School of Civil and Environmental Engineering, University of Technology, Sydney, Post Box 129, Broadway, NSW 2007, Australia.
School of Civil and Environmental Engineering, University of Technology, Sydney, Post Box 129, Broadway, NSW 2007, Australia; College of Environmental Science and Engineering, State Environmental Protection Engineering Center for Pollution Treatment and Control in Textile Industry, Donghua University, Shanghai 201620, China.
Bioresour Technol. 2017 Sep;240:50-58. doi: 10.1016/j.biortech.2017.03.069. Epub 2017 Mar 14.
The present study investigated the performance of an integrated osmotic and microfiltration membrane bioreactor system for wastewater treatment employing baffles in the reactor. Thus, this reactor design enables both aerobic and anoxic processes in an attempt to reduce the process footprint and energy costs associated with continuous aeration. The process performance was evaluated in terms of water flux, salinity build up in the bioreactor, organic and nutrient removal and microbial activity using synthetic reverse osmosis (RO) brine as draw solution (DS). The incorporation of MF membrane was effective in maintaining a reasonable salinity level (612-1434mg/L) in the reactor which resulted in a much lower flux decline (i.e. 11.48-6.98LMH) as compared to previous studies. The stable operation of the osmotic membrane bioreactor-forward osmosis (OMBR-FO) process resulted in an effective removal of both organic matter (97.84%) and nutrient (phosphate 87.36% and total nitrogen 94.28%), respectively.
本研究采用挡板在反应器中考察了集成渗透和微滤膜生物反应器系统处理废水的性能。因此,这种反应器设计能够同时进行好氧和缺氧过程,试图减少与连续曝气相关的工艺占地面积和能源成本。该工艺采用合成反渗透(RO)盐水作为汲取液(DS),从水通量、生物反应器中盐度的积累、有机物和营养物去除以及微生物活性等方面评估了其性能。微滤膜的加入有效地维持了反应器中合理的盐度水平(612-1434mg/L),与以前的研究相比,通量下降幅度要小得多(即 11.48-6.98LMH)。渗透膜生物反应器-正向渗透(OMBR-FO)工艺的稳定运行分别实现了有机物(97.84%)和营养物(87.36%的磷酸盐和 94.28%的总氮)的有效去除。