School of Chemistry, Chemical and Environmental Technology Section, Aristotle University of Thessaloniki, Box 116, 54124, Thessaloniki, Greece.
Environ Sci Pollut Res Int. 2018 May;25(13):12274-12283. doi: 10.1007/s11356-017-0142-8. Epub 2017 Sep 13.
This study investigates the hydraulic performance and the fouling characteristics of a bench-scale membrane sequencing batch reactor (MSBR), treating mature landfill leachate under various time-based operating conditions. The MSBR system operated initially under a high-flux condition (Period 1) which resulted in a rapid trans-membrane pressure (TMP) rise due to intense fouling. Following the characterization of Period 1 as super-critical, the system was subsequently operated under a near-critical condition (Period 2). The overall filtration resistance analysis showed that cake layer formation was the dominant fouling mechanism during Period 1, contributing to 85.5% of the total resistance. However, regarding the MSBR operation during Period 2, adsorption was found to also be a dominant fouling mechanism (Days 1 to 47), contributing to 29.1% of the total resistance. Additionally, the irregular total resistance variation, which was observed during the subsequent operation (Days 48 to 75), and the respective filtration resistance analysis suggested also the formation of an initial sludge cake layer on the membrane surface, contributing to the 47.7% of the total resistance.
本研究考察了在不同时间操作条件下,处理成熟垃圾渗滤液的中试规模膜序批式反应器(MSBR)的水力性能和污染特性。MSBR 系统最初在高通量条件下运行(第 1 期),由于强烈的污染,导致跨膜压力(TMP)迅速上升。在第 1 期被表征为超临界后,系统随后在近临界条件下运行(第 2 期)。总的过滤阻力分析表明,在第 1 期,滤饼层的形成是主要的污染机制,占总阻力的 85.5%。然而,对于第 2 期的 MSBR 运行,发现吸附也是一种主要的污染机制(第 1 天至第 47 天),占总阻力的 29.1%。此外,在随后的运行(第 48 天至第 75 天)中观察到不规则的总阻力变化,以及相应的过滤阻力分析表明,在膜表面也形成了初始的污泥滤饼层,占总阻力的 47.7%。