Ranieri Ezio, Goffredo Vito, Campanella Mariachiara, Falk Michael W
DICATECh, Politecnico di Bari - Via Orabona, 4, 70125 Bari, Italy E-mail:
HDR Engineering, 2365 Iron Point Road, Suite 300, Folsom, CA 95630, USA.
Water Sci Technol. 2016;73(9):2222-30. doi: 10.2166/wst.2016.071.
A flux-step method was used for monitoring the pressure variation in a solids separation membrane at different operating conditions. A submerged membrane bioreactor pilot plant, used during the short-term tests, was used to purify actual restaurant wastewater. The influence of membrane backwash and relaxation on the variation of pressure variation was also evaluated. In order to reduce the deposition of irreversible fouling, the authors modified the literature-supported filtration to backwash cycling with filtration and relaxation cycling. The trials maintained a constant filtration to relaxation ratio that was in line with optimal filtration to backwashing ratios found in the literature. The relaxation cycling between two constant flux-steps effectively counteracted membrane fouling and the excessive decrease in average pressure, and it results in a lower waste of energy and water than a backwashing strategy.
采用通量步长法监测固体分离膜在不同运行条件下的压力变化。短期试验期间使用的浸没式膜生物反应器中试装置用于净化实际的餐饮废水。还评估了膜反冲洗和松弛对压力变化的影响。为了减少不可逆污染的沉积,作者将文献支持的过滤修改为过滤与反冲洗循环以及松弛循环。试验保持恒定的过滤与松弛比,该比例与文献中发现的最佳过滤与反冲洗比一致。在两个恒定通量步长之间的松弛循环有效地抵消了膜污染和平均压力的过度下降,并且与反冲洗策略相比,它导致更低的能量和水的浪费。