure relaxation (tTMP=0) and backwash (tTMP<0) steps. Both pressure relaxation and permeate backwash led to significant reductions in removal of human adenovirus (HAdV). For the same value of tTMP>0/tTMP=0, longer filtration/relaxation cycles (i.e. larger tTMP+tTMP=0) led to higher transmembrane pressure (TMP) but did not have a significant impact on HAdV removal. A shorter backwash (tTMP<0 = 10 min) at a higher flow rate (Q = 40 mL/min) resulted in more substantial decreases in TMP and HAdV removal than a longer backwash (tTMP<0 = 20 min) at a lower flow rate (Q = 20 mL/min) even though the backwash volume (QtTMP<0) was the same. HAdV removal returned to pre-cleaning levels within 16 h after backwash was applied. Moderate to strong correlations (R(2) = 0.63 to 0.94) were found between TMP and HAdV removal.
压力松弛和渗透反洗是膜生物反应器(MBR)系统中两种常用的减轻膜污染的物理方法。为了评估这些方法对 MBR 去除病毒的影响,在处理合成废水的中试浸没式 MBR 中进行了实验。所使用的膜是标称孔径为 0.45 μm 的中空纤维。实验变量包括过滤(tTMP>0)、压力松弛(tTMP=0)和反洗(tTMP<0)步骤的持续时间。压力松弛和渗透反洗都会导致人腺病毒(HAdV)去除率显著降低。对于相同的 tTMP>0/tTMP=0 值,较长的过滤/松弛周期(即较大的 tTMP+tTMP=0)会导致更高的跨膜压力(TMP),但对 HAdV 去除率没有显著影响。在较高的流速(Q=40mL/min)下进行较短的反洗(tTMP<0=10min)比在较低的流速(Q=20mL/min)下进行较长的反洗(tTMP<0=20min)会导致 TMP 和 HAdV 去除率更大幅度的降低,尽管反洗体积(QtTMP<0)相同。反洗后 16 小时内,HAdV 去除率恢复到清洗前的水平。TMP 和 HAdV 去除率之间存在中度至强相关性(R²=0.63 至 0.94)。