Department of Municipal Engineering, School of Civil Engineering, Hefei University of Technology, Hefei, 230009, China.
State Key Laboratory of Separation Membranes and Membrane Processes, School of Environmental and Chemical Engineering, Tianjin Polytechnic University, Tianjin, 300387, China.
Environ Sci Pollut Res Int. 2019 Nov;26(33):34167-34176. doi: 10.1007/s11356-018-3802-4. Epub 2018 Nov 27.
Although anaerobic membrane bioreactor (AnMBR) has been proposed for the treatment of phenolic wastewater, the membrane fouling is still a major obstacle. The effects of dosing of granular activated carbon (GAC) and polyaluminum chloride (PACl) on the treatment performance and membrane fouling of anaerobic ceramic membrane bioreactor were investigated for treating phenol- and quinoline-containing wastewater. The results suggested that the one-off dosing of GAC resulted in a decrease of protein/carbohydrate ratio, which might account for the aggravation of membrane fouling alongside with the decreased flocs size. Nevertheless, the substrate uptake rates (SUR) of phenol and quinoline, and the specific methanogenic activity of sludge at the GAC dosing stage of experimental reactor (R1) were 8.79 ± 0.63 mg phenol g MLVSS d, 7.01 ± 0.09 mg quinoline g MLVSS d and 0.27 ± 0.01 g COD g MLVSS d, which were 1.69, 3.59 and 1.93 times higher than that of the control reactor (R2). The dosing of PACl reduced the membrane fouling rate by changing the floc structure of sludge, as well as the component of SMP and EPS. However, the substrate uptake rate of quinoline was declined. This work provides a comprehensive evaluation on the effect of GAC and PACl dosing on membrane fouling and performance of anaerobic ceramic membrane bioreactor treating phenol-and quinoline-containing wastewater.
尽管厌氧膜生物反应器(AnMBR)已被提议用于处理含酚废水,但膜污染仍然是一个主要障碍。本研究考察了投加颗粒活性炭(GAC)和聚合氯化铝(PACl)对处理含酚和喹啉废水的厌氧陶瓷膜生物反应器处理性能和膜污染的影响。结果表明,GAC 的一次性投加导致蛋白质/碳水化合物比降低,这可能是膜污染加剧的原因,同时也导致絮体粒径减小。然而,在实验反应器(R1)的 GAC 投加阶段,酚和喹啉的基质摄取速率(SUR)和污泥的比甲烷活性分别为 8.79 ± 0.63 mg 酚 g MLVSS d、7.01 ± 0.09 mg 喹啉 g MLVSS d 和 0.27 ± 0.01 g COD g MLVSS d,分别是对照反应器(R2)的 1.69、3.59 和 1.93 倍。PACl 的投加通过改变污泥的絮体结构以及 SMP 和 EPS 的成分来降低膜污染速率。然而,喹啉的基质摄取速率下降。本工作全面评价了 GAC 和 PACl 投加对处理含酚和喹啉废水的厌氧陶瓷膜生物反应器膜污染和性能的影响。